WorldWideScience

Sample records for finned tube performance

  1. Airside performances of finned eight-tube heat exchangers

    Science.gov (United States)

    Li, Cheng; Li, Junming

    2016-11-01

    For applications in the relatively low temperature refrigeration systems with large constant temperature bath, the present work performed the experimental studies on the airside performances of the staggered finned eight-tube heat exchangers with large fin pitches. The airside heat transfer coefficients and pressure drops for three fin types and two fin pitches are obtained and analyzed. The heat transfer enhancement with louver fins is 11-16 % higher than the flat fins and that with sinusoidal corrugated fins is 1.1-3.4 % higher than the flat fins. Higher Re brings larger enhancement for various fins. Fin pitches show weak influence on heat transfer for eight tube rows. However, effects of fin pitch on heat transfer for both the sinusoidal corrugation and the louvered fin are larger than the flat fins and they are different from those for N ≤ 6. Airside Colburn j factor are compared with previous and it could be concluded that the airside j factor is almost constant for finned tube heat exchangers with eight tubes and large fin pitches, when Re is from 250 to 2500. The results are different from previous studies for fewer tube rows.

  2. Performance study of a fin and tube heat exchanger with different fin geometry

    OpenAIRE

    2016-01-01

    This study analyses the effect of different fin geometries on the heat transfer and pressure loss characteristics of a fin and tube heat exchanger. A numerical investigation is carried out on liquid–gas type double-finned tube heat exchanger under cross-flow condition. Three different cross-sections namely: a) Rectangular, b) Trapezoidal, c) Triangular are adopted to define the fin geometry. The CFD simulations are performed to incorporate coupled steady state conjugate heat transfer with the...

  3. Performance study of a fin and tube heat exchanger with different fin geometry

    DEFF Research Database (Denmark)

    Singh, Shobhana; Sørensen, Kim; Condra, Thomas Joseph

    2016-01-01

    This study analyses the effect of different fin geometries on the heat transfer and pressure loss characteristics of a fin and tube heat exchanger. A numerical investigation is carried out on liquid–gas type double-finned tube heat exchanger under cross-flow condition. Three different cross......-sections namely: a) Rectangular, b) Trapezoidal, c) Triangular are adopted to define the fin geometry. The CFD simulations are performed to incorporate coupled steady state conjugate heat transfer with the turbulent flow phenomenon for the Reynolds number in the range of 5000-13000. Dimensionless heat transfer...... models show that triangular fin geometry can provide higher heat transfer performance in comparison to the fins with rectangular and trapezoidal geometry with lower pressure loss and a bonus of 7.27% reduction in weight under similar operating conditions....

  4. Finned tubes for heat exchangers: Characterization and performance simulation

    Energy Technology Data Exchange (ETDEWEB)

    Armand, J.-L.; Molle, N. (Centre Tecnique des Industries Aerauliques et Thermiques (CETIAT), 75 Paris (France))

    1992-06-01

    Relevant to air conditioning applications, the state-of-the-art of finned tube heat exchanger design is reviewed. The review covers the key design, performance and operation characteristics, as well as, principal heat transfer correlations for exchangers adopting 'dry' (without condensation) and 'wet' operation. External side heat transfer and pressure drop calculation methods are established for the characterization of external surfaces. For internal surfaces, correlations are given for two-phase flow and pressure drop. Reference is made to the NTU and CANUT simulation codes for the determination of optimum finned tube geometries for standard and particular operating conditions.

  5. Performance study of a fin and tube heat exchanger with different fin geometry

    DEFF Research Database (Denmark)

    Singh, Shobhana; Sørensen, Kim; Condra, Thomas Joseph

    2016-01-01

    This study analyses the effect of different fin geometries on the heat transfer and pressure loss characteristics of a fin and tube heat exchanger. A numerical investigation is carried out on liquid–gas type double-finned tube heat exchanger under cross-flow condition. Three different cross......-sections namely: a) Rectangular, b) Trapezoidal, c) Triangular are adopted to define the fin geometry. The CFD simulations are performed to incorporate coupled steady state conjugate heat transfer with the turbulent flow phenomenon for the Reynolds number in the range of 5000-13000. Dimensionless heat transfer...... and pressure loss characteristics such as Nusselt number, Euler number, and efficiency index are determined and utilized to compare the performance of different fin geometries. The results obtained from the models are verified using experimentally developed correlations. The results obtained from the numerical...

  6. Performance Evaluation of Plate-Fin-And Tube Heat Exchanger with Wavy Fins- A Review

    Directory of Open Access Journals (Sweden)

    Sandip S. Kale

    2014-09-01

    Full Text Available The plate fin-and-tube heat exchangers are widely used in variety of industrial applications, particularly in the heating, air-conditioning and refrigeration, HVAC industries. In most cases the working fluid is liquid on the tube side exchanging heat with a gas, usually air. It is seen that the performance of heat exchangers can be greatly increased with the use of unconventionally shaped flow passages such as plain, perforated offset strip, louvered, wavy, vortex generator and pin. The current study is focused on wavy-fin. The wavy surface can lengthen the path of airflow and cause better airflow mixing. In order to design better heat exchangers and come up with efficient designs, a thorough understanding of the flow of air in these channels is required. Hence this study focuses on the heat transfer and friction characteristics of the air side for wavy fin and tube heat exchanger.

  7. Performance Prediction of Cross-Finned Tube Heat Exchangers

    Science.gov (United States)

    Kondou, Chieko; Senshu, Takao; Oguni, Kensaku

    The plane fin of a cross-finned tube heat exchangers is the basis for all kinds of fins used in air conditioners. In this paper, an improvement the dimensionless arrangements of pressure drop for plane fins was attempted. The detailed calculation results for all geometrical parameters, especially tube disposition, showed the reflecting to the effect of contracted flow in the existing equations of friction factor is insufficient. Therefore, an amendment for these equations was suggested. Further, the analogy between the revised friction factor and the Colburn's j factor was verified. In addition an approximate expression for the fin efficiency using wide parameters was devised.

  8. Performance Prediction of Cross-finned Tube Heat Exchangers

    Science.gov (United States)

    Kondou, Chieko; Senshu, Takao; Matsumura, Kenji; Oguni, Kensaku

    An important issue in heat pumps is increasing their efficiency, in order to achieve a significant optimization for heat exchangers. Techniques to simulate the flow length averaged heat transfer coefficient and static pressure drop through the flow passage are presented in this paper. In addition, an analytical evaluation of the cost reduction for a cross-fined tube heat exchanger of outdoor heat pump units is instantiated. The dimensionless factors, Colburn's factor j and Fanning's friction factor f, express the heat transfer performance and frictional characteristics, as a function of Reynolds number. These depend on slit possession, an original parameter used in this study. Further, this paper describes an approximate expression of the fin efficiency, which can be used for to survey the fin parameters. The above three concepts were necessary to forecast the performance on the airside. In the results, the cost minimum point was obtained with a comparable performance.

  9. The Effects of Fin Collar Form on Heat Transfer Performance of Cross Fin-tube Heat Exchanger

    Science.gov (United States)

    Tsubaki, Koutaro; Miyara, Akio; Nagai, Yuma; Sasaki, Naoe; Mizuta, Yoshihiko

    A numerical study has been conducted to investigate effects of fin collar form of cross fin-tube heat exchangers on heat transfer performance. Two adjacent fin collars and a copper tube form a triangular space during the making process. And also end of the fin collar protrudes into air-side. The protruded end and triangular space affect on air-side heat convection and thermal resistance between the tube and fin collars, respectively. The increase in triangular space increases non-contact surface area between tube and fin collar, which affects to decrease heat transfer rate. The protruded end disturbs air-side flow and expands the surface of the fin collar. As a result of these two effects, heat transfer rate from the heat transfer tube increases. However, protruded end increases pressure loss of air-side.

  10. Performance Characteristics of Cross-Fin-Tube-Type Heat Exchanger for Air Conditioner

    Science.gov (United States)

    Sasaki, Naoe; Kakiyama, Shiro; Sanuki, Noriyoshi

    The effects of enhanced heat transfer tube with ability to control the heat transfer disturbance by mechanical tube expanding were experimentally investigated on the performance characteristics of air-cooled cross-fin-tube-type heat exchanger for air conditioner. Three kinds of the enhanced heat transfer tube were developed and used in the experiment. The enhanced heat transfer tube was a kind of spirally grooved tube and composed with the fins smaller than those of the conventional spirally grooved tube excepting four fins located in orthogonal position on the tube circumference. The optimum groove number to enhance the performance of heat exchanger was also shown.

  11. Parametric analysis of the performance of internally finned tubes for heat exchanger application

    Energy Technology Data Exchange (ETDEWEB)

    Webb, R.L.; Scott, M.J.

    1980-02-01

    This paper presents a parametric analysis of the performance of internally finned tubes in turbulent forced convection for application to heat exchangers. The analysis compares the performance of an internally finned tube exchanger with that of an exchanger having internally smooth tubes. The calculations are performed for three important design cases.

  12. Parametric CFD Analysis to Study the Influence of Fin Geometry on the Performance of a Fin and Tube Heat Exchanger

    DEFF Research Database (Denmark)

    Singh, Shobhana; Sørensen, Kim; Condra, Thomas Joseph

    2016-01-01

    Heat transfer and pressure loss characteristics of a fin and tube heat exchanger are numerically investigated based on parametric fin geometry. The cross-flow type heat exchanger with circular tubes and rectangular fin profile is selected as a reference design. The fin geometry is varied using...... a design aspect ratio as a variable parameter in a range of 0.1-1.0 to predict the impact on overall performance of the heat exchanger. In this paper, geometric profiles with a constant thickness of fin base are studied. Three-dimensional, steady state CFD model is developed using commercially available...... are determined. The best performed geometric fin profile based on the higher heat transfer and lower pressure loss is predicted. The study provides insights into the impact of fin geometry on the heat transfer performance which help escalate the understanding of heat exchanger designing and manufacturing...

  13. Experimental and numerical investigation to evaluate the performance of triangular finned tube heat exchanger

    OpenAIRE

    Vinous M. Hameed, Bashar Muslem Essa

    2015-01-01

    Experimental and numerical investigation has been performed in this work to evaluate the performance for triangular finned tube heat exchanger. Experimental work included designing and manufacturing of shaped triangular fins from copper material of (10mm) length, (10mm) height, (1mm) thickness, (22 mm) distance between every two fins shaped and (15mm) pitch between each two of fins which are install on the straight copper tube of (2m) length having (20mm) inner diameter and (22mm) outer diame...

  14. Determination of fin pitches for maximum performance index of L-footed spiral fin-and-tube heat exchangers

    OpenAIRE

    2015-01-01

    In this study, the fin pitches of L-footed spiral finned tube heat exchangers were determined for maximimum performance index. The experiments were done at various fin pitches (fp = 2.4, 3.2, and 4.2 mm) under the range of high Reynolds numbers (5,000–15,000). The test sections had a parallel and counter cross-flow arrangement having the number of tube row of 2. The two working fluids were the ambient air and hot water. The performance indexes (ζ1, ζ2, and ζ3) were used to analyze the experim...

  15. Performance of residential air-conditioning systems with flow maldistribution in fin-and-tube evaporators

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Brix, Wiebke; Elmegaard, Brian;

    2011-01-01

    Refrigerant and airflow maldistribution in fin-and-tube evaporators for residential air-conditioning was investigated with numerical modeling. Fin-and-tube heat exchangers usually have a pre-defined circuitry. However, the objective in this study was to perform a generic investigation of each...

  16. Computational analysis of heat transfer and pressure drop performance for internally finned tubes with three different longitudinal wavy fins

    Energy Technology Data Exchange (ETDEWEB)

    Wang, Qiu-Wang; Lin, Mei; Zeng, Min; Tian, Lin [Xi' an Jiaotong University, State Key Laboratory of Multiphase Flow in Power Engineering, Xi' an, Shaanxi (China)

    2008-12-15

    Turbulent pressure drop and heat transfer characteristics in tubes with three different kinds of internally longitudinal fin patterns (interrupted wavy, sinusoidal wavy and plain) are numerically investigated for Re=904-4,520. The channel velocity, temperature, and turbulence fields are obtained to discern the mechanisms of heat transfer enhancement. Numerical results indicate that the steady and spatially periodic growth and disruption of cross-sectional vortices occur near the tube/fin walls along the streamwise locations. The thermal boundary layers near the tube/fin surfaces are thereby periodically interrupted, with heat transfer near the recirculation zones being enhanced. The overall heat transfer coefficients in wavy channels are higher than those in a plain fin channel, while with larger pressure drop penalties. At the same waviness, the interrupted wavy fin tube could enhance heat transfer by 72-90%, with more than 2-4 times of pressure drop penalty. Among the fins studied, the sinusoidal wavy fin has the best comprehensive performance. (orig.)

  17. Experimental and numerical investigation to evaluate the performance of triangular finned tube heat exchanger

    Directory of Open Access Journals (Sweden)

    Vinous M. Hameed, Bashar Muslem Essa

    2015-01-01

    Full Text Available Experimental and numerical investigation has been performed in this work to evaluate the performance for triangular finned tube heat exchanger. Experimental work included designing and manufacturing of shaped triangular fins from copper material of (10mm length, (10mm height, (1mm thickness, (22 mm distance between every two fins shaped and (15mm pitch between each two of fins which are install on the straight copper tube of (2m length having (20mm inner diameter and (22mm outer diameter. The inner tube is inserted inside the Perspex tube of (54mm inner diameter and (60mm outer diameter. Cold Air and hot water are used as working fluids in the shell side and tube side, respectively. Air at various mass flow rates (0.001875 to 0.003133 kg/sec flows through annuli and water at Reynold's numbers ranging from (10376.9 to 23348.03 flows through the inner tube. Performance of (smooth and finned tube heat exchanger was investigated experimentally. Experimental results showed that the enhancement of heat dissipation for triangular finned tube is (3.252 to4.502 times than that of smooth tube respectively. Numerical simulation has been carried out on present heat exchanger to analyze flow field and heat transfer using COMSOL computational fluid dynamic (CFD package model. The comparison between experimental work and numerical results showed good agreement.

  18. The fin design for small-diameter tube and performance evaluation method

    Energy Technology Data Exchange (ETDEWEB)

    Fan, J.F.; Wu, Z.G.; He, Y.L.; Tao, W.Q. [Xi' an Jiaotong Univ., Xi' an (China). School of Energy and Power Engineering

    2010-07-01

    The heat transfer and friction characteristics of heat exchangers were investigated in order to improve the overall performance of heat exchangers, including a reduction in size and energy conservation. This paper proposed a simple but efficient performance comparison method based on the assumptions of constant properties and identical frontal area. An orthogonal design method proposed by Taguchi was used to reduce the number of computational cases, but still obtain nearly optimum combination of major geometric factors. The equations for constructing a plot for comparison of in-designing surface were derived and then the Taguchi method was used to find a nearly-optimum structure. A new slotted fin with tubes of 4 mm was then proposed to replace the original louvered fin with tubes of 7 mm. The reasonable parametric combination of global parameters was obtained by analyzing the numerical results of 16 plain plate fins. Three new slotted fins with different fin pitch were proposed. The slotted fin with fin pitch of 1.4 mm was recommended after considering the heat transfer, comprehensive performance, and cost of material and operation. The results showed that compared to the original louvered fin, the heat transfer rate of the recommended fin increased by 2.2, 22.5 and 13.7 per cent under identical flow rate, identical pressure drop and identical pumping power constraint, respectively. The new fin design also saved on the use of copper tubing material by about 36 per cent. 25 refs., 2 tabs., 10 figs.

  19. Study on turbulent flow and heat transfer performance of tubes with internal fins in EGR cooler

    Science.gov (United States)

    Liu, Lin; Ling, Xiang; Peng, Hao

    2015-01-01

    In this paper, flow and heat transfer performances of the tubes with internal longitudinal fins in Exhaust Gas Recirculation (EGR ) cooler were investigated by three-dimension computation and experiment . Each test tube was a single-pipe structure, without inner tube. Three-dimension computation was performed to determine the thermal characteristics difference between the two kinds of tubes, that is, the tube with an inner solid staff as a blocked structure and the tube without the blocked structure. The effects of fin width and fin height on heat transfer and flow are examined. For proving the validity of numerical method, the calculated results were compared with corresponding experimental data. The tube-side friction factor and heat transfer coefficient were examined. As a result, the maximum deviations between the numerical results and the experimental data are approximately 5.4 % for friction factor and 8.6 % for heat transfer coefficient, respectively. It is found that two types of internally finned tubes enhance significantly heat transfer. The heat transfer of the tube with blocked structure is better, while the pressure drop of the tube without blocked structure is lower. The comprehensive performance of the unblocked tube is better to applied in EGR cooler.

  20. Performance investigation of evaporatively-cooled heat exchangers - part one: plain and finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Hasan, A.; Siren, K.

    2004-07-01

    The performance of two evaporatively cooled heat exchangers is investigated under similar operating conditions of airflow rates and inlet hot water temperatures. The types of the heat exchangers are plain and plate-finned circular tube which occupy the same volume. A substantial increase in heat transfer takes place for the plate-finned tubes. The increase is 92-140% for air velocities from 1.66 to 3.57 m s{sup -1}. The wet-finned surfaces show low fin efficiency compared with dry surfaces. An energy index defined as the ratio of volumetric thermal conductance to air pressure drop per unit length is found to be close for the two heat exchangers. This reveals higher thermal utilisation of the occupied volume by the finned tubes with the same energy index. (orig.)

  1. Thermal-hydraulic performance of novel louvered fin using flat tube cross-flow heat exchanger

    Institute of Scientific and Technical Information of China (English)

    Junqi DONG; Jiangping CHEN; Zhijiu CHEN

    2008-01-01

    Experimental studies were conducted to investigate the air-side heat transfer and pressure drop characteristics of a novel louvered fins and flat tube heat exchangers. A series of tests were conducted for 9 heat exchangers with different fin space and fin length, at a constant tube-side water flow rate of 2.8 m/h. The air side thermal performance data were analyzed using the effectiveness-NTU method. Results were presented as plot of Colburn j factor and friction factor f against the Reynolds number in the range of 500-6500. The characteristics of the heat transfer and pressure drop of different fin space and fin length were analyzed and compared. In addition, the curves of the heat transfer coefficients vs. pumping power per unit heat transfer area were plotted. Finally, the area optimization factor was used to evaluate the thermal hydraulic performance of the louvered fins with differential geometries. The results showed that the j and ffactors increase with the decrease of the fin space and fin length, and the fin space has more obvious effect on the thermal hydraulic characteristics of the novel louvered fins.

  2. Indoor test for thermal performance evaluation of seven Elcam fin-tube solar collector configurations

    Science.gov (United States)

    1979-01-01

    The test procedure used and the results obtained from an evaluation test program conducted to obtain thermal performance data on seven Elcam fin-tube solar collector configurations under simulated conditions are described. These tests were made using the Marshall Space Flight Center solar facilities. The Elcam fin-tube (liquid) solar collectors each consist of an absorber plate 5.9 inches wide by 83 inches long and a type M copper tube of 0.569 inch nominal inside diameter. No cover plate was used with any of the specimens. The uniqueness of each of the seven configurations is described, and tests were performed on each separate configuration.

  3. Effect of Fin-Collar Shape at Contact Area between Tube and Fin on Heat Exchanger Performance

    Science.gov (United States)

    Matsuo, Yoshimi; Tsubaki, Koutaro; Miyara, Akio

    In this study, numerical simulation of a cross fin-tube heat exchanger was conducted to investigate the effects of fin-collar shape on the heat transfer performance and pressure drop. During the making process, two adjacent fin-collars and a tube form a triangular space and the end of fin collar protrude to air side. To investigate these effects on the heat exchanger performance, the form ratio was defined to make an indicator of the triangular space size. Furthermore, the simulation of the models with and without protruded end was conducted. The results indicated that the increase of the form ratio results in the decrease in the heat transfer rate. On the other hand, it contributed to a relatively small increase in the heat transfer coefficient on the air side. A high heat transfer coefficient on the air side was obtained by the protruded fin-collar end. However, the pressure drop was not much different between the models with and without the protruded end. The ratio of the thermal contact resistance to the air side thermal resistance was about 1:5 for the form ratio of 20% to 40%.

  4. An improved model for predicting performance of finned tube heat exchanger under frosting condition, with frost thickness variation along fin

    Energy Technology Data Exchange (ETDEWEB)

    Tso, C.P. [Multimedia University, Jalan Ayer Keroh Lama, Melaka (Malaysia). Faculty of Engineering and Technology; Cheng, Y.C.; Lai, A.C.K. [Nanyang Technological University, Singapore (Singapore). School of Mechanical and Aerospace Engineering

    2006-01-15

    Frost accumulation on a heat exchanger, a direct result of combined heat and mass transfer between the moist air flowing across a cold surface, causes heat transfer performance degradation due to the insulating effect of frost layer and the coil blockage as the frost grows. The complex geometry of finned tube heat exchangers leads to uneven wall and air temperature distribution inside the coil, and causes variations of frost growth rate and densification along the coil. In this study, a general distributed model with frost formation was developed. The equations for finned tube heat exchanger were derived in non-steady-state manner and quasi-steady state in the frost model. In order to make the model more realistic, the variation of frost along fin due to uneven temperature distribution was included. The presented model is able to predict the dynamic behavior of an air cooler both under non-frost and frost condition. Comparisons were made based on the frost mass accumulation, pressure drop across coil and energy transfer coefficient, and results were found to agree well with reported experimental results. (author)

  5. Investigations on the heat transfer performance of edge-shaped finned-tubes

    Science.gov (United States)

    Wang, Xiao-wu; Wan, Zhen-ping; Tang, Yong

    2014-09-01

    The third generation enhanced heat transfer technologies, such as three-dimensional fin and dimple, are still important means of improving energy efficiency and will continue to be challenging issues. This paper concentrates on the analysis of the condensation heat transfer performance of an edge-shaped finned-tube fabricated by extrusion-ploughing process. Experimental results show that the overall heat transfer coefficient increases with increases of volumetric flow rate of cold water and heat flux whereas the shell side heat transfer coefficient decreases with volumetric flow rate and heat flux increasing. At the similar volumetric flow rate, the shell side heat transfer coefficient of the edge-shaped finned-tube is 4-6 times larger than that of the smooth tube. At the similar volumetric flow rate, the shell side heat transfer coefficient of edge-shaped finned-tube increases with ploughing depth increasing. At the same temperature difference between wall and vapor, the shell side heat transfer coefficient is also higher than what had been reported in the literature.

  6. A numerical analysis on heat transfer performance from various gap size between finned tube module and side-wall in finned tube evaporator

    Energy Technology Data Exchange (ETDEWEB)

    Lee, Soo Yoon; Shin, Seung Won [Hongik Univ, Seoul (Korea, Republic of); Ahn, Joon [Korea Institute of Energy Research, Daejeon (Korea, Republic of)

    2009-07-01

    Recently, Heat Recovery Steam Generator(HRSG) is widely used in various commercial places such as hospital, restaurant, and sauna for steam generation equipment due to increasing demand on steam usage for disinfection or fumigation. In HRSG, finned tube type evaporator is usually utilized to enhance heat transfer performance for higher steam generation. Most previous research so far has been focused on heat transfer enhancement aspect from geometry of each individual fin such as pitch distance, length, and thickness. In current study, we have tried to identify the effect from gap size between tube module and side wall on overall heat transfer. We found out that the gap size has considerable effect on total heat transfer rate. We also observed that both heat transfer performance and pressure drop is decreasing with increasing gas size.

  7. Dry and wet air-side performance of a louver-finned heat exchanger having flat tubes

    Energy Technology Data Exchange (ETDEWEB)

    Kim, Nae Hyun; Kim, Soo Hwan [University of Incheon, Incheon (Korea, Republic of)

    2010-07-15

    A louver-finned flat tube heat exchanger was tested, and the data are compared with those of the state-of-the-art round tube heat exchanger. Both heat exchangers have the same tube perimeter and fin pitch. Tests were conducted under dry and wet condition. Results show that, under dry condition, both j and f factors of the round tube heat exchanger are larger than those of the flat tube heat exchanger. As the Reynolds number decreases, however, the j and f factors of the flat tube heat exchanger increase at steeper slopes than those of the round tube heat exchanger. Under wet condition, contrary to the dry surface, both j and f factors of the flat tube heat exchanger are larger than those of the round tube heat exchanger. Explanation is provided considering the condensate drainage between louvers and fins. Performance evaluation was also performed

  8. Fin-tube solar collectors

    Science.gov (United States)

    1980-01-01

    Report presents test procedures and results of thermal-performance evaluation of seven commercial fin tube (liquid) solar collector-absorber plates. Tests were conducted indoors at Marshall Space Flight Center Solar simulator. Results are graphically shown along with supporting test data and summary, indicating efficiency as function of collector inlet temperature.

  9. An engineering procedure for air side performance evaluation of flat tube heat exchangers with louvered fins

    Science.gov (United States)

    Antonijevic, Dragi

    2013-01-01

    An accurate evaluation of possible air side heat transfer surface geometries is a prerequisite for optimal heat exchanger design. Aiming for practical engineering applicability a simplified and transparent analytical procedure for the assessment of louvered fin and flat tube heat exchanger geometries and the calculation of fin parameters that enable maximal performance for given boundary conditions has been developed. The proposed method comprises determining fins temperature profiles and effective heat transfer temperature difference, introduction of a relative heat transfer surface area, as well as the utilization of recent experimentally obtained heat transfer correlations confirmed for the observed range of boundary conditions. The proposed methodology is validated through comparison with experimental and numerical results of other authors.

  10. Effects of Tube Diameter and Tubeside Fin Geometry on the Heat Transfer Performance of Air-Cooled Condensers

    Science.gov (United States)

    Wang, H. S.; Honda, Hiroshi

    A theoretical study has been made on the effects of tube diameter and tubeside fin geometry on the heat transfer performance of air-cooled condensers. Extensive numerical calculations of overall heat transfer from refrigerant R410A flowing inside a horizontal microfin tube to ambient air were conducted for a typical operating condition of the air-cooled condenser. The tubeside heat transfer coefficient was calculated by applying a modified stratified flow model developed by Wang et al.8). The numerical results show that the effects of tube diameter, fin height, fin number and helix angle of groove are significant, whereas those of the width of flat portion at the fin tip, the radius of round corner at the fin tip and the fin half tip angle are small.

  11. A COMPARISON OF HEAT TRANSFER AROUND A SINGLE SERRATED FINNED TUBE AND A PLAIN FINNED TUBE

    Directory of Open Access Journals (Sweden)

    S.R.Mcilwain

    2010-02-01

    Full Text Available With comparable bundle geometry, serrated fin finned tube heat exchangers transfer more heat than plain finned ones. There are believed to be many factors in this behaviour, and this investigation used CFD to examine the heat transfer and fluid flow patterns around the fins to try to understand the magnitude of the differences in the processes. The study is a first step in developing a new theory-based method to predict the performance of serrated fin tube bundles.

  12. A COMPARISON OF HEAT TRANSFER AROUND A SINGLE SERRATED FINNED TUBE AND A PLAIN FINNED TUBE

    OpenAIRE

    2010-01-01

    With comparable bundle geometry, serrated fin finned tube heat exchangers transfer more heat than plain finned ones. There are believed to be many factors in this behaviour, and this investigation used CFD to examine the heat transfer and fluid flow patterns around the fins to try to understand the magnitude of the differences in the processes. The study is a first step in developing a new theory-based method to predict the performance of serrated fin tube bundles.

  13. Finned tubes decide performance. A closer look at water coolers. Wasserkuehlsaetze unter der Lupe: Auf die Rippenrohre kommt es an

    Energy Technology Data Exchange (ETDEWEB)

    Menze, K.W.; Webb, R.L.; Apparao, T. (Pennsylvania State Univ., University Park (USA))

    1989-05-01

    The performance of standard and high-efficiency finned tubes in 800 kW water coolers was compared experimentally. Details are given of the dual-flow evaporators of the two R11 water coolers with 170 tubes each, the corrugated inner surface of the finned tube, the experimental facility, and the data acquisition system. After three years (9000 hours) of trial operation, it can be stated that the heat transfer was raised by an average 60% inside the condenser and by 40% inside the evaporator. Electricity savings amounted to about 13%. The amortisation period (replacement of standard tubes by high-efficiency tubes) is about 2 years. (HWJ).

  14. An experimental investigation on air-side performances of finned tube heat exchangers for indirect air-cooling tower

    Directory of Open Access Journals (Sweden)

    Du Xueping

    2014-01-01

    Full Text Available A tremendous quantity of water can be saved if the air cooling system is used, comparing with the ordinary water-cooling technology. In this study, two kinds of finned tube heat exchangers in an indirect air-cooling tower are experimentally studied, which are a plain finned oval-tube heat exchanger and a wavy-finned flat-tube heat exchanger in a cross flow of air. Four different air inlet angles (90°, 60 °, 45°, and 30° are tested separately to obtain the heat transfer and resistance performance. Then the air-side experimental correlations of the Nusselt number and friction factor are acquired. The comprehensive heat transfer performances for two finned tube heat exchangers under four air inlet angles are compared. For the plain finned oval-tube heat exchanger, the vertical angle (90° has the worst performance while 45° and 30° has the best performance at small ReDc and at large ReDc, respectively. For the wavy-finned flat-tube heat exchanger, the worst performance occurred at 60°, while the best performance occurred at 45° and 90° at small ReDc and at large ReDc, respectively. From the comparative results, it can be found that the air inlet angle has completely different effects on the comprehensive heat transfer performance for the heat exchangers with different structures.

  15. Performance Evaluation Of Peripheral-Finned Tube Evaporators Under Frosting Conditions

    OpenAIRE

    2016-01-01

    The peripheral finned-tube (PFT) is a novel air-side geometry for compact heat exchangers. Previous studies (Pussoli et al., Int. J. Heat Mass Transfer 55, 2835–2843, 2012) dealt with the evaluation of the thermal-hydraulic performance of the PFT geometry under dry conditions (i.e., no frost or condensate formation on the air side). The present study is focused on quantifying the thermal-hydraulic perfomance of the PFT geometry under frosting conditions. PFT evaporators were tested in a clo...

  16. Turbulent flow in longitudinally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Edwards, D.P.; Hirsa, A.; Jensen, M.K. [Rensselaer Polytechnic Inst., Troy, NY (United States). Dept. of Mechanical Engineering, Aeronautical Engineering and Mechanics

    1996-09-01

    An experimental investigation of fully developed, steady, turbulent flow in longitudinally finned tubes has been performed. A two-channel, four-beam, laser-Doppler velocimeter was used to measure velocity profiles and turbulent statistics of air flow seeded with titanium dioxide particles. Mean velocities in axial, radial, and circumferential directions were measured over the tube cross sections and pressure drop in the tubes was measured at six stations along the test section length in order to calculate the fully developed friction factor. Four experimental tube geometries were studied: one smooth tube; two 8-finned tubes (fin height-to-radius ratios of 0.333 and 0.167), and one 16-finned tube (fin height-to-radius ratio of 0.167); detailed measurements were taken at air flow rates corresponding to Reynolds numbers of approximately 5,000, 25,000, and 50,000. Friction factor data were compared to literature results and showed good agreement for both smooth and finned tubes. The wall shear stress distribution varied significantly with reynolds number, particularly for Reynolds numbers of 25,000 and below. Maximum wall shear stress was found at the fin tip and minimum at the fin root. Four secondary flow cells were detected per fin (one in each interfin spacing and one in each core region for each fin); secondary flows were found to be small in comparison to the mean axial flow and relative magnitudes were unaffected by axial flow rate at Reynolds numbers above 25,000. The fluctuating velocities had a structure similar to that of the smooth tube in the core region while the turbulence in the interfin region was greatly reduced. The principal, primary shear stress distribution differed considerably from that of the smooth tube, particularly in the interfin region, and the orientation was found to be approximately in the same direction as the gradient of the mean axial velocity, supporting the use of an eddy viscosity formulation in turbulence modeling.

  17. Comparison of thermal and hydraulic performances of eccentric and concentric annular-fins of heat exchanger tubes

    Science.gov (United States)

    Benmachiche, Abdelmoumène Hakim; Tahrour, Farouk; Aissaoui, Faris; Aksas, Mounir; Bougriou, Cherif

    2017-02-01

    The present study is an experimental and 3-D computational fluid dynamics. It is used to compare between the heat transfer characteristics and pressure drops of eccentric and concentric annular-finned tube bundles. The RNG k-ɛ turbulence model of fluent is used to determine the optimum tube position in the circular fin that gives the highest thermal and hydraulic performances for both staggered and aligned arrangements. Then, experiments and numerical simulations were performed to examine the effects of bundle configurations, the Reynolds number (ranging from 5500 to 29,700) and the tube location inside the heat exchangers. A satisfactory qualitative and quantitative agreement was obtained between the numerical and experimental results. For both aligned and staggered heat exchangers, the thermal characteristics of the eccentric annular-finned tube are greater than that of the concentric ones. This gain is associated with reduction in pressure drop.

  18. Numerical Analysis of Shell-and-Tube Type Latent Thermal Energy Storage Performance with Different Arrangements of Circular Fins

    Directory of Open Access Journals (Sweden)

    Sebastian Kuboth

    2017-02-01

    Full Text Available Latent thermal energy storage (LTS systems are versatile due to their high-energy storage density within a small temperature range. In shell-and-tube type storage systems fins can be used in order to achieve enhanced charging and discharging power. Typically, circular fins are evenly distributed over the length of the heat exchanger pipe. However, it is yet to be proven that this allocation is the most suitable for every kind of system and application. Consequently, within this paper, a simulation model was developed in order to examine the effect of different fin distributions on the performance of shell-and-tube type latent thermal storage units at discharge. The model was set up in MATLAB Simulink R2015b (The MathWorks, Inc., Natick, MA, USA based on the enthalpy method and validated by a reference model designed in ANSYS Fluent 15.0 (ANSYS, Inc., Canonsburg, PA, USA. The fin density of the heat exchanger pipe was increased towards the pipe outlet. This concentration of fins was implemented linearly, exponentially or suddenly with the total number of fins remaining constant during the variation of fin allocations. Results show that there is an influence of fin allocation on storage performance. However, the average storage performance at total discharge only increased by three percent with the best allocation compared to an equidistant arrangement.

  19. Experimental Performance of a Finned-tube Silica Gel Adsorption Chiller for Air-Conditioning Application

    Directory of Open Access Journals (Sweden)

    Mohammed A. Atiya

    2014-09-01

    Full Text Available This work presents the construction of a test apparatus for air-conditioning application that is flexible in changing a scaled down adsorbent bed modules. To improve the heat and mass transfer performance of the adsorbent bed, a finned-tube of the adsorbent bed heat exchanger was used. The results show that the specific cooling power (SCP and the coefficient of performance (COP are 163 W/kg and 0.16, respectively, when the cycle time is 40 min, the hot water temperature is 90oC, the cooling water temperature is 30oC and the evaporative water temperature is 11.4oC.

  20. Heat transfer and pressure drop performance of smooth and internally finned tubes with oil and refrigerant 22 mixtures

    Energy Technology Data Exchange (ETDEWEB)

    Schlager, L.M. (Indiana-Purdue Univ., Ft. Wayne, IN (US)); Pate, M.B. (Iowa State Univ., Ames, IA (US)); Bergles, A.E. (Rensselaer Polytechnic Inst., Troy, NY (US))

    1989-01-01

    The overall performance of a smooth tube and two augmented tubes is compared by using an enhancement performance ratio, defined as the ratio of heat transfer enhancement to pressure drop increase. The augmented tubes are compared to the smooth tube with pure R-22 and with mixtures of R-22 plus 150-or 300-SUS naphthenic mineral oil. Additionally, the performance of all three tubes with refrigerant-oil mixtures is compared to performance of the same tube with pure refrigerant. Various oil concentrations up to 5% by weight were tested and mass flux was varied from 92,000 to 294,000 lb/h{circle dot}ft{sup 2} (125 to 400 kg/m{sup 2}{circle dot}s). Nominal evaporation conditions were 37{degrees}F(3{degrees}C) with inlet and outlet qualities of 15% and 85%, respectively. The condensation conditions were 105{degrees}F (41{degrees}C) with inlet and outlet qualities of 85% and 15%, respectively. The enhancement performance ratio of the micro-fin tube is consistently higher than that of the low-fin tube with either pure refrigerant or refrigerant-oil mixtures. With pure refrigerant, the enhancement performance ratio of the augmented tubes is generally greater than unity, indicating improved performance relative to a smooth tube.

  1. Experimental Study of the Airside Performance for Interrupted Fin-and-tube Heat Exchanger with Hydrophilic Coating under Dehumidifying Conditions

    Institute of Scientific and Technical Information of China (English)

    MA Xiao-kui; DING Guo-liang; ZHANG Yuan-ming

    2009-01-01

    The airside heat transfer and friction characteristics of seven interrupted fin-and-tube heat exchangers with hydrophilic coating under dehumidifying conditions are experimented. The effects of number of tube rows, fin pitch and inlet relative humidity on airside performance are analyzed. The test results show that the influence of fin pitch on the friction characteristic under dehumidifying conditions is similar to that under dry surface, and the friction factors decrease slightly with the increase of number of tube rows. The heat transfer performance decreases as fin pitch and number of tube rows increases. The heat transfer performance and the friction characteristic are independent of inlet relative humidity. Based on the test results, heat transfer and friction correlations in terms of the Colburn j factor and Fanning f factor, are proposed to describe the airside performance of the interrupted fin geometry with hydrophilic coating under dehumidifying conditions. The correlation of the Colburn j factor gives a mean deviation of 9.7%, while the correlation of the Fanning f factor shows a mean deviation of 7.3%.

  2. Effect of refrigerant mal-distribution in fin-and-tube evaporators on system performance

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Elmegaard, Brian; Larsen, Lars Finn Sloth

    2009-01-01

    Refrigerant mal-distribution in fin-and-tube evaporators for residential air-conditioning (RAC) is investigated numerically in this paper. A model of the system is developed in the object-oriented modeling language Modelica. Themodels of the compressor and expansion valve are static, whereas...... straight tubes. The refrigerant mal-distribution is then induced to the evaporator by varying the vapor quality at the inlet to each feeder tube, the pressure drop through each feeder tube and the air-flow across each tube. Finally it is shown that air-flow mal-distribution can be compensated...... by an intelligent distributor, that ensures equal superheat in both tubes. The refrigerant is R410a....

  3. Augmentation of Condensation Heat Transger by Finning of Tubes

    OpenAIRE

    1992-01-01

    This paper summarizes experimental and theoretical studies that have been performed in our laboratory to enhance condensation heat transfer on horizontal tubes and tube bundles by use of fins. Use of a drainge strip is proved to be very effective in further enhancing condensation heat transfer on the horizontal finned tube. Effects of fin geometry and tube arrangement on the condensation heat transfer performance of the tube bundle are investigated. A theoretical model is proposed to predict ...

  4. Ice formation around isothermal radial finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Ismail, K.A.R.; Henriquez, J.R.; Moura, L.F.M.; Ganzarolli, M.M. [UNICAMP-FEM-DETF, Campinas (Brazil)

    2000-04-01

    The present study presents a thermal numerical model for the solidification of Phase Change Material around a radially finned tube with a constant wall temperature. The model is based upon a pure conduction formulation and the enthalpy method. The finite difference approach and the alternating direction implicit scheme are used to discretize the system of equations and the associated boundary, initial and final conditions. Numerical experiments were realized to optimise the numerical code. Numerical simulations were performed to investigate the effects, of the number of fins, fin thickness, fin material, aspect ratio of the tube arrangement and the tube wall temperature. Graphical results were presented, discussed and equations relating the effect of each of the variables on the time for complete solidification are also presented. (author)

  5. Experimental Investigation of Gas-Side Performance of a Compact Finned-Tube Heat Exchanger

    Science.gov (United States)

    Gedeon, Louis

    1959-01-01

    Heat-transfer and pressure-drop data were obtained experimentally for the gas side of a liquid-metal to air, compact finned-tube heat exchanger. The heat exchanger was fabricated from 0.185-inch Inconel tubing in an inline array. The fins were made of 310 stainless-steel- clad copper with a total thickness of 0.010 inch, and the fin pitch was 15.3 fins per inch. The liquid used as the heating medium was sodium. The heat-exchanger inlet gas temperature was varied from 5100 to 1260 R by burning JP fuel for airflow rates of 0.4 to 10.5 pounds per second corresponding to an approximate Reynolds number range of 300 to 9000. The sodium inlet temperature was held at 1400 R with the exception of a few runs taken at 1700 and 1960 R. The maximum ratio of surface temperature to air bulk temperature was 1.45. Friction-factor data with heat transfer were best represented by a single line when the density and viscosity of Reynolds number were evaluated at the average film temperature. At the lower Reynolds numbers reported, the friction data with heat transfer plotted slightly above the friction data without heat transfer. The density of the friction factor was calculated at the average bulk temperature. Heat-transfer results of this investigation were correlated by evaluating the physical properties of air (specific heat, viscosity, and thermal conductivity) at the film temperature.

  6. Heat Transfer Performance of a Plate-Finned Tube Heat Exchanger : A Three-Dimensional Steady Numerical Analysis for a Single Row Tube in Low Reynolds Number Range

    OpenAIRE

    1998-01-01

    A three dimensional steady numerical analysis has been made for a one unit of single row plate-finned tube heat exchanger located in a uniform flow. The structures of the flow and thermal fields have been examined for conduction-convection conjugate heat transfer problem of the studied fin-and-tube model. The results of the numerical analysis revealed some important effects of geometric parameters on heat transfer from the fin-and-tube surface. The effects of fin thickness, fin pitch, fin len...

  7. Numerical analysis of the influence of circuit arrangement on a fin-and-tube condenser performance

    Directory of Open Access Journals (Sweden)

    Cesare Maria Joppolo

    2015-09-01

    Full Text Available In the present paper a model for the steady-state simulation of fin-and-tube condenser is developed. The model is based on a finite volume approach that divides each tube into small elemental volumes where mass, momentum and energy conservation equations are solved using the effectiveness-NTU method and with appropriate correlations for void fraction, friction factor and heat transfer coefficient calculation. The model is validated against experimental data on two small condensers finding that the calculated heat transfer rate and refrigerant-side pressure drop agree within ±5% and ±21% respectively to the experimental values. The model is then used to numerically analyse the impact of different circuit arrangements on the condenser heat transfer rate, refrigerant-side pressure drop and refrigerant charge.

  8. Fin Distance Effect at Tube-Fin Heat Exchanger

    Directory of Open Access Journals (Sweden)

    Frana K.

    2013-04-01

    Full Text Available Article deals with numerical simulation of the Tube-Fin heat exchanger. Several distances between fins are examined with intence of increasing the cooling output of the heat exchanger. Geometrical model consists of set of 2 fins with input and output area. Calculations covers the area of the gap from 2.25 mm to 4 mm with new fin geometry. For the numerical silumation was used software Ansys Fluent.

  9. Fin Distance Effect at Tube-Fin Heat Exchanger

    Science.gov (United States)

    Lemfeld, F.; Muller, M.; Frana, K.

    2013-04-01

    Article deals with numerical simulation of the Tube-Fin heat exchanger. Several distances between fins are examined with intence of increasing the cooling output of the heat exchanger. Geometrical model consists of set of 2 fins with input and output area. Calculations covers the area of the gap from 2.25 mm to 4 mm with new fin geometry. For the numerical silumation was used software Ansys Fluent.

  10. The optimum fin spacing of circular tube bank fin heat exchanger with vortex generators

    Science.gov (United States)

    Hu, Wanling; Su, Mei; Wang, Liangcheng; Zhang, Qiang; Chang, Limin; Liu, Song; Wang, Liangbi

    2013-09-01

    In real application, once the pattern of fin is determined, fin spacing of tube bank fin heat exchanger can be adjusted in a small region, and air flow velocity in the front of the heat exchanger is not all the same. Therefore, the effects of fin spacing on heat transfer performance of such heat exchanger are needed. This paper numerically studied the optimal fin spacing regarding the different front flow velocities of a circular tube bank fin heat exchanger with vortex generators. To screen the optimal fin spacing, an appropriate evaluation criterion JF was used. The results show that when front velocity is 1.75 m/s, the optimal fin spacing is 2.25 mm, when front velocity is 2.5 m/s, the optimal fin spacing is 2 mm, and when front velocity is higher than 2.5 m/s, the optimal fin spacing is 1.75 mm.

  11. Investigation of contact resistance for fin-tube heat exchanger by means of tube expansion

    Science.gov (United States)

    Hing, Yau Kar; Raghavan, Vijay R.; Meng, Chin Wai

    2012-06-01

    An experimental study on the heat transfer performance of a fin-tube heat exchanger due to mechanical expansion of the tube by bullets has been reported in this paper. The manufacture of a fin-tube heat exchanger commonly involves inserting copper tubes into a stack of aluminium fins and expanding the tubes mechanically. The mechanical expansion is achieved by inserting a steel bullet through the tube. The steel bullet has a larger diameter than the tube and the expansion provides a firm surface contact between fins and tubes. Five bullet expansion ratios (i.e. 1.045 to 1.059) have been used in the study to expand a 9.52mm diameter tubes in a fin-tube heat exchanger. The study is conducted on a water-to-water loop experiment rig under steady state conditions. In addition, the effects of fin hardness and fin pitch are investigated in the study. The results indicate that the optimum heat transfer occurred at a bullet expansion ratio ranging from 1.049 to 1.052. It is also observed that larger fin pitches require larger bullet expansion ratios, especially with lower fin hardness. As the fin pitch increases, both fin hardness (i.e. H22 and H24) exhibit increasing heat transfer rate per fin (W/fin). With the H22 hardness temper, the increase is as much as 11% while H24 increases by 1.2%.

  12. Thermal Performance of a Single-row Fin-and-tube Heat Exchanger

    Institute of Scientific and Technical Information of China (English)

    Sheng TANG; Kwang-Tzu YANG

    2005-01-01

    @@ Experiments were carried out to study the heat transfer characteristics of a single-row aluminum fin-and-tube crossflow heat exchanger with an emphasis in the regime of low flow rate of the in-tube fluid. The Chilton-Colburn analogy, in conjunction with the least-squares power-law technique, was used to correlate experimental data. Both air- and water-side heat transfer correlations were developed in the form of the Nusselt numbers as a function of Reynolds and Prandtl numbers. The experimental observations are quantitatively compared to the predictions of correlations available in the published literature. Different transfer mechanisms were found to be operative in the ranges of water-side Reynolds numbers based on the hydraulic diameter. In a range of Reynolds number from 1,200 to 6,000, the water-side thermal resistance accounts for less than ten percent of the overall thermal resistance. The dominant thermal resistance is always on the air-side. On the other hand, the thermal resistance of water-side is nearly equal to that of air-side in a Reynolds number range from 500 to 1,200.

  13. Improve seawater cooling with titanium finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    O' Donnell J. (High Performance Tube, Inc., Warren, NJ (United States))

    1992-10-01

    Seawater offers an endless supply of cooling water for these coastal processing facilities. But users must address seawater's corrosive nature in selecting construction materials for heat exchangers. Copper-nickel or carbon steel tubing fails continually under seawater service. This paper reports that titanium tubes, once thought to be too expensive a material for heat exchanger tubing, offer a unique combination of high material strength, excellent resistance to corrosion, and endurance to erosion by seawater. Titanium's superior physical properties in combination with enhanced surface area of low finned tubing perform the same heat duty with half the lineal footage of traditional heat exchanger tubes. High density low finned tubes multiply heat transfer capacity by a factor of two compared to plain tube. The technology applies in retrofit and original equipment manufacture (OEM) situations. It works best when the ratio of heat transfer coefficients is 2:1 or higher between the seawater coolant and shellside flow being cooled.

  14. Condensation heat transfer of r134a for single tubes and tube bundles using standard and high performance finned tubes; Kondensatseitiger Waermeuebergang am Einzelrohr und im Rohrbuendel beim Einsatz von Standard- und Hochleistungsrippenrohren mit R134a

    Energy Technology Data Exchange (ETDEWEB)

    Gebauer, Thomas; Leipertz, Alfred; Froeba, Andreas Paul [Erlangen-Nuernberg Univ. (Germany). Lehrstuhl fuer Technische Thermodynamik; Gotterbarm, Achim; El Hajal, Jean; Beutler, Andreas [Wieland-Werke AG, Ulm (Germany)

    2011-08-15

    This work aims at the optimization of the heat transfer of refrigerant R134a on finned tubes in shell-and-tube condensers. The coating and optimization of the fin structure should increase the drainage of the condensate in the space between the fins and therefore the condensation heat transfer on single tubes and tube bundles. (orig.)

  15. Study on Effect of Fin-tube Arrangement on the Heat Exchange Performance of Fin-tube Radiator%翅片管布置方式对管翅式散热器换热性能的影响

    Institute of Scientific and Technical Information of China (English)

    陈金友; 杨林; 漆波

    2016-01-01

    文章运用CFD软件对市场上主流的采暖用管翅式散热器建立了数学、物理模型,并进行了数值分析,对计算结果进行了验证,其误差在允许范围内;然后,对不同翅片管布置方式下的管翅式散热器的散热性能进行了数值分析,结果表明采用S型和交叉型的布置方式能够在一定程度上提高散热器的散热能力,对管翅式散热器的设计及优化有一定的理论指导意义。%The paper uses CFD software to construct the physical and mathematical models on the fins-tube radiator used widely in the market . After comparing the experimental results, the error of numerical modeling is acceptable. Comparing the heat dissipation performance of different fin-tube arrangement radiator through analyzing the temperature field and velocity field. Results show that the “S”and cross layout style can improve the performance of heat dissipation. And these results have the certain theoretical guiding significance for the design and optimization of fin-tube radiators.

  16. CFD Analysis of Plate Fin Tube Heat Exchanger for Various Fin Inclinations

    OpenAIRE

    2014-01-01

    ANSYS Fluent software is used for three dimensional CFD simulations to investigate heat transfer and fluid flow characteristics of six different fin angles with plain fin tube heat exchangers. The numerical simulation of the fin tube heat exchanger was performed by using a three dimensional numerical computation technique. Geometry of model is created and meshed by using ANSYS Workbench software. To solve the equation for the fluid flow and heat transfer analysis ANSYS FLUENT ...

  17. PHASE CHANGE AROUND A FINNED TUBE

    Directory of Open Access Journals (Sweden)

    Aytunç EREK

    2003-01-01

    Full Text Available This study presents the heat transfer enhancement in the thermal energy storage system by using radially finned tube. The solution of the system consists of the solving the equations of the heat transfer fluid (HTF, the pipe wall and fin, and the phase change material (PCM as one domain. The control volume finite difference approach and the semi implicit solver (SIS are used to solve the equations. Fully developed velocity distribution is taken in the HTF. Flow parameters (Re number and inlet temperature of coolant and fin parameters (the number of fins, fin length, fin thickness are found to influence solidification fronts and the total stored energy.

  18. Experiments with micro-fin tube in single phase

    Energy Technology Data Exchange (ETDEWEB)

    Copetti, J.B.; Macagnan, M.H.; De Souza, D.; Oliveski, R.D.C. [Universidade do Vale do Rio dos Sinos, Sao Leopoldo (Brazil). Department of Mechanical Engineering

    2004-12-01

    This work shows heat transfer and friction characteristics for water single-phase flow in micro-fin tubes. The analysis of thermal and hydraulic behavior from a laminar to a turbulent flow was carried out in an experimental setup with a 9.52 mm diameter micro-fin tube. The tube was wrapped up with an electrical resistance tape to supply a constant heat flux to its surface. Different operational conditions were considered in the heating tests. The inlet and outlet temperatures, differential wall temperatures along the tube, pressure drop and flow rate were measured. The relationships of heat flux and flow rate with heat transfer coefficient and pressure drop were analyzed. Under the same conditions, comparative experiments with an internally smooth tube were conducted. The micro-fin tube provides higher heat transfer performance than the smooth tube (in turbulent flow h{sub micro-fin}/h{sub smooth}=2.9). In spite of the increase in pressure drop ({delta}p{sub micro-fin}/{delta}p{sub smooth}=1.7) the heat transfer results were significantly higher (about 80%). This shows the advantages of this enhanced configuration in thermal performance related to conventional tubes. The smooth tube results were validated by the comparison with the Dittus-Boelter and Gnielinski correlations. For the micro-fin tube an empirical correlation to the heat transfer coefficient adjusted from the set of measured data is proposed. The values obtained are in conformity with experimental results. (author)

  19. Crystallization fouling of finned tubes during pool boiling: effect of fin density

    Energy Technology Data Exchange (ETDEWEB)

    Esawy, M.; Malayeri, M.R. [University of Stuttgart, Institute for Thermodynamics and Thermal Engineering (ITW), Stuttgart (Germany); Mueller-Steinhagen, H. [University of Stuttgart, Institute for Thermodynamics and Thermal Engineering (ITW), Stuttgart (Germany); German Aerospace Centre (DLR), Institute of Technical Thermodynamics, Stuttgart (Germany)

    2010-11-15

    Bubble characteristics such as density, size, frequency and motion are key factors that contribute to the superiority of nucleate pool boiling over other modes of heat transfer. Nevertheless, if heat transfer occurs in an environment prone to fouling, the very same parameters may lead to accelerated deposit formation due to concentration effects beneath the growing bubbles. This has led to the widely accepted design recommendation to maintain the heat transfer surface temperature below the boiling point if fouling may occur, e.g., in seawater desalination. The present paper aims at investigating the formation of deposits on finned tubes during nucleate pool boiling of CaSO{sub 4} solutions. The test finned tubes are low finned tubes with fin densities of 19 and 26 fins/in. made from Cu-Ni. The fouling experiments were carried out at atmospheric pressure for different heat fluxes ranging from 100 to 300 kW/m{sup 2} and a CaSO{sub 4} concentration of 1.6 g/L. For the sake of comparison, similar runs were performed with smooth stainless steel tubes. The results show that: (1) the fouling resistance decreases with increasing fin density, (2) fouling on the finned tubes was reduced with increasing nucleate boiling activity and (3) if any fouling layer occurred on the finned tubes it could be removed easily. (orig.)

  20. 翅片间距对翅片管换热性能影响分析%Research on the Influence of Fin Spacing to the Heat Transfer Performance of Finned Tube

    Institute of Scientific and Technical Information of China (English)

    曾小林; 林金国; 童小川

    2015-01-01

    对环形翅片管的自然对流换热过程进行了数值计算,主要关注翅片间距对翅片管自然对流换热过程的影响,结果表明:在给定结构尺寸下,翅片间距达到10mm以上时,翅片间散热不会相互影响;翅片间距在10mm以内时,随着翅片间距减小,翅片的表面换热系数逐渐降低。%Numerical analysis is performed on the natural convection of the finned tube. The influence of the fin spacing to the heat transfer performance of the finned tube is mostly concerned. The result shows that, under the given structure, the heat transfer of the fins will not affect each other when the fin spacing exceeds 10 millimeters,otherwise, the heat transfer performance will be reduced with the decrease of the fin spacing.

  1. Effect of Fin Geometry on Condensation of R134a in a Staggered Bundle of Horizontal Finned Tubes

    Science.gov (United States)

    Honda, Hiroshi; Takata, Nobuo; Takamatsu, Hiroshi; Kim, Jeongsk; Usami, Keiichiro

    Experimental results are presented that show the effect of fin geometry on condensation of refrigerant R134a in a staggered bundle of horizontal fined tubes. Two kinds of conventional low-fin tubes and three kinds of three-dimensional fin tubes were tested. The refrigerant mass velocity ranged from 8 to 23 kg/m2s and the condensation temperature difference from 1.5 to 12 K. In most cases, the highest performance was obtained by one of the three-dimensional fin tubes. In the case of high mass velocity and high film Reynolds number, however, the highest performance was obtained by one of the low-fin tubes. The results were compared with previous experimental results for bundles of smooth tubes and low-fin tubes.

  2. The Effects of Fin Spacing and Tube Outer Diameter of Evaporator on System Performance in Heat Pump Tumble Dryers

    OpenAIRE

    Onan, Cenk; Erdem, Serkan; Özkan, Derya Burcu; Heperkan, Hasan Alpay

    2014-01-01

    In heat pump tumble dryers, moisture separates from the laundry and leaves the dryer system at the evaporator. Moist air goes out the drum and enters the evaporator whose outer surface is below the dew point temperature. Air cools and then leaves its moisture. At the airside of the evaporator the wet surface develops and simultaneous heat-mass transfer occurs. Fin-and-tube heat exchangers are used as evaporators in household heat pump tumble dryers. In addition to optimum operating conditions...

  3. PHASE CHANGE AROUND A FINNED TUBE

    OpenAIRE

    EREK, Aytunç

    2003-01-01

    This study presents the heat transfer enhancement in the thermal energy storage system by using radially finned tube. The solution of the system consists of the solving the equations of the heat transfer fluid (HTF), the pipe wall and fin, and the phase change material (PCM) as one domain. The control volume finite difference approach and the semi implicit solver (SIS) are used to solve the equations. Fully developed velocity distribution is taken in the HTF. Flow parameters (Re number and in...

  4. Laminar heat transfer characteristics of internally finned tube with sinusoidal wavy fin

    Science.gov (United States)

    Lin, M.; Tian, L.; Wang, Q. W.

    2011-06-01

    Comparative numerical study of laminar heat transfer characteristics of annular tubes with sinusoidal wavy fins has been conducted both experimentally and numerically with Re = 299-1,475. The uniform heat flux is imposed on the tube outside wall surface. Two tube materials (copper and stainless steel) are considered. It is found that the fluid temperature profile is not linear but convex along the flow direction due to the axial heat conduction in tube wall, and the effects of axial heat conduction on the heat transfer decreases with an increase in Reynolds number or decrease in tube wall thermal conductivity. The axial distributions of local Nusselt number could reach periodically fully developed after 3-5 cycles. The convectional data reduction method based on the traditional method should be improved for tube with high thermal conductivity or low Reynolds numbers, Otherwise, the heat transfer performance of internally finned tube may be underestimated.

  5. Study of the effect of finned tube adsorber on the performance of solar driven adsorption cooling machine using activated carbon-ammonia pair

    Energy Technology Data Exchange (ETDEWEB)

    Louajari, Mohamed; Mimet, Abdelaziz [Energetic Laboratory, Sciences Faculty, Abdelmalek Essaadi University, BP 2121, 93000 Tetouan (Morocco); Ouammi, Ahmed [Energetic Laboratory, Sciences Faculty, Abdelmalek Essaadi University, BP 2121, 93000 Tetouan (Morocco); Department of Communication, Computer and System Sciences (DIST), University of Genova, Genova (Italy)

    2011-03-15

    Solar refrigeration represents an important application of solar energy due to the excellent matching between the high sunshine and the refrigeration needs. Solar adsorption refrigeration devices are among the significant techniques used to meet the needs for cooling requirements. Several solar refrigeration systems have been proposed and are under development such as sorption systems including liquid/vapor, solid/vapor absorption, adsorption, vapor compression and others. The purpose of this paper is to identify the influence of a cylindrical adsorber on the performances of a solar adsorption refrigerating machine. The adsorber heated by solar energy contains an activated carbon-ammonia pair; it is composed by many cylindrical tubes welded using external fins. A model based on the conservation equations of energy and mass in the adsorber has been developed and well described. Using real solar irradiance data as well as many initial conditions, the model computes for each point and in the considered time interval during the day, the temperature, the adsorbed mass, the pressure inside the adsorber and the solar performance coefficient (COP). The results show that the optimal diameter of the adsorber with fins is greater than the one without fins. Moreover the mass cycled in the case of an adsorber equipped with external fins is more significant than the one without fins, and the maximal temperature reached in the adsorber with fins attains 97 C while in the adsorber without fins reaches 77 C. Thus, the performances of the solar adsorption refrigerating machine with an adsorber equipped with fins are higher than the machine without fins. (author)

  6. Effects of Fin Shape on Condensation Heat Transfer and Pressure Drop inside Herringbone Micro Fin Tubes

    Science.gov (United States)

    Miyara, Akio; Otsubo, Yusuke; Ohtsuka, Satoshi

    Experiments of in-tube condensation of R410A have been carried out for as mooth tube, a h elical micro fin tube and five types of herringbone micro fin tubes. In the herringbone micro fin tube, the micro fins work to remove liquid at fin-diverging parts and collect liquid at fin-converging parts. In the high mass velocity region, heat transfer coefficient of all the herringbone tubes is about 2-4 times higher than that of the helical micro fin tube. In the low mass velocity region, however, the heat transfer coefficients of the herringbone micro fin tubes are equal to or smaller than those of the helical micro fin tube. Up to the fin height of 0.18 mm, the heat transfer coefficient is higher for higher fin, whereas that of ah igher fin tube is saturated. The pressure drop increases with increasing fin height. The helix angle strongly affects the heat transfer and pressure drop. Higher helix angle causes higher heat transfer coefficient and higher pressure drop. In the case of the herringbone tube which has shorter fin and/or smaller helix angle, pressure drops are equal to or lower than that of the helical micro fin tube, whereas those of other tubes are higher.

  7. Some aspects of film condensation of steam on finned tubes

    OpenAIRE

    Coumes, James M.

    1989-01-01

    Approved for public release; distribution is unlimited Heat-transfer measurements were made for filmwise condensation of steam on smooth tubes and finned tubes with rectangular-shaped fins. The influence of fin root diameter on a single horizontal finned tube was examined by taking data for two families of tubes whose fin root diameters were 12.7 and 19.05 mm. Each family of tubes had fins that were 1 mm thick and 1 mm high but with fin spacings of 0.25, 0.50, 1.0, 1.5, 2.0, and 4.0 mm. ...

  8. Selection of plain or segmented finned tubes for heat recovery

    Energy Technology Data Exchange (ETDEWEB)

    Reid, D.R.; Taborek, Jerry (Fintube Corp. (United States))

    1994-01-01

    Heat recovery heat exchangers with gas as one of the streams depend on the use of finned tubes to compensate for the inherently low gas heat transfer coefficient. Standard frequency welded ''plain'' fins were generally used in the past - until the high-frequency resistance welding technology permitted the cost-effective manufacture of segmented fins. The main advantage of the segmented fin design is that it permits higher heat flux and hence smaller, lighter units for most operating conditions. While the criteria that dictate optimum design, such as compactness, weight and cost per unit area, favour the segmented fin design, a few other considerations, such as fouling, ease of cleaning and availability of dependable design methods, have to be considered. This article analyses the performance parameters that affect the selection of either fin type. (4 figures, 1 table, 10 references) (Author)

  9. 纵向翅片扁管的传热性能分析%Performance Analysis of Vertical Fin and Flat Tube Heat Transfer

    Institute of Scientific and Technical Information of China (English)

    顾平道; 梁小强; 汤国芳; 邱燃

    2011-01-01

    本文运用FLUENT软件对纵向翅片扁管进行数值模拟,对翅片的长度、高度、间距在不同进口参数下翅片表面的传热和流动性能进行比较,得出有效翅片长度受速度的影响,翅片间距与换热系数成正比,与空气流道压降成反比。为强化纵向翅片扁管传热提供参考。%A simulation of vertical fin and flat tube is carried out using FLUENT software compared with heat transfers and flow performances of fin surface at different import parameters to length.Obtained the effective fin length by the velocity,the fin pitch is proportional to the heat transfer coefficient,inverse to pressure drop.The reference is provided for enhancing the heat transfer of vertical fin and flat tube.

  10. Heat Transfer Analysis of Fin Tube

    Energy Technology Data Exchange (ETDEWEB)

    Jeon, Woo-Jin [Korea Atomic Energy Research Institute, Daejeon (Korea, Republic of); Choi, Cheng-Ryul [ELSOLTEC Co., Yongin (Korea, Republic of)

    2015-10-15

    This paper describes a preliminary numerical analysis of fin tube used for a heat exchanger of the air-water cooling system. The internal flow in a fin tube is steam and the external of the fin is cooled by air. Cooling system in a nuclear power plant can be divided into two categories; 1) active pump driven system powered by alternating current and 2) passive cooling system drived by natural circulation phenomena. After the accident in Hukushima Nuclear Power Plants, the importance of the passive cooling system that can provide a long-term cooling of reactor decay heat during station blackout condition is emphasized. However, the effectiveness of passive cooling system based on cooling water is limited by the capacity of water storage tank. To overcome the limit due to the exhaustion of the cooling water, an natural convection air cooling system is proposed. As the air operated cooling system utilizes natural circulation phenomena of air, it does not require cooling water. However, the heat transfer area of the air operated cooling system should be increased much as the heat removal capacity per unit area is much lower than that of water cooling system. The air-water combined cooling system can resolve this excess increase of the heat transfer area in the air operated cooling system. This air-water cooling system can be also used in the passive containment cooling system. The effect of design parameters such as fin tube arrangement, the fin height, and pitch has been analyzed and the chimney effect on the simulation of heat transfer in a heat exchanger is evaluated. The internal flows in a fin tube heat exchanger for natural circulation flow condition and forced convection (suction) condition were investigated.

  11. Validation of a Model for Ice Formation around Finned Tubes

    OpenAIRE

    Kamal A. R. Ismai; Fatima A. M. Lino

    2016-01-01

    Phase change materials although attaractive option for thermal storage applications its main drawback is the slow thermal response during charging and discharging processes due to their low thermal conductivity. The present study validates a model developed by the authors some years ago on radial fins as a method to meliorate the thermal performance of PCM in horizontal storage system. The developed model for the radial finned tube is based on pure conduction, the enthalpy approach and was di...

  12. CFD Analysis of Plate Fin Tube Heat Exchanger for Various Fin Inclinations

    Directory of Open Access Journals (Sweden)

    Subodh Bahirat,

    2014-08-01

    Full Text Available ANSYS Fluent software is used for three dimensional CFD simulations to investigate heat transfer and fluid flow characteristics of six different fin angles with plain fin tube heat exchangers. The numerical simulation of the fin tube heat exchanger was performed by using a three dimensional numerical computation technique. Geometry of model is created and meshed by using ANSYS Workbench software. To solve the equation for the fluid flow and heat transfer analysis ANSYS FLUENT was used in the fin-tube heat exchanger. The fluid flow and heat transfer are simulated and result compared for both laminar and turbulent flow models k-epsilon and SST k-omega, with steady state solvers to calculate heat transfer, flow velocity and temperature fields of variable inclined fin angles (Ɵ = 00 ,100 , 200 , 300 , 400 ,500 . Model is validate by comparing the simulated value of velocity, temperature and colburn factor with experimental and numerical results investigated by WANG [1] and GHORI KIRAR [10]. Reasonable agreement is found between the simulations and other results, and the ANSYS Fluent software is sufficient for simulating the flow fields in tube fin heat exchanger.

  13. Laser Welding Of Finned Tubes Made Of Austenitic Steels

    Directory of Open Access Journals (Sweden)

    Stolecki M.

    2015-09-01

    Full Text Available This paper describes the technology of welding of finned tubes made of the X5CrNi1810 (1.4301 austenitic steel, developed at Energoinstal SA, allowing one to get high quality joints that meet the requirements of the classification societies (PN-EN 15614, and at the same time to significantly reduce the manufacturing costs. The authors described an automatic technological line equipped with a Trumph disc laser and a tube production technological process. To assess the quality of the joints, one performed metallographic examinations, hardness measurements and a technological attempt to rupture the fin. Analysis of the results proved that the laser-welded finned tubes were performed correctly and that the welded joints had shown no imperfections.

  14. Film condensation of steam on externally finned horizontal tubes.

    OpenAIRE

    Flook, Frederick A.

    1985-01-01

    Approved for public release; distribution is unlimited Filmwise condensation measurements of steam were made on horizontal finned tubes under vacuum and near-atmospheric conditions. Data were obtained for copper tubes with fins of rectangular, triangular, trapezoidal, and parabolic cross sections, and for a commercially-available finned tube. A stainless steel finned tube was also tested to investigate the effect of thermal conductivity. Maximum enhancements of about 4.8 were obtained...

  15. Sizing-tube-fin space radiators

    Science.gov (United States)

    Peoples, J. A.

    1978-01-01

    Temperature and size considerations of the tube fin space radiator were characterized by charts and equations. An approach of accurately assessing rejection capability commensurate with a phase A/B level output is reviewed. A computer program, based on Mackey's equations, is also presented which sizes the rejection area for a given thermal load. The program also handles the flow and thermal considerations of the film coefficient.

  16. Study on Thermo-Conductive Plastic Finned Tube Radiators

    Institute of Scientific and Technical Information of China (English)

    1997-01-01

    This paper discusses thermo-conductive plastic finned tube radiators used in water saving type power stations.First,the development of thermo-conductive plastics is introduced.Second,in order to determine the rational geometric dimensions of thermo-conductive plastic finned tubes,an objective function which takes the minimum volume of the consumed material for making finned tubes as an object is introduced.On the basis of the function,the economy comparison between thermo-conductive plastic finned tubes and metal finned tubes is conducted.

  17. Convection heat transfer and pressure drop in cross flow over finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Baran, M.; Pronobis, M.

    1984-05-15

    This paper reports the results of an experimental study on the heat transfer and pressure drop in finned tube banks. The measurements were carried out for the tubes with fins arranged parallel and a certain angle to the flow direction. The performance of such a heat exchanger with that of the conventional one i.e. plain tube heat exchanger, is compared.

  18. Enhancenment of In-tube Condensation of Nonazeotropic Refrigerant Mixtures with a Micro-fin Tube

    Science.gov (United States)

    Koyama, Shigeru; Gao, Lei; Hujii, Tetsu

    Condensation heat transfer and pressure drop characteristics of nonazeotropic refrigerant mixtures (NARMs) of HCFC22 and CFC114 inside horizontal smooth and micro-fin tubes are experimentally investigated. The local Nusselt number for both tubes based on the temperature difference between bulk refrigerant and tube wall is compared. Data for the micro-fin tube are about 50% higher than those for the smooth tube in both cases of pure refrigerants and NARMs. In case of NARMs, however, the decrease of Nesselt number due to vapor mass transfer resistance is observed for the micro-fin tube as well as for the smooth tube. By assuming that heat transfer characteristics of the condensate of NARMs are similar to those for pure refrigerants, the vapor mass transfer coefficient of NARMs is evaluated. Comparison of frictional pressure drop for both tubes is also performed in the Lockharte-Martinelli relation. Data for the micro-fin tube are higer than those for the smooth tube. The maximum increase of the frictional pressure drop is about 30%.

  19. Film condensation of R-113 on in-line bundles of horizontal finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H. (Kyushu Univ., Fukuoka (Japan)); Uchima, B.; Nozu, S.; Nakata, H.; Torigoe, E. (Okayama Univ. (Japan))

    1991-05-01

    Film condensation of R-113 on in-line bundles of horizontal finned tubes with vertical vapor downflow was experimentally investigated. Two tubes with flat-sided annular fins and four tubes with three-dimensional fins were tested. The test sections were 3 {times} 15 tube bundles with and without two rows of inundation tubes at the top. Heat transfer measurements were carried out on a row-by-row basis. The heat transfer enhancement due to vapor shear was much less for a finned tube bundle than for a smooth tube bundle. The decrease in heat transfer due to condensate inundation was more marked for a three-dimensional fin tube than for a flat-sided fin tube. The predictions of the previous theoretical model for a bundle of flat-sided fin tubes agreed well with the measured data for low vapor velocity and a small to medium condensate inundation rate. Among the six tubes tested, the highest heat transfer performance was provided by the flat-sided fin tube with fin dimensions close to the theoretically determined optimum values.

  20. Heat transfer in bundles of finned tubes in crossflow

    Energy Technology Data Exchange (ETDEWEB)

    Stasiulevicius, J.; Skrinska, A.; Zukauskas, A.; Hewitt, G.F.

    1986-01-01

    This book provides correlations of heat transfer and hydraulic data for bundles of finned tubes in crossflow at high Reynolds numbers. Results of studies of the effectiveness of the fin, local, and mean heat transfer coefficients are presented. The effect of geometric parameters of the fins and of the location of tubes in the bundle on heat transfer and hydraulic drag are described. The resistance of the finned tube bundles under study and other factors are examined.

  1. Efficiency of the unit cell in rectangular finned tube arrangements

    Energy Technology Data Exchange (ETDEWEB)

    Buzzoni, Luca; Dall' Olio, Roberto; Spiga, Marco [Bologna Univ., DIENCA, Bologna (Italy)

    1999-11-01

    This paper is aimed at presenting an investigation concerning the efficiency of the single unit in finned air-cooled heat exchangers with staggered and in-line bundles of rectangular ducts, where a hot process fluid flows inside extended-surface tubes and atmospheric air is circulated outside, over the extended surface. The differential energy equation is numerically solved by a finite difference technique, in order to determine the spatial temperature profiles, then the fin efficiency and the augmentation factor are calculated by a simple numerical integration. The results show that the temperature distribution and the fin performance depend on four dimensionless parameters (m,{beta},p{sub x},p{sub y}), the first accounting for the heat transfer condition, the other ones accounting for the geometry of the extended surface (tube aspect ratio and pitches). Several tables are presented, allowing the efficiency of the extended surface to be deduced as a function of the thermal and geometric parameters. (Author)

  2. Film condensation of downward flowing R-113 vapor on in-line bundles of horizontal finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Honda, Hiroshi; Uchima, Bunken; Nozu, Shigeru; Nakata, Hironori; Torigoe, Eiichi (Okayama Univ., Faculty of Engineering, Okayama, (Japan))

    1989-08-25

    The film condensation characteristics of a downward flowing R-113 vapor on in-line bundles of horizontal finned tubes were experimentally investigated using two tubes with flat-sided fins and four tubes with three-dimensional fins. The flow pattern of falling condensate on the finned tube bundle is similar to that on the smooth tube bundle, basically. The liquid filled position of tube with flat-sided fins is not affected by the vapor velocity. The effect of the vapor velocity on the film condensation in the finned tube bundle was considerably smaller than the case of the smooth tube bundle. The decrease of the heat transfer coefficient due to the condensate inundation was larger in case of the tubes with three-dimensional fins than in case of the tubes with flat-sided fins. While the tubes with three-dimensional fins showed contrary tendency against the tubes with flat-sided fins. Among six sample tubes, a tube with flat-sided fins of 0.5mm fin pitch and 1.3mm fin height showed the best heat transfer performance over the range of the whole experiment. 16 refs., 11 figs., 2 tabs.

  3. Numerical Analysis of Mixed Convection through an Internally Finned Tube

    Directory of Open Access Journals (Sweden)

    Sachindra Kumar Rout

    2012-01-01

    Full Text Available Wall temperature of an internally finned tube has been computed numerically for different fin number, height, and shape by solving conservation equations of mass, momentum, and energy using Fluent 12.1 for a steady and laminar flow of fluid inside a tube under mixed flow condition. It has been found that there exists an optimum number for fins to keep the pipe wall temperature at a minimum. The fin height has an optimum value beyond which the wall temperature becomes insensitive to fin height. For a horizontal tube, under mixed flow condition, it is seen that the upper surface has higher average temperature than the lower surface. The impact of fin shape on the heat transfer rate shows that wall temperature is least for triangular-shaped fins, compared to rectangular- and T-shaped fins. In addition to the thermal characteristics, the pressure drop caused due to the presence of fins has also been studied.

  4. Film condensation of R-113 on staggered bundles of horizontal finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H. (Kyushu Univ., Fukuoka (Japan)); Uchima, B. (Kagawa Technical Coll., Marugame (Japan)); Nozu, S.; Torigoe, E.; Imai, S. (Okayama Univ., Tsushima (Japan))

    1992-05-01

    Film condensation of R-113 on staggered bundles of horizontal finned tubes with vertical vapor downflow was experimentally investigated. Two tubes with flat-sided annular fins and four tubes with three-dimensional fins were tested. The condensate flow and heat transfer characteristics were compared with the previous results for in-line bundles of the same test tubes and a staggered bundle of smooth tubes. The decrease in heat transfer characteristics were compared with the previous results for in-line bundles of the same test tubes and a staggered bundle of smooth tubes. The decrease in heat transfer due to condensate inundation was most significant for the in-line bundles of the three-dimensional fin tubes, whereas the decrease was very slow for both the staggered and in-line bundles of the flat-sided fin tubes. The predictions of the previous theoretical model for a bundle of flat-sided fin tubes agreed fairly well with the measured data at a low vapor velocity. The highest heat transfer performance was provided by the staggered bundle of flat-sided fin tubes with fin dimensions close to the theoretically determined optimum values.

  5. Thermal Analysis of Fin and Tube Heat Exchanger

    Directory of Open Access Journals (Sweden)

    Ms N. B. Rairker

    2014-06-01

    Full Text Available This paper studied experimentally the effect of heat transfer of fin and tube type heat exchanger for different mass flow rate of fluid. The thermal stresses induced on fin and tube is also studied by ansys software at steady state condition by changing the width of fin and diameter of tube. Readings were taken experimentally by changing mass flow rate of fluid at respective temperatures. Comparison was done on theoretically and experimentally obtained results. It is observed that as the width of fin increases thermal stresses on fin also increases. Likewise for tube, by varying diameter of tube different values of stress are obtained. It is also observed at full valve position maximum thermal stresses are induced on fin as well as tube.

  6. Validation of a Model for Ice Formation around Finned Tubes

    Directory of Open Access Journals (Sweden)

    Kamal A. R. Ismai

    2016-09-01

    Full Text Available Phase change materials although attaractive option for thermal storage applications its main drawback is the slow thermal response during charging and discharging processes due to their low thermal conductivity. The present study validates a model developed by the authors some years ago on radial fins as a method to meliorate the thermal performance of PCM in horizontal storage system. The developed model for the radial finned tube is based on pure conduction, the enthalpy approach and was discretized by the finite difference method. Experiments were realized specifically to validate the model and its numerical predictions.

  7. Thermal Analysis of Fin and Tube Heat Exchanger

    OpenAIRE

    2014-01-01

    This paper studied experimentally the effect of heat transfer of fin and tube type heat exchanger for different mass flow rate of fluid. The thermal stresses induced on fin and tube is also studied by ansys software at steady state condition by changing the width of fin and diameter of tube. Readings were taken experimentally by changing mass flow rate of fluid at respective temperatures. Comparison was done on theoretically and experimentally obtained results. It is observed ...

  8. Filmwise condensation of steam on low integral-finned tubes

    OpenAIRE

    Georgiadis, Ioannis V.

    1984-01-01

    Approved for public release; distribution is unlimited Filmwise condensation heat-transfer measurements if steam were made on horizontal tubes under vacuum and near-atmospheric pressures. Data were taken for a smooth tube and for 21 tubes which contained rectangularly-shaped, low integral fins. The fin geometry was systematically varied in order to investigate the dependence of the steam-side heat-transfer coefficient on fin spacing, thickness and height. The condensation process was fo...

  9. Finned Small Diameter Tube Heat Exchanger

    Science.gov (United States)

    Dang, Chaobin; Daiguji, Hirofumi; Hihara, Eiji; Tokunaga, Masahide

    The performance of fined small tube heat exchangers was investigated both experimentally and theoretically. The Inner diameters of tubes were 1.0mm, 2.1mm and 4.0mm. Exchanged heat and pressure drop obtained from numerical simulation agreed well with the experimental ones. Calculation results show that the volume of a 2.0mm tube heat exchanger can be reduced to 33% of that of a 4mm tube heat exchanger with the same capacity. In addition the distribution of two-phase flow in a branching unit was investigated by measuring downstream temperature distribution. The flow distribution in a branching unit strongly affects the exchanged heat.

  10. Heat transfer, erosion and acid condensation characteristics for novel H-type finned oval tube

    Science.gov (United States)

    Wang, Y.; Zhao, X.; Tang, G.

    2015-09-01

    Low efficiency of heat transfer, acid corrosion and erosion of economizers affect the economy and security in coal-fired power plants significantly. The H-type finned oval tube is proposed to alleviate these problems. Based on the H-type finned oval tube, we investigated three novel types of fins, including bleeding dimples, longitudinal vortex generators (LVGs), and compound dimple-LVG. We considered the three aspects together, and obtained the heat transfer, acid condensation rate and erosion loss. The results show that the tube bank with the new structured fins can improve the performance on the three aspects, and the compound dimple-LVG performs the highest comprehensive effect.

  11. The Mathematical Model of Cooling Fan Finned Tube and Its Performance Analysis Using Comparison Methods%冷风机翅片管的数学模型及性能的比较法辨析

    Institute of Scientific and Technical Information of China (English)

    李锐

    2014-01-01

    不同的翅片管材料及翅片形式都将直接影响着翅片盘管的性能优异,以铝管铝套片冷风机为设计依据展开讨论,对冷风机蒸发器翅片管的设计建立数学模型,重点论述了翅片管特性,并用比较法对翅片管的性能进行了分析,以求能在设计时选出最佳的翅片管设计方案。%Different finned tube material and fin form will directly affect the performance of the fin coil. This paper discusses the design basis of the cooling fan with aluminum tubes and aluminum chipsets, establishes the mathematical model for designing its evaporator finned tube, focuses on the finned tube characteristics, and analyses the finned tube performance by using comparison methods, in order to select the best design scheme.

  12. Multiphysics Numerical Modeling of a Fin and Tube Heat Exchanger

    DEFF Research Database (Denmark)

    Singh, Shobhana; Sørensen, Kim; Condra, Thomas Joseph

    2015-01-01

    In the present research work, a modeling effort to predict the performance of a liquid-gas type fin and tube heat exchanger design is made. Three dimensional (3D) steady state numerical model is developed using commercial software COMSOL Multiphysics based on finite element method (FEM......). For the purposes here, only gas flowing over the fin side is simulated assuming constant inner tube wall temperature. The study couples conjugate heat transfer mechanism with turbulent flow in order to describe the temperature and velocity profile. In addition, performance characteristics of the heat exchanger...... design in terms of heat transfer and pressure loss are determined by parameters such as overall heat transfer coefficient, Colburn j-factor, flow resistance factor, and efficiency index. The model provides useful insights necessary for optimization of heat exchanger design....

  13. Heat transfer to finned tubes exposed to hot waste gas

    Energy Technology Data Exchange (ETDEWEB)

    Scholand, E.; Kremer, H.

    1975-05-01

    Transfer of heat by forced convection to finned tubes, particularly to those with an elliptical center pipe, is described. These pipes are used in gas-fired water heaters, boilers, and heat exchangers. Finned tubes in a test tunnel were exposed to a stream of waste gas from a gas/air mixture at different Reynolds numbers. Mathematical relationships showing the dependence of the Nusselt number on the Reynolds number and on the geometry of the tubes were derived. The single pipe showed a significant drop in the heat-transfer coefficient as the gap between fins became closer. The results of the measurement of heat transfer by forced convection to finned tubes were expressed in a standard form for all tubes. The same heat transfer law can be applied to electrically heated finned tubes exposed to a stream of cooling air.

  14. Film condensation of HCFC-123 on in-line bundles of horizontal finned tubes. Effect of fin geometry. Suihei fin tsuki kan no gobanme kangun ni okeru HCFC-123 no gyoshuku. Fin keijo no eikyo

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H.; Takamatsu, H.; Takada, N. (Kyushu University, Fukuoka (Japan). Institute of Advanced Material Study); Kim, K. (Kyushu University, Fukuoka (Japan)); Ishikawa, Y. (Otsuka Pharmaceutical Co. Ltd., Tokyo (Japan))

    1994-06-25

    Theoretical analysis and experiments were carried out in regard to the condensation of HCFC-123 vapor on a horizontal finned tube. The previous paper described the theoretical analysis on the film condensation in a tube nest with low-fins. In this study, approximate expressions of heat transfer coefficient for a newly proposed high-performance finned tubes are suggested and compared with the experimental results. In the test, HCFC-123 vapor was flowed from the upper part of the tube nest arranged in squares of 3 rows and 15 layers (tube pitch: 22mm), and was condensed on the tube surface. The liquid film formation was observed, and the heat transfer properties were measured. Two kinds of conventional low-fin tubes and two kinds of finned tubes of which shape is similar to the newly proposed ones were tested. One of the new finned tubes showed the highest heat transfer performance, which was about 85% higher than that of the conventional low-fin (26 fpi) tube. The theoretical model for condensation in the previous paper was correspondent with the experimental data at low vapor speed and low condensate inundation rate. 14 refs., 14 figs., 4 tabs.

  15. Film condensation of HCFC-123 on staggered bundles of horizontal finned tubes. Effect of fin geometry; Suihei fintsukikan no chidori kanbun ni okeru HCFC-123 no gyoshuku. Fin keijo no eikyo

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H.; Takamatsu, H.; Takada, N. [Kyushu University, Fukuoka (Japan). Institute of Advanced Material Study; Makishi, O. [Kyushu University, Fukuoka (Japan); Sejimo, H. [NKK Corp., Tokyo (Japan)

    1995-03-25

    Experiments were conducted to obtain row-by-row heat transfer data during condensation of downward flowing HCFC-123 vapor in staggered bundles of horizontal two-dimensional fin tubes. Two conventional low fin tubes and two finned tubes with fin shapes close to that of a new high-performance fin proposed by Zhu and Honda were tested. The latter tubes had fin dimensions that were optimized by theoretical analysis. The heat transfer characteristics were compared with previous results for in-line bundles of the same test tubes and with theoretical predictions for stagnant vapor. The decrease in heat transfer due to condensate inundation was less significant for the staggered tube bundle. The highest heat transfer coefficient was provided by the staggered bundle of one of the new finned tubes. The theoretical predictions compared well with experimental data at a low vapor velocity and a low to medium condensate inundation rate. 15 refs., 10 figs., 2 tabs.

  16. Heat exchanger with helical bundles of finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Eyking, H.J.

    1975-01-23

    The invention applies to a heat exchanger with helical bundles of tubes consisting of finned tubes separated by spacers. The spacers are designed as closed holding cylinders with holding devices for the tube bundles, each ot which surrounds a bundle of tubes. This construction serves to simplify the production process and to enable the use of the heat exchanger at higher loads.

  17. THERMAL EFFICIENCY ANALYSIS OF CROSS-FINNED TUBES

    OpenAIRE

    Лагутін, А.Ю.; П.Ф. Стоянов

    2015-01-01

    Finned heat exchangers are the basic type of heat exchanger employed in many industrial applications such as refrigeration, air conditioning and other thermal processes. This paper presents experimental research of air-side heat transfer of finned surfaces. Seven types of finned surfaces are employed in this study. Investigation describes temperature fields and temperature cooling air-flow changing in the inter-fin duct without taking into account tube section. Temperature difference in-betwe...

  18. Layout of a latent heat storage system with finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Wolff, D.

    1980-10-26

    The theoretical and experimental investigations show by the example of Glauber's salt in a finned-tube latent heat storage vessel how heat transfer and storage capacity at charging and discharging depend on the variables of geometry, temperature, time and on the composition of the storing medium. By vertical arrangement of transversely finned tubes the separation problems occurring with Glauber's salt are solved insofar as the technical utilization of the latent heat of conversion corresponding to the complete conversion during charging and discharging not being possible, no decrease, of the reduced storage capacity, however, is found even after very many charging/discharging cycles. For the heat transfer during discharging correlations can be given on the basis of a model concept, be means of which a heat transfer coefficient, varying during the discharging process, can be predicted almost for the total range of discharge as a function of geometry, temperature and state of discharge. On the basis of the simple working formula for the heat transfer coefficient at crystallization of a latent heat storing medium the dynamic behavior of a compact finned-tube storage vessel can be predicted by means of a computer code. These means allow to perform the thermal design of a compact latent heat storage facility according to given design criteria accounting for economic aspects.

  19. Effect of vapor velocity during condensation on horizontal finned tubes

    OpenAIRE

    Hopkins, Charles Louis III

    1988-01-01

    Approved for public release; distribution is unlimited Heat-transfer measurements were made for condensation of R-113 and steam on a smooth tube and on three finned tubes with rectangular shape fins. These tubes had a fin height and width of 1.0 mm and spacings of 0.25, 1.5, and 4.0 mm (tubes A, B, and C respectively) . Data were taken by increasing the vapor velocity from 0.4 to 1.9 m/s for R-113 and 4.8 to 31.3 m/s for steam. For both fluids, the improvement of the c...

  20. Conjugated laminar forced convective heat transfer from internally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Wen-Quan Tao (Xi' an Jiaotong Univ., Shaanxi (China))

    1987-08-01

    The use of internal fins is a very effective means of augmenting heat transfer in a tubular heat exchanger, especially for the laminar flow case. Several theoretical investigations have been undertaken to determine heat transfer performance under fully developed conditions. Results reported in the literature are derived for prescribed thermal boundary conditions, wither with axially uniform heat flux with peripherally uniform temperature, or with constant temperature axially as well as circumferentially. However, for double pipe heat exchangers, the thermal boundary condition of the separating wall can not be prescribed a priori; it is determined by the thermal interaction between the fluid inside the tube and that in the annular space. Mikhailov and Shishedjiev (1981), and Tao (1986) have shown that Nusselt number of the tube and that of the annular are strongly dependent upon the heat capacity ratio of the two fluids. In this investigation, a performance analysis is conducted numerically for an internally finned tube which serves as the inner tube of a double pipe heat exchanger.

  1. Compensation of flow maldistribution in fin-and-tube evaporators for residential air-conditioning

    OpenAIRE

    2011-01-01

    Compensation of flow maldistribution in multi-channel fin-and-tube evaporators for residential air-conditioning is investigated by numerical modeling. The considered sources of maldistribution are distribution of the liquid and vapor phases in the distributor and non-uniform airflow distribution. Fin-and-tube heat exchangers usually have a predefined circuitry, however, the evaporator model is simplified to have straight tubes, in order to perform a generic investigation. The compensation of ...

  2. HEAT EXCHANGE AND AERODYNAMICS OF THE COMBINED TUBING BUNDLES WITH CROSS INCLINED FINS

    Directory of Open Access Journals (Sweden)

    Knyazyuk V. I

    2013-04-01

    Full Text Available The paper presents results of experimental research and analyses air-side thermal performance of combined tube bundles with cross inclined fins. The empirical correlations for heat transfer and flow friction of tubes with inclined fins at different orientation finned tubes relatively of air flow are presented. The errors of thermal and aerodynamic tests are 3-5% and 9.2%, respectively. The proposed correlations describe an experimental data with a coefficient of determination about 0.979-0.998. The impact of tubes arrangement in a bundle on energy performance of heat exchanger were analyzed using complete and local heat modeling methods at a stationary heat flux. Experimental research indicates that efficiency of inclined fins can be calculated by using the equation for cross rectangular fins with average deviation of ±5 %.

  3. Numerical Simulation Study of Natural Convection Heat Transfer Performance of Circumferential Finned Tube%环形翅片管自然对流传热特性的数值模拟研究

    Institute of Scientific and Technical Information of China (English)

    李家乐

    2013-01-01

    利用FLUENT数值模拟方法,研究了自然对流条件下环形翅片管几何参数对其对流换热性能的影响.结果表明:随翅片间距的增大,单位长度散热量先增大后减小,表面平均自然对流换热系数及单位面积散热量先增大后基本稳定不变;翅片厚度对换热性能的影响随间距变化而变化.通过模拟计算,为自然对流条件下翅片管的优化设计提供了参考.%Applying numerical simulation, the paper studies the effect of fin spacing and fin thickness of circumferential finned tube on natural convection heat transfer performance. The results indicate that, with the increase of fin spacing, unit length heat dissipating capacity increases at the previous period and decreases at the later period. The average surface convection coefficient of heat transfer and unit surface area heat dissipating capacity increase at first and then keep constant. The effect of fin thickness on heat transfer performance changes along with the fin spacing. By simulation, it provides reference to the optimization design of finned tube.

  4. Calculation base of flooded type evaporators with finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Brod, W.; Slipcevic, B.

    1989-03-01

    For the construction of flooded type evaporators with halogen refrigerants, the refrigeration industry is using finned tubes. Equations for thermodynamical calculations of the apparaturs are given, and explained with the aid of a calculation example.

  5. Numerical Analysis for Optimal Design of Fin and Tube Type Adsorber

    Science.gov (United States)

    Kariya, Keishi; Kuwahara, Ken; Shigeru, Koyama

    Adsorption cooling systems driven by low temperature waste heat (below 100°C) or renewable energy sources have gained considerable attention as one of the solutions for both energy and environment related problems. In this study, a two dimensional numerical analysis is carried out to evaluate the adsorption characteristics and to determine the performance of a fin and tube type adsorber/desorber heat exchanger; activated carbon fiber (ACF) of type A-20, which has relatively higher surface area, and ethanol are used as adsorbent/refrigerant pair. The effects of heat exchanger design configurations such as fin height, fin thickness, fin pitch, tube diameter and apparent density of ACF bed on the performance are examined numerically. The simulation results show that the cooling capacity can be optimized in the condition of fin height 15mm and fin pitch 5.5mm when other parameters are fixed.

  6. Heat transfer of smooth and finned tubes in A CFBC

    Energy Technology Data Exchange (ETDEWEB)

    Kim, B.H. [Korea Electric Power Research Institute, Taejeon (Korea); Cho, H.H. [Yonsei University, Seoul (Korea)

    2000-11-01

    The objective of present work is to investigate experimentally the characteristics of heat transfer. A fluidized bed combustion has advantages of pollution control, fuel flexibility and excellent heat transfer. The present study investigates fundamental phenomena of bed-to-surface heat transfer in high temperature fluidized beds to improve design of immersed tube surface. The tested operating variables are bed temperature, superficial velocity, mean size of bed material, and the rake angle of fin. Generally, heat transfer rates between the fluidized bed and immersed finned-tube are much higher than those of a smooth tube. A life time of finned-tube is generally longer than that of smooth tube. (author). 4 figs.

  7. Application of cross finned tubes in latent heat storages

    Energy Technology Data Exchange (ETDEWEB)

    Schwind, H.; Wolff, D. (Dortmund Univ. (Germany, F.R.). Lehrstuhl fuer Anlagentechnik); Brose, J. (Dortmund Univ. (Germany, F.R.). Arbeitsgruppe Chemieapparatebau)

    1978-01-01

    Heat storages, utilizing the latent heat of materials have in comparison with sensible heat storages the two fundamental advantages of small storage volumes and constant temperatures during charge and discharge. Known storage systems in the field of industrial heating may be replaced advantageous by latent heat storage systems. A new latent heat storage, applying storage material around vertical arranged cross finned tubes is presented. It results in good heat transfer rates and avoids degredation and stratification of salthydrates during operation. The scaling-up of a single cross finned tube to a compact unit with plate fins seems to be practicable without problems. Some experimental results are presented.

  8. The effect of the fin structural parameters to the heat transfer performance of the vertical fin and flat tube heat exchangers%翅片结构参数对纵向翅片扁管换热器换热性能的影响

    Institute of Scientific and Technical Information of China (English)

    陈俊华; 陶丽; 顾平道; 汤国芳

    2011-01-01

    Taking the vertical fin and flat tube heat exchanger as a research exemple, the effects of the fin length, the fin height and the fin pitch upon the heat transfer performance were analyzed. At the same time, the fin structure parameters were also optimized. A group of better fin structural parameters were obtained when the import speed of wind is 2m/s. These optimized parameters were 400mm of fin length, 25mm of fin height and 2.7mm of fin pitch.%以纵向翅片扁管换热器为研究对象,分析翅片长度、翅片高度及翅片间距对换热性能的影响,并对换热器的翅片结构参数进行优化,得出进口风速为2m/s时理想的翅片结构参数为:翅片长度为400mm、翅片高度为25mm、翅片间距为2.7mm.

  9. Computation of boiling water on circular finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Fan, C.C.; Liaw, S.P. [National Taiwan Ocean Univ., Keelung (Taiwan, Province of China). Dept. of Mechanical and Marine Engineering

    1999-04-01

    This study investigates the maximum heat transfer rate and the critical temperature of circular finned tubes in a boiling liquid. The analysis is conducted numerically by solving a two-dimensional heat conduction equation in a steady state. The dependence between heat flux and the temperature at the inner wall of the tube is quantified. Varying the width, height, and pitch of fins, an optimal finned tube with efficient heat transfer rate can be obtained. In the theoretical approach the successive over relaxation (S.O.R.) accompanied with Multi-grid scheme is used. The local heat transfer rates are assumed to follow power-law-type temperature dependence. The initial guess at very high temperatures or so-called a cooling process is also executed in a same way. The results reveal that increasing either the width or the height of a fin increases the total heat transfer rate.

  10. Numerical Study on the Effect of Tube Rows on the Heat Transfer Characteristic of Dimpled Fin

    Directory of Open Access Journals (Sweden)

    Xuehong Wu

    2014-09-01

    Full Text Available The dimpled fin has excellent heat transfer performance and has attracted a lot of attention to apply on the fin and tube heat exchanger. A study presents to investigate the effects of number of tube rows on the air-side heat transfer characteristics of dimpled fin for velocity ranging from 1 to 3 m/s. The Q/ΔP and Q/((ΔP × V are used to evaluate the heat transfer performance of the heat exchanger. The results show that the dimpled arrangement can change the mainstream direction, increase the disturbance, and enhance the heat transfer. With the increase of the number of tube rows, the average Nusselt number decreases and Q/ΔP and Q/((ΔP × V increase gradually. Compared with the multipipe tube rows, the performance of two-row tube is better.

  11. Effect of Fin Geometry on Condensation of Zeotropic Refrigerant Mixture R407C in a Staggered Bundle of Horizontal Finned Tubes

    Science.gov (United States)

    Honda, Hiroshi; Takata, Nobuo; Takamatsu, Hiroshi; Kim, Jeongsik; Usami, Keiichiro

    Row-by-row heat transfer data were obtained during condensation of downward-flowing refrigerant mixture R407C in a staggered bundle of horizontal finned tubes. Two kinds of conventional low-fin tubes with flat-sided annular fins and three kinds of three-dimensional fin tubes were tested. The refrigerant mass velocity ranged from 4 to 23 kg/m2s, and the condensation temperature difference from 1.5 to 12 K. At a low to medium film Reynolds number(2000), on the other hand, the highest performance was obtained by one of the low-fin tubes. For all tubes tested, the heat transfer coefficient decreased with decreasing mass velocity. On the basis of previous results for R134a, consideration was given to the characteristics of vapor phase mass transfer of R407C.

  12. Chemical milling of Zircaloy tubing to produce integral OD spiral finned tubes (AWBA development program)

    Energy Technology Data Exchange (ETDEWEB)

    Horwood, W.A.

    1982-02-01

    A detailed process description is provided for producing integral spiral fins on the outside surface of Zircaloy nuclear fuel cladding tubes by masking with pressure sensitive tape strips and then chemical milling (pickling) the tube wall between the tape strips to leave the fins in relief. Fins up to 0.020 inch high by 0.05 to 0.12 inch wide were consistently produced on tubes having wall thickness of 0.008 inch or greater after fin pickling. Wall thickness uniformity was excellent. Information is provided on tube surface preparation to maximize tape mask adhesion time during pickling, acid chemistry control to prevent local tube wall thinning near the fin, and pickling techniques to promote uniform material removal. Simple fixture designs are described for quickly and conveniently applying the tape strips to the tube wall in an accurate spiral. 13 figures, 4 tables.

  13. Experimental determination of heat transfer and friction in helically-finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Zdaniuk, Gregory J. [Ramboll Whitbybird Ltd., 60 Newman Street, London W1T 3DA (United Kingdom); Chamra, Louay M.; Mago, Pedro J. [Department of Mechanical Engineering, Mississippi State University, 210 Carpenter Engineering Building, P.O. Box ME, Mississippi State, MS 39762-5925 (United States)

    2008-01-15

    Heat transfer coefficients and friction factors were determined experimentally for eight helically-finned tubes and one smooth tube using liquid water at Reynolds numbers ranging from 12,000 to 60,000. The helically-finned tubes tested in this investigation have helix angles between 25 and 48 , number of fin starts between 10 and 45, and fin height-to-diameter ratios between 0.0199 and 0.0327. An uncertainty analysis was completed and plain-tube results were compared to the Blasius and Dittus-Boelter equations with satisfactory agreement. Power-law correlations for Fanning friction and Colburn j-factors were developed using a least-squares regression. The performance of the correlations was evaluated with data of other researchers with average prediction errors between 30% and 40%. (author)

  14. Condensation and evaporation of new refrigerants in advanced micro-finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Laterrible, P. [Trefimetaux, 92 - Courbevoie (France); Marvillet, C. [CEA/Grenoble, Dept. de Thermohydraulique et de Physique (DTP-GRETH), 38 (France)

    1999-07-01

    Due to the European deadline for the phase-out of HCFCs, the air-conditioning manufacturers are launching new product range purpose-designed to operate on the non-ozone depleting refrigerants: R404A, R134a or R407C. The micro-finned tubes optimised for finned heat exchangers as for shell and tube evaporators and condensers are one of these recent techniques which may allow increase performance of refrigerating units the new refrigerants. Two models of thermal correlation have been established resulting from experimental measurements on single micro-fin tubes: in evaporation, the model is a modification of Gungor-Winterton which concerns the addition of nucleation and convection processes within the inner grooves. In condensation, this model is a modification of Cavallini-Zecchin correlation. With these models, it is possible to predict the behaviour micro-fin tubes in specific conditions. This permits the necessary adaptation of heat-exchangers. (authors)

  15. Heat Transfer of Tube-fin Heat Exchanger Having Parallel Louver Continuous Fins

    Science.gov (United States)

    Take-Uchi, Masaaki; Yamada, Jun; Tanaka, Jun-Ichirou

    Heat transfer from tubes has been numerically simulated in a fan coil unit for an airconditioning equipment. The array of tubes has parallel louver continuous fins, perpendicular to staggered round tubes. Quite a few of slits divide plates into many strips, which are offsetted, so that the heat transfer will be augmented from the plate to the air flow. On the other hand, the conduction of heat in the platemight be prevented with these slits. The conduction retardation due to slit is estimated, and the simulation shows that the retardation is not serious for present fins.

  16. Effective Heat Transfer Enhancement in Finned Tube Heat Exchanger with Different Fin Profiles

    Directory of Open Access Journals (Sweden)

    J.A.Livingston1 , P. Selvakumar2

    2013-04-01

    Full Text Available During cross flow in a heat exchanger, heat transfer in the front portion of the tube is more compared to back portion of the tube. This is due to less formation of vortices at the backside of the tube. For uniform heat transfer to take place throughout the tube, it is necessary to increase the vortex formation at the rear side of the tube. The aim of this study is to explore the possibilities of improving the flow structure and thereby increasing uniform heat transfer around the tubes by introducing special type of fin arrangement over the tubes. The effect of shape and orientation of the fin on vortex generation and respective heat transfers are studied numerically. It have been identified that by introducing special type of fin arrangement over the tube there is a possibility for increase the vortex formation at the rear portion of the tube, which significantly leads to creation of uniform heat transfer all around the tube.

  17. 波纹穿圆孔翅片管换热器换热特性的数值模拟%Numerical Simulation of Heat Exchange Performance of Corrugated Fin-and-tube Heat Exchangers with Circular Holes

    Institute of Scientific and Technical Information of China (English)

    秦萌; 尤学一

    2015-01-01

    The air-side flow and heat transfer performance of corrugated fin-and-tube heat exchangers with circular holes were studied by simulation method carried out by FLUENT software. The effects of two factors on corrugated fin-and-tube heat exchangers with circular holes were analyzed:fin pitch(1.6~2.8mm)and fin thickness(0.14~0.26mm). A comparison was made between the variation range of Re from 819 to 5735 and simulation data of corrugated fins. The simulation results showed that the circular holes caused rather great disturbance to the air flow over the fins,and the heat transfer effect was improved. Under the same conditions,the heat exchange amount of the air-side fins with circular holes was about 20.8%more than that of corrugated fins. In addition,the corresponding pressure drop loss only increased by about 11.2%. In the circular-hole-fin heat exchangers,the Nu number increased with the increase of fin pitch and thickness;however,the friction factor always aggrandized with the increase of fin thickness and decreased with the increase of fin pitch.%采用 FLUENT 数值模拟方法,对波纹穿圆孔翅片管换热器空气侧流动和传热特性进行研究,分析出翅片厚度(1.6~2.8,mm)与翅片间距(0.14~0.26,mm)对换热特性的影响,并选择 Re在819到5735变化范围内与波纹翅片的模拟数据相比较.结果表明,穿圆孔对翅片上空气流动产生了较大的扰动作用,增强了换热.在相同条件下,穿圆孔翅片空气侧的换热量比波纹翅片大20.8%,左右,压力降仅增大11.2%,.穿圆孔翅片换热器中,Nu 数随着翅片间距和厚度的增加均会增加,但阻力因子f 随翅片厚度的增加而增加,随翅片间距的增加而减小.

  18. Condensation heat transfer on finned tubes with radial ridges on the fin surfaces. 2nd Report. ; Theoretical study. Hankei hoko ni tokki wo motsu shuhoko fin ni yoru gyoshuku netsu dentatsu sokushin. 2. ; Rironteki kenkyu

    Energy Technology Data Exchange (ETDEWEB)

    Hijikata, K.; Nakabeppu, O. (Tokyo Inst. of Technology, Tokyo (Japan)); Wang, P.

    1991-05-25

    A model of finned tubes is developed to predict condensation performance of R-tubes with radial ridges circumferential fin surfaces. Results predicted by this model make an accurate explanation of experimental data, and the condensation mechanism of R-tubes and freon {prime} s condensation heat transfer to R-tubes are predicted by the model R-tubes have high condensation heat transfer coefficients because the ridges on the fin surfaces of the R-tube extend the thin condensate film area and also promote convective heat transfer in the film. In condensation of high performance finned tubes, load values like local temperature differences, local heat flux, local heat transfer coefficient change circumferentially. Therefore, it is necessary to consider this change using theoretical models. 17 refs., 9 figs.

  19. Heat transfer during boiling at finned tubes and finned tube bundles; Der Waermeuebergang beim Sieden an Rippenrohren und Rippenrohrbuendeln

    Energy Technology Data Exchange (ETDEWEB)

    Chen Qiurong

    1991-06-10

    Based on bubble dynamics at single tubes and hydrodynamics at multi-tube arrangements (a vertical tube row, tube bundle), a theory for calculation of heat transfer at single tubes, at a vertical tube row and at tube bundles was developed. The theory applies both to finned tubes and plain tubes. To verify the presented theory, measured heat transfer coefficients taken from literature are recalculated. A comparison between heat transfer coefficients for single tubes and two-tube arrangements, calculated according to the theory and determined by measurements shows good agreement. Measuring results for plain tube bundles and bundles of finned tubes also agree well with the theory. (orig./MM) [Deutsch] Aufbauend auf der Blasendynamik an Einzelrohren und der Hydrodynamik in Mehrrohranordnungen (eine senkrechte Rohrreihe, Rohrbuendel) wurde eine Theorie zur Berechnung des Waermeuebergangs an Einzelrohren, an einer senkrechten Rohrreihe und an Rohrbuendeln entwickelt. Die Theorie gilt sowohl fuer Rippenrohre als auch fuer Glattrohre. Zur Ueberpruefung der vorgestellten Theorie werden gemessene Waermeuebergangskoeffizienten aus der Literatur nachgerechnet. Ein Vergleich zwischen den nach der Theorie berechneten und den aus Messungen ermittelten Waermeuebergangskoeffizienten fuer Einzelrohre und Zweirohranordnungen zeigt gute Uebereinstimmung. Auch die Messergebnisse von Glattrohrbuendeln und von Buendeln mit den Rippenrohren lassen sich durch die Theorie gut wiedergeben. (orig./MM)

  20. Numerical Analysis on Optimization of a Fin and Tube Type Adsorber/Desorber Heat Exchanger using ACF/C2H5OH Pair

    Science.gov (United States)

    Kariya, Keishi; Kuwahara, Ken; Koyama, Shigeru

    This study deals with a two dimensional numerical analysis of the fin and tube type adsorber/desorber heat exchanger design such as fin height, fin pitch, fin thickness and tube diameter effect on the performance of closed adsorption cooling system with activated carbon fiber (ACF) of type A-20, which has relatively higher surface area, and ethanol pair. The simulation results show that the fin tube diameter is effective on the performance of the heat exchanger. It is also found that the cycle COP can be optimized in the condition of fin pitch 4.5mm and fin height 20mm, respectively when other parameters are fixed.

  1. Numerical study of a round tube heat exchanger with louvered fins and delta winglets

    Science.gov (United States)

    Huisseune, H.; T'Joen, C.; De Jaeger, P.; Ameel, B.; De Paepe, M.

    2012-11-01

    Louvered fin and round tube heat exchangers are widely used in air conditioning devices and heat pumps. In this study the effect of punching delta winglet vortex generators in the louvered fin surface is studied numerically. The delta winglets are located in a common-flow-down orientation behind each tube of the staggered tube layout. It is shown that the generated vortices significantly reduce the size of the tube wakes. Three important heat transfer enhancement mechanisms can be distinguished: a better flow mixing, boundary layer thinning and a delay in flow separation from the tube surface. The compound heat exchanger has a better thermal hydraulic performance then when only louvers or only delta winglets are used. Comparison to other enhanced fin designs clearly shows its potential, especially for low Reynolds number applications.

  2. Forced Convective Condensation of Nonazeotropic Refrigerant Mixtures in Horizontal Annulus with Petal Shaped Fin Tubes

    Institute of Scientific and Technical Information of China (English)

    WangShiping; ZhouXinqiu; 等

    1995-01-01

    In this paper,condensation performance in horizontal annulus was compared with a smooth tube,one Saw-Tooth Finned tube(STF tube),four Petal Shaped Fin tubes(PF tubes),using R113,R11 and their mixtures(vapor molar fractions of R11 at the test section inlet were 0.384,0.588and 0.809) as working fluid.The mass flux at the test section ranged from 15-220/m2s。Camera and video camera were used to shoot the flow pattern and condensation phenomena.The condensation transfer coefficient(hc) of mixtures were considerably lower than those of pure fluid,and did not change linearly with composition.The maximum degradation of measured hc from the ideal value were 23% for the smooth tube,65%for STF tube,67% for PF tubes,which occurred in the composition range of 0.4-0.6 vapor molar fraction of R11.For the condensation of mixture,R11 molar fraction from 38%to 81%,the PF tubes had the highest value of hc.which were 10-25% higher than those of STF tubes,and 480-580% higher than that of smooth tube,because the petal shaped fins of PF tubes could promote strong turbulence in the two phase flow,and reduce the mass transfer resistance.

  3. Experimental study on condensation heat transfer enhancement by various kinds of integral finned tubes. Hankei hoko ni tokki wo motsu shuhoko fin ni yoru gyoshuku netsudentatsu sokushin

    Energy Technology Data Exchange (ETDEWEB)

    Hijikata, K. (Tokyo Inst. of Technology., Tokyo (Japan)); Wang, S.

    1990-07-25

    Condensation heat transfer enhancement by a finned tube having radial ridges on the fin surface (called the R-tube), was investigated. Thermoexcel-C has a flat fin surface, while the R-tube has ridges on the fin surface, consequently the mean heat-transfer coefficient of the R-tube is 30-40% higher than that of Thermoexcel-C, in spite of same condensing areas in the two. The function of ridges on the fin surface of the R-tube to heat transfer enhancement, is remarkable. It is considered that a thin condensate film is formed on the tip of ridges, in the same way as that on the tip of fin without having ridges. The ridges disturb the flow of condensate in the channel, and promote a convective heat transfer due to an agitation action. Though the R-tube shows superior performance than other heat transfer tubes, the mechanisms of heat transfer enhancement are different in the upper part and the lower part of the tube. In the upper part of the tube, the effect of heat transfer enhancement due to the formation of thin film region by the ridges, is predominant. And in the lower part, the enhancement effect due to the convective heat transfer by the agitation of the condensate, is important. 13 refs., 10 figs., 1 tab.

  4. Experimental Study on Condensation of Pure Refrigerants in Horizontal Micro-fin Tubes

    Science.gov (United States)

    Yonemoto, Ryuichiro; Koyama, Shigeru

    This paper presents the heat transfer and pressure drop correlations for condensation in micro-fin tubes. Experimental data for eleven micro-fin tubes with different fin dimensions were used, and the refrigerants tested were R22, R123 and R134a. The predicted results using new correlations show good agreement with experimental results within an absolute deviation of ±30%. Experimental results for the micro-fin tubes were also compared with previous correlations for micro-fin Tubes.

  5. Experimental investigation of heat transfer and pressure drop in fin-tube waste heat recovery heat exchangers

    OpenAIRE

    2014-01-01

    The aim of this master thesis was to investigate heat transfer and pressure drop of fin-tube heat exchangers. Experimental investigations of heat transfer and pressure drop in fin-tube bundles has been performed. The main focus was to investigate the influence of the fin height and the fin tip clearance. The effect of the uneven heat transfer distribution on the heat transfer coefficient has been analyzed.A literature survey has been dedicated to investigate the influence of the fin height an...

  6. Finned double-tube PCM system as a waste heat storage

    Science.gov (United States)

    Alhamdo, M. H.; Theeb, M. A.; Golam, A. S.

    2015-11-01

    In this work, focus is taken on developing a waste heat recovery system for capturing potential of exhaust heat from an air conditioner unit to be reused later. This system has the ability to store heat in phase change material (PCM) and then release it to a discharge water system when required. To achieve this goal, a system of Finned, Water-PCM, Double tube (FWD) has been developed and tested. Different profiles of fins attached to the (FWD) system have been investigated for increasing the thermal conductivity of the PCM. These include using Circular Finned, Water-PCM, Double tube (CFWD) system; Longitudinal Finned, Water-PCM, Double tube (LFWD) system; Spiral Finned, Water-PCM, Double tube (SFWD) system; as well as; Without Fins, Water-PCM, Double tube (WFWD) system. An experimental test rig that attached to an air-conditioner unit has been built to include 32- tubes of the FWD systems for both vertical and horizontal layouts during charging and water discharging processes. Results show a significant performance improvement when using spiral and circular fins during charging process at vertical position. However, longitudinal and without fins showed better performance in horizontal position. Overall, the developed SFWD system in vertical position has been found to exhibit the most effective type due to the fastest PCM melting and solidification. As compared to the WFWD system, the FWD systems have been found to increase the PCM temperature gain of about 15.3% for SFWD system; 8.2% for CFWD; and 4.3% for LFWD system.

  7. Selection criteria for plain and segmented finned tubes for heat recovery systems

    Science.gov (United States)

    Reid, D. R.; Taborek, J.

    1994-04-01

    Heat recovery heat exchangers with gas as one of the streams depend on the use of finned tubes to compensate for the inherently low gas heat transfer coefficient. Standard frequency welded 'plain' fins were generally used in the past, until the high-frequency resistance welding technology permitted a cost-effective manufacture of 'segmented' fins. The main advantage of this fin design is that it permits higher heat flux and hence smaller, lighter weight units for most operating conditions. While the criteria that dictate optimum design, such as compactness, weight, and cost per unit area favor the segmented fin design, a few other considerations such as fouling, ease of cleaning, and availability of dependable design methods have to be considered. This paper analyzes the performance parameters that affect the selection of either fin type.

  8. Selection criteria for plain and segmented finned tubes for heat recovery systems

    Energy Technology Data Exchange (ETDEWEB)

    Reid, D.R. (FINTUBE Corp., Tulsa, OK (United States)); Taborek, J. (Taborek (J.), Virginia Beach, VA (United States))

    1994-04-01

    Heat recovery heat exchangers with gas as one of the streams depend on the use of finned tubes to compensate for the inherently low gas heat transfer coefficient. Standard frequency welded plain'' fins were generally used in the past, until the high-frequency resistance welding technology permitted a cost-effective manufacture of segmented'' fins. The main advantage of this fin design (Fig. 1) is that it permits higher heat flux and hence smaller, lighter weight units for most operating conditions. While the criteria that dictate optimum design, such as compactness, weight, and cost per unit area favor the segmented fin design, a few other considerations such as fouling, ease of cleaning, and availability of dependable design methods have to be considered. This paper analyzes the performance parameters that affect the selection of either fin type.

  9. Energy conservation performance of finned-tube heat exchanger under frosting condition%变间距对称圆孔翅片管式换热器结霜工况下的节能性能

    Institute of Scientific and Technical Information of China (English)

    方赵嵩; 王厚华

    2012-01-01

    利用风洞试验装置试验研究变间距对称圆孔翅片管式换热器在结霜工况下的制冷性能.研究结果证明:在迎面平均风速为1.87~4.30 m/s时,在同等试验条件下,变间距对称圆孔翅片管式制冷换热器的制冷量在低风速下比非变间距圆孔翅片管式制冷换热器换热量提高7.6%,当量表面传热系数提高18.26%,阻力减小48.85%,节省21.43%的翅片金属材料.%In order to investigate the refrigeration performance of finned-tube heat exchanger with changing fin spacing and symmetrical holes under frosting conditions, a wind-tunnel experiment on the energy conservation performance was carried out. The experimental results show that in the range of head-on-average velocity from 1.87-4.30 m/s, comparing the finned-tube refrigeration heat exchanger with no-changing fin spacing and holes, in the same experimental condition and geometric size, the cooling capacity of the former exchanger increases by 7.6%; the surface of the fin heat transfer coefficient raises by 18.26%; and the resistance decreases by 48.85% with saving 21.43% metal material of fin in lower velocity.

  10. Compensation of airflow maldistribution in fin-and-tube evaporators

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Tiedemann, Thomas

    2012-01-01

    Compensation of airflow maldistribution in fin-and tube evaporators for residential air-conditioning is investigated with regards to circuitry design and control of individual channel superheats. In particularly, the interlaced and the face split circuitry designs are compared numerically using...

  11. Fin formation model during pre-roll ploughing of copper 3D outside fin tube

    Institute of Scientific and Technical Information of China (English)

    2001-01-01

    The mechanism of pre-roll ploughing for 3D fins on the outside surface of copper tube was studied systematically, and especially the process and conditions of 3D fin formation were analyzed. The right mathematical model was also established. Based on the volume of fin ploughed out is equal to the volume of the metal extruded up by the extruding face of the tool, the relations between fin height, pre-roll ploughing feed and pre-roll ploughing depth have been achieved. With the increase of pre-roll ploughing depth which must be equal to groove depth, the fin height gradually becomes larger. There are different critical feeds with the various depths of pre-roll ploughing. The pre-roll ploughing feed is the critical one, the height of fin is largest. And when the feed is above the critical one, the fin height will reduce with the increase of feed. The theoretical analysis basically accords with experimental results.

  12. Detailed analysis of fin-and-tube evaporators

    OpenAIRE

    2009-01-01

    This paper is devoted to the presentation of a new model for fin-and-tube evaporators, focusing on the solid core simulation and its integration with a quasi-homogeneous two-phase flow model for the in-tube refrigerant flow. Special attention is dedicated to separated in-tube flow patterns (stratified, stratified-wavy), because of their importance in liquid overfeed evaporators and the impact on the solid core temperature distribution. The paper presents the solid core formulation and nume...

  13. Bundle impact with th condensation of propane at horizontal smooth tubes and finned tubes; Buendeleffekt bei der Kondensation von Propan an horizontalen Glatt- und Rippenrohren

    Energy Technology Data Exchange (ETDEWEB)

    Gebauer, Thomas; Leipertz, Alfred; Froeba, Andreas Paul [Erlangen-Nuernberg Univ., Erlangen (Germany). Lehrstuhl fuer Technische Thermodynamik (LTT); Gotterbarm, Achim; El Hajal, Jean [Wieland-Werke AG, Ulm (Germany)

    2012-07-01

    With respect to a basic description of the bundling impact in tube bundle condensers, the authors of the contribution under consideration report on the impact of the material properties of the working fluid, tube structure and tube material on the heat transfer. For this, the existing experimental database on the condensate side heat transfer coefficient with 1.1.1.2-tetrafluoroethane (R134a) has been extended by the natural refrigerant propane (R290). In addition to plain tubes, standard finned tubes and high-performance finned tubes consisting of copper, ribbed and grooved steel finned tubes were used. The experimental condensation tests were carried out at the outside of the tube at a saturation temperature of 37 Celsius. By expanding the data base, both analytical models and a CFD model for predicting the condensate side heat transfer coefficient on the smooth and finned tube a well as corresponding single tube bundles could be verified. The results on single smooth tube showed a very good agreement between the condensate side heat transfer coefficients of propane and R134a with the Nusselt theory. The largest side condensate heat transfer coefficients were determined at the single high-performance finned tube made of copper and the corresponding tube bundle with R134a. Compared to the standard finned tubes of both materials, the high-performance finned copper tubes showed a greater bundling effect for both working fluids. Unlike R134a, almost no differences were observed for the experimentally determined behavior of the bundle on standard finned tubes and high-performance finned tube made of steel with propane. The condensation side heat transfer coefficients on the latter two tubes were below the values for the finned copper tubes with propane. The CFD simulations for the single tube were within the experimental uncertainties. In the case of the investigations of bundles, the modeled data showed a larger deviation from the experimental data than the

  14. Experimental Investigation of Heat Transfer and Pressure Drop Characteristics of H-type Finned Tube Banks

    OpenAIRE

    2014-01-01

    H-type finned tube heat exchanger elements maintain a high capacity for heat transfer, possess superior self-cleaning properties and retain the ability to effect flue gas waste heat recovery in boiler renovations. In this paper, the heat transfer and pressure drop characteristics of H-type finned tube banks are studied via an experimental open high-temperature wind tunnel system. The effects of fin width, fin height, fin pitch and air velocity on fin efficiency, convective heat transfer coe...

  15. Experimental studies on pressure drop characteristics of cryogenic cross-counter flow coiled finned tube heat exchangers

    Science.gov (United States)

    Gupta, Prabhat Kumar; Kush, P. K.; Tiwari, Ashesh

    2010-04-01

    Cross-counter flow coiled finned tube heat exchangers used in medium capacity helium liquefiers/refrigerators were developed in our lab. These heat exchangers were developed using integrated low finned tubes. Experimental studies have been performed to know the pressure drop characteristics of tube side and shell side flow of these heat exchangers. All experiments were performed at room temperature in the Reynolds number range of 3000-30,000 for tube side and 25-155 for shell side. The results of present experiments indicate that available correlations for tube side can not be used for prediction of tube side pressure drop data due to complex surface formation at inner side of tube during formation of fins over the outer surface. Results also indicate that surface roughness effect becomes more pronounced as the value of di/ D m increases. New correlations based on present experimental data are proposed for predicting the friction factors for tube side and shell side.

  16. Transient response of finned-tube condenser in household refrigerators

    Energy Technology Data Exchange (ETDEWEB)

    Porkhial, S. [Technical Department, Karaj Branch, Islamic Azad University, Tehran (Iran); Khastoo, B. [Mechanical Engineering Department, Amirkabir University, Tehran (Iran); Modarres Razavi, M.R. [Mechanical Engineering Department, Ferdowsi University, Mashhad (Iran)

    2006-10-15

    A distributed parameter model for prediction of the transient performance of a condenser is presented. The model is capable of predicting the refrigerant temperature distribution, tube wall temperature, quality of refrigerant, inventory mass of refrigerant as a function of position and time. An efficient two-level iteration method is proposed to obtain the numerical solution of the model without solving a large set of non-linear equations simultaneously. A finned tube condenser of 12ft{sup 3} refrigerator with R12 as working fluid was chosen as a sample and some tests were carried out to determine its transient response. The examination of results indicates that the theoretical model provides a reasonable prediction of dynamic response compared to the experimental data. Transient behavior of temperature, pressure, mass flow rate, mass of liquid and vapor of refrigerant, quality, heat transfer in household refrigerators have been presented. Also time-dependent displacement of interface between saturated and superheated regions has been shown. Extensive examinations of theoretical and experimental results show that with utilization of a controllable compressor, power consumption can be reduced. (author)

  17. The optimization of fin-tube heat exchanger with longitudinal vortex generators using response surface approximation and genetic algorithm

    Science.gov (United States)

    Wu, Xuehong; Liu, DanDan; Zhao, Min; Lu, YanLi; Song, Xiaoyong

    2016-09-01

    Delta winglet works better than other vortex generators in improving the performance of fin-tube heat exchangers. In this paper, Response Surface Approximation is used to study the effects of the fin pitch, the ratio of the longitudinal tube pitch to transverse tube pitch, the ratio of both sides V 1 , V h of delta winglets and the attack angle of delta winglets on the performance of fin-tube heat exchanger. Firstly, Twenty-nine numerical group experiments including five times repeated experiments at the central point are conducted. Then, the analyses of variable (ANOVA) and regression are performed to verify the accuracy of the polynomial coefficients. Finally, the optimization of the fin-tube heat exchanger using the Genetic Algorithm is conducted and the best performance of j/f (1/3) is found to be 0.07945, which is consistent with the numerical result.

  18. 管翅式热管换热器性能分析%Performance Research of Tube fin of Heat pipe Heat Exchanger

    Institute of Scientific and Technical Information of China (English)

    任常在; 代元军; 赵龙广

    2014-01-01

    一款具有新型结构的热管换热器,与传统的此类换热器相比,新装置可以方便地安装螺旋型翅片,使其换热效果在不变的基础上增加了除尘的功能。针对所设计的一种新型热管换热器,本文采用FLUENT软件对其进行模拟。模拟结果表明,改进之后的新型换热器不但换热效率有所提高,而且具有一定的除尘能力,这种新型换热器采用的是螺旋翅片形式的热管,烟气流通区域存在有环形流道,这种设计的好处是,它使得灰尘颗粒在翅片管以及换热器内壁表面聚集,同时由于重力作用,这些灰尘在达到一定重量后就会沿着翅片的倾角降落到排灰斗中。%A gravity type heat pipe heat exchanger has be designed in the paper. Compared to traditional heat pipe heat exchanger,the new equipment can add fins strengthening heat transfer conveniently. The new equipment increasing the dust removal function while the effect of heat transfer was no change. this issue developed a new heat pipe heat exchanger, and made numerical simulation by the software of FLUENT. This new type heat exchanger not only has high thermal efficiency, but also has certain dusting ability, its internal heat pipe adopting spiral finned tube form,the flue gases side and water side are circular runner. This kind of unique internal structure made the dust particles in the flue gases easy to deposit on the surface of spiral finned tube and in wall, and in the pull of gravity the dust particles falls down to the ash hopper.

  19. Three-dimensional optimization of staggered finned circular and elliptic tubes in forced convection

    Energy Technology Data Exchange (ETDEWEB)

    Matos, R.S.; Vargas, J.V.C. [Departamento de Engenharia Mecanica, Centro Politecnico, Universidade Federal do Parana, Caixa Postal 19011, PR 81531-990, Curitiba (Brazil); Laursen, T.A. [Department of Civil and Environmental Engineering, Duke University, 27708-0287, Durham, NC (United States); Bejan, A. [Department of Mechanical Engineering and Materials Science, Duke University, 27708-0300, Durham, NC (United States)

    2004-05-01

    This paper presents a three-dimensional numerical and experimental geometric optimization study to maximize the total heat transfer rate between a bundle of finned tubes in a given volume and external flow, for staggered arrangements of circular and elliptic tubes. Experimental results were obtained for circular and elliptic configurations with twelve tubes, starting with an equilateral triangle configuration, which fitted uniformly into the fixed volume with a resulting optimal dimensionless tube-to-tube spacing of S/2b = 1.5, where S is the actual spacing and b is the smaller semi-axis of the ellipse. Several experimental configurations were built by reducing the tube-to-tube spacings, identifying the optimal spacing for maximum heat transfer. Similarly, it was possible to investigate the existence of optima with respect to two other geometric degrees of freedom, such as tube eccentricity and fin-to-fin spacing. The results are reported for air as the external fluid in the laminar regime, for Re{sub L} = 852 and 1065, where L is the swept length of the fixed volume. Circular and elliptic arrangements with the same flow obstruction cross-sectional area were compared on the basis of maximizing the total heat transfer. This criterion allows one to isolate and quantify the heat transfer gain, by studying arrangements with equivalent total pressure drops independently of the tube cross-section shape. This paper continues with three-dimensional numerical optimization results for finned circular and elliptic tubes arrangements, which are validated by direct comparison with experimental measurements. Global optima with respect to tube-to-tube spacing, eccentricity and fin-to-fin spacing (S/2b{approx_equal}0.5, e{approx_equal}0.5, {phi}{sub f}{approx_equal}0.06 for Re{sub L}=852 and 1065) were found and reported in dimensionless terms. A relative heat transfer gain of up to 19% is observed in the optimal elliptic arrangement, as compared to the optimal circular one. The

  20. A theoretical model of film condensation in a bundle of horizontal low finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H.; Nozu, S.; Takeda, Y. (Okayama Univ. (Japan))

    1989-05-01

    The previous theoretical model of film condensation on a single horizontal low finned tube is extended to include the effect of condensate inundation. Based on the flow characteristics of condensate on a vertical column of horizontal low finned tubes, two major flow modes, the column mode and the sheet mode, are considered. In the column mode, the surface of the lower tubes is divided into the portion under the condensate column where the condensate flow is affected by the impinging condensate from the upper tubes, and the portion between the condensate columns where the condensate flow is not affected by the impinging condensate. In the sheet mode, the whole tube surface is assumed to be affected by the impinging condensate. Sample calculations for practical conditions show that the effects of the fin spacing and the number of vertical tube rows on the heat transfer performance is significant for R-12, while the effects are small for steam. The predicted value of the heat transfer coefficient for each tube row compares well with available experimental data, including four fluids and five tube bundles.

  1. Numerical Analysis of Tube-Fin Heat Exchanger using Fluent

    Directory of Open Access Journals (Sweden)

    M. V. Ghori

    2012-08-01

    Full Text Available Three-dimensional CFD simulations are carried out to investigate heat transfer and fluid flow characteristics of two-row plain Tube and Fin heat exchanger using FLUENT software. Heat transfer and pressure drop characteristics of the heat exchanger are investigated for Reynolds numbers ranging from 330 to 7000. Model geometry is created and meshed by using GAMBIT software. Fluid flow and heat transfer are simulated and results compared using both laminar and turbulent flow models k-, and SST k-omega, with steady-state solvers to calculate pressure drop, flow, and temperature fields. Model validation is carried out by comparing the simulated value friction factor f and Colburn factor j to experimental results investigate by Wang. Reasonable agreement is found between the simulations and experimental data, and the fluent software has been sufficient for simulating the flow fields in tube-fin heat exchangers.

  2. Mixed convection laminar flow and heat transfer of liquids in horizontal internally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Shome, B. [Univ. of Delaware, Newark, DE (United States). Dept. of Mechanical Engineering

    1998-01-01

    Energy and material savings, as well as economic incentives, have led to concentrated efforts over the past several decades in the field of heat transfer enhancement to produce more efficient and compact heat exchangers. Internally finned tubes are widely used for heat transfer enhancement, particularly in chemical process and petroleum industries. A finned tube heat exchanger with optimum geometry could offer 35--40% increase in heat duty for equal pumping power and size over a smooth tube heat exchanger or a comparable decrease in the heat exchanger size for a given heat duty. Developing mixed convection flow in internally finned tubes with variable viscosity was numerically investigated for a fin geometry range of 8 {le} N {le} 24, 0.1 {le} H {le} 0.3 and an operating condition range of 50 {le} Pr{sub in} {le} 1,250, 0 {le} Ra{sub in} {le} 10{sup 7}, and 0 {le} q{sub w}d/k{sub in} {le} 2,000. The numerical model was validated by comparison with existing numerical and experimental data. Internal finning was found to produce a complex two-cell, buoyancy-induced vortex structure. The results show that coring (retarded velocity in the interfin region) leads to poor heat transfer performance of tubes with large numbers of fins or with tall fins. The overall results indicated that large enhancement in the heat transfer can be obtained in the entrance region. Furthermore, variable viscosity effects are seen to have a pronounced effect on the friction factor and Nusselt number predictions.

  3. Laser Welding Of Finned Tubes Made Of Austenitic Steels

    OpenAIRE

    Stolecki M.; Bijok H.; Kowal Ł.; Adamiec J.

    2015-01-01

    This paper describes the technology of welding of finned tubes made of the X5CrNi1810 (1.4301) austenitic steel, developed at Energoinstal SA, allowing one to get high quality joints that meet the requirements of the classification societies (PN-EN 15614), and at the same time to significantly reduce the manufacturing costs. The authors described an automatic technological line equipped with a Trumph disc laser and a tube production technological process. To assess the quality of the joints, ...

  4. Effect of Vapor Velocity during Condensation on Horizontal Finned Tubes

    Science.gov (United States)

    1988-12-01

    surface area (m2 ) b Fin spacing (mm) Ci Sieder -Tate type coefficient used in Equation (4.5) C p Specific heat of cooling water (J/kgK) Di Inside diameter...and auxiliary condensers, together with the energy lost to the environment. Raw data were processed immediately using an assumed value for the Sieder ...sets were collected, the data were reprocessed using a new Sieder -Tate coefficient found by the modified Wilson method. 40 F. TUBES TESTED For this

  5. Film Condensation of Steam on Externally Finned Horizontal Tubes.

    Science.gov (United States)

    1985-03-01

    Area Based on the Fin Diameter b - Experimentally Determined Constant B - Constant Used in the Sieder -Tate-Type Equation c - Experimentally Determined...Constant C - Leading Coefficient for the Sieder -Tate-Type Equation C1 - Constant of Proportionality d - Experimentally Determined Constant De...leading constants for the Sieder -Tate equation used to determine the water-side heat-transfer coefficient. Data taken on smooth tubes were used to

  6. Absorber Tube with Internal Pin-Fins for Solar Parabolic Trough Collector

    Directory of Open Access Journals (Sweden)

    Kalidasan B.

    2016-01-01

    Full Text Available Solar parabolic trough collectors exploit solar energy for power generation in solar thermal power stations. These systems require long arrays of reflective troughs with absorber tube running along the axis of parabolic dish. A successful attempt to reduce the length of arrays was accomplished by experimentally analysing the modifications done in absorber tube. Two out of three tubes were fabricated and they were employed to obtain the performance parameters through experimentation conducted at VIT University, Vellore, India. Distilled water was used as the working fluid. Maximum efficiency of 39.12% was obtained at 451.6 W/m2 of direct normal irradiance (DNI for absorber tube with internal pin-fins and without glass tube (AFWGt compared to 8.15% obtained at same value of DNI and other conditions for simple absorber tube without glass cover (AWGt. Cylindrical parabolic trough available at the university was utilized, providing the basis for designing and fabrication of the tubes. Plots for varying mass flow rate at interval of 10 minutes were made against instantaneous thermal efficiency and heat utilized, for direct normal irradiance vs. temperature difference across the tubes and instantaneous thermal efficiency. Through the experimentation conducted, better performance was procured compared to earlier works. Thus, the proposal infers that absorber tube with internal fins has good scope for its application, both domestically as well as industrially. It also calls for further research and development of proposed techniques so as to achieve better performance curves.

  7. Influence of the degree of thermal contact in fin and tube heat exchanger

    DEFF Research Database (Denmark)

    Singh, Shobhana; Sørensen, Kim; Condra, Thomas Joseph

    2016-01-01

    Present work aims to investigate the significance of thermal contact area between fins and tubes in a heat exchanger. The heat exchanger type selected for the study is a liquid-gas fin and tube heat exchanger. Four different cases namely I, II, III, and IV, based on a variable degree of thermal...... is simulated in the present study. The performance of the heat exchanger is characterized in terms of overall heat transfer coefficient, Colburn j-factor, flow resistance factor, and efficiency index. Results obtained from numerical modeling are useful to examine the impact of the degree of thermal contact...... element method (FEM) are developed for the different cases studied. Conjugate heat transfer mechanism coupled with turbulent flow is simulated to elucidate temperature and velocity profiles. In order to develop a simplified model with desired physical phenomena, only gas-side flow over the fin...

  8. The cooling heat transfer characteristics of the supercritical CO2 in micro-fin tube

    Science.gov (United States)

    Lee, Ho-Saeng; Kim, Hyeon-Ju; Yoon, Jung-In; Choi, Kwang-Hwan; Son, Chang-Hyo

    2013-02-01

    This study intended to verify the cooling heat transfer characteristics of supercritical gas for refrigerating and air-conditioning devices that use CO2, a natural refrigerant, as the operating fluid. Experiments were performed with a gas cooler, which was the test part. The gas cooler was a heat exchanger made of a micro-fin tube with an inner diameter of 4.6 mm and an outer diameter of 5.0 mm. The experiment results are summarized as follows. The heat transfer coefficient, according to the mass flux, peaked at the low cooling pressure of 8.0 MPa in the gas cooler, and reached its minimum at the high pressure of 10.0 MPa. Furthermore, when the mass flux of the refrigerant increased, the coefficient increased faster with the lower cooling pressure in the gas cooler. The heat transfer coefficient, according to the shape of the heat transfer tube, showed that the maximum values of the CO2 cooling heat transfer coefficients of the smooth tube and the micro-fin tube were found at 44.7 °C, which were the pseudo-critical temperatures for the entrance pressures. It was found that the cooling heat transfer coefficient of the micro-fin tube increased by 12-39 % more than that of the smooth tube. The experiment results for the CO2 heat transfer coefficients of the smooth tube and the micro-fin tube were compared with the results estimated from previous correlations. It was found that the experiment values generally significantly differed from and the experiment values greater than the estimated values. The differences were especially greater in the vicinity of the critical temperature points. Based on these results, a new correlation was suggested that includes the density ratio and the specific heat ratio.

  9. 几种环形翅片管通道内流体流动与换热特性的对比研究%Comparative Study on Fluid Flow and Heat Transfer Performance in the Channel of Annular Finned Tube

    Institute of Scientific and Technical Information of China (English)

    欧龙姣; 阴继翔; 武广剑; 杨宇伟; 阴勇光

    2016-01-01

    采用 Fluent软件,对基管相同的圆翅片管和5种椭圆翅片管用稳态RNGκ-ε模型进行三维数值模拟,5种椭圆翅片管Afin ,Amin ,De ,Per ,β分别与圆翅片(Cir )有相同的翅片面积、最小截面面积、翅片当量直径、翅片周长和翅化比.通过对不同雷诺数(Re)下流场及翅片表面局部努塞尔数(Nu)的分析比较,得到翅片管通道内流体流动及换热的特征,并提供了圆翅片管和5种椭圆翅片管的综合换热性能Nu/f 的结果.研究表明,圆翅片Cir的Nu大于椭圆翅片Afin ,De ,Per ,β,但小于椭圆翅片Amin .圆翅片的阻力系数f大于椭圆翅片Afin ,Per ,β的f ,且小于椭圆翅片Amin的f.椭圆翅片De 在Re 较小(Re≤8000)时与圆翅片Cir的f的差值较小,在Re较大(Re>8000)时与圆翅片Cir基本相同.椭圆翅片Amin的综合换热效果最好.%The three dimensional numerical simulation of circular finned tube and 5 kinds of elliptical fin tube is performed with the steady state RNGκ-εmodel by the Fluent software.The base pipes of the cir-cular finned tube and five elliptical finned tubes are same.Fluid field and local Nusselt number on fin surface are analyzed and compared for different Reynolds numbers (Re)to obtain fluid flow and heat transfer characteristics in the channel of annular finned tube,and the result of comprehensive heat trans-fer coefficient (Nu/f)on a circular finned tube and 5 elliptical finned tubes is also provided.The results show that the Nu of circular fin is biggest among elliptical fin Afin ,elliptical fin De ,elliptical fin Per and elliptical finβ,but it is smaller than elliptical fin Amin .The flow resistance coefficient of circular fin is biggest among elliptical fin Afin ,elliptical fin Per and elliptical finβ,but it is smaller than elliptical fin Amin .The results of Thermal Resistance is contrary to Nusselts.The difference of flow resistance coeffi-cient between elliptical fin De,and the circular fin is small when the

  10. Effect of Fin Geometry on Condensation Heat Transfer of Refrigerant R134a on Enhanced Finned Tubes

    Science.gov (United States)

    Takahashi, Hiroyuki; Saeki, Chikara; Koyama, Shigeru

    This paper presents the experimental results on the outside condensation heat tral1sfer coefficient of horizontal enhanced filmed tubes. Three different fin geometry types of three-dimensional enhanced finned tubes were tested. A low-fin-tube (LFT) 19 fin-per-inch (fpi) was also tested for reference. Experimental refrigerant used was R134a. The heat tral1sfer coefficient test was carried out at a condensing temperature of 40°C, at a cooling water velocity of 1.5 m/s, and the heat flux of 10 to 110 kW/m2K. The outside condensation heat transfer coefficient of all three dimensional enhanced finned tubes were approximately 1.9 times higher than that of LFTl9fpi at high heat flux range. In low heat flux range, the enhanced finned tube of small circumferential segmentation pitches at the fin tip was shown the highest outside heat transfer coefficient for all tubes tested.

  11. Heat transfer enhancement of finned oval tubes with staggered punched longitudinal vortex generators

    Energy Technology Data Exchange (ETDEWEB)

    Chen, Y.; Fiebig, M.; Mitra, N.K. [Ruhr-Universitaet Bochum (Germany). Inst. fuer Thermo- und Fluiddynamik

    2000-02-01

    Punched longitudinal vortex generators in form of winglets in staggered arrangements were employed to enhance heat transfers in high performance finned oval tube heat exchanger elements. Three-dimensional hydrodynamically and thermally developing laminar flow (Re = 300) and conjugate heat transfer in finned oval tubes were calculated by solving the Navier-Stokes and energy equations with a finite-volume method in curvilinear grids. Velocity field, pressure distribution, vortex formation, temperature fields, local heat transfer distributions and global results for finned oval tubes with two to four staggered winglets ({beta}= 30{sup o}, {lambda} = 2, h =H) were presented and compared. Winglets in staggered arrangement bring larger heat transfer enhancement than in in-line arrangement since the longitudinal vortices from the former arrangement influence a larger area and intensify the fluid motion normal to the flow direction. For Re = 300 and Fi = 500, the ratios of heat transfer enhancement to flow loss penalty (j/j{sub 0})/( f/f{sub 0}) were 1.151 and 1.097 for a finned oval tube with two and four staggered winglets, respectively. (author)

  12. Constructal design of finned tubes used in air-cooled heat exchangers

    Energy Technology Data Exchange (ETDEWEB)

    Shokouhmand, Hossein; Mahjoub, Shoeib [University of Tehran, Tehran (Iran, Islamic Republic of); Salimpour, Mohammad Reza [Isfahan University of Technology, Isfahan (Iran, Islamic Republic of)

    2014-06-15

    The present study documents the constructal design and optimization of finned tubes used in air-cooled heat exchangers. The considered tubes are equipped with annular fins. The aim is to minimize the overall thermal resistance by morphing the geometry. The geometrical and thermo-physical parameters considered are the number of fins, ratio of fin height to tube diameter, Stanton number, ratio of fin conductivity to air conductivity, ratio of in-tube fluid conductivity to air conductivity and dimensionless pressure drop. Two constraints are applied in the optimization process: fixed overall volume of heat exchanger and fixed volume fraction of fin material. It is found that there exist optimal values for the number and the height of fins. Moreover, the optimal heat transfer has an extremum in a special volume fraction of fin material.

  13. Investigation of enhancement of steam condensation heat transfer on finned tubes with porous drainage strips

    Energy Technology Data Exchange (ETDEWEB)

    Liu Xijuan; Ma Tongze; Zhang Zhengfang

    1999-07-01

    Condensation of steam on horizontal finned tube with porous drainage strip was investigated experimentally and theoretically. Composite metal screens were used as porous drainage strip. Distilled water was taken in the experiments as working fluid. The experiments were carried out to find the structure effects of composite screen drainage strip on the condensation heat transfer on finned tubes with fin spacing of 0.5mm. Influences of the mesh number of both outer and inner layers and of length and thickness of the drainage strip were investigated. The outer layers of the screens have the mesh numbers of 100, 150, 185 and 220, which lead to different effective pore radius; the inner layers have the mesh numbers of 20, 30 and 40, which lead to different permeability. Strip lengths are 15mm, 20mm and 30mm, while the thickness is 2mm, 4mm and 6mm. Experimental results show that the structure parameters of the porous drainage strip strongly influence condensation on the finned tube. A porous strip having small effective pore radius on the outer layer as well as large permeability, reasonably large length and thickness will lead to excellent performance. In the tested ranges, for steam condensation on a 0.5mm spacing finned tube, the optimum structure of a composite screen drainage strip is of 150 mesh outer layer screen, 20 mesh inner layer screen, 30mm long and 4mm thick. The enhanced condensation heat transfer coefficients are equivalent to 1.15{approximately}1.74 times that of the finned tube and 2.08{approximately}3.08 times that of the plain tube. A new prediction model of condensation on finned tube with porous drainage strip was established. The condensate flow in the interfin grooves and in the porous strip was treated as flow through two kinds of porous medium with different structures. The momentum equation of single phase flow in porous medium was used to solve the condensate flow. The equation was analyzed and several terms were neglected because of their

  14. Numerical Modeling of Fin and Tube Heat Exchanger for Waste Heat Recovery

    DEFF Research Database (Denmark)

    Singh, Shobhana; Sørensen, Kim; Condra, Thomas Joseph

    In the present work, multiphysics numerical modeling is carried out to predict the performance of a liquid-gas fin and tube heat exchanger design. Three-dimensional (3D) steady-state numerical model using commercial software COMSOL based on finite element method (FEM) is developed. The study...... associates conjugate heat transfer phenomenon with the turbulent flow to describe the variable temperature and velocity profile. The performance of heat exchanger design is investigated in terms of overall heat transfer coefficient, Nusselt number, Colburn j-factor, flow resistance factor, and efficiency...... between fin and tube. The present numerical model predicts the performance of the heat exchanger design, therefore, can be applied to existing waste heat recovery systems to improve the overall performance with optimized design and process-dependent parameters....

  15. Local Heat Transfer for Finned-Tube Heat Exchangers using Oval Tubes

    Energy Technology Data Exchange (ETDEWEB)

    O' Brien, James Edward; Sohal, Manohar Singh

    2000-08-01

    This paper presents the results of an experimental study of forced convection heat transfer in a narrow rectangular duct fitted with either a circular tube or an elliptical tube in crossflow. The duct was designed to simulate a single passage in a fin-tube heat exchanger. Heat transfer measurements were obtained using a transient technique in which a heated airflow is suddenly introduced to the test section. High-resolution local fin-surface temperature distributions were obtained at several times after initiation of the transient using an imaging infrared camera. Corresponding local fin-surface heat transfer coefficient distributions were then calculated from a locally applied one-dimensional semi-infinite inverse heat conduction model. Heat transfer results were obtained over an airflow rate ranging from 1.56 x 10-3 to 15.6 x 10-3 kg/s. These flow rates correspond to a duct-height Reynolds number range of 630 – 6300 with a duct height of 1.106 cm and a duct width-toheight ratio, W/H, of 11.25. The test cylinder was sized such that the diameter-to-duct height ratio, D/H is 5. The elliptical tube had an aspect ratio of 3:1 and a/H equal to 4.33. Results presented in this paper reveal visual and quantitative details of local fin-surface heat transfer distributions in the vicinity of circular and oval tubes and their relationship to the complex horseshoe vortex system that forms in the flow stagnation region. Fin surface stagnation-region Nusselt numbers are shown to be proportional to the square-root of Reynolds number.

  16. Experimental Investigation of Heat Transfer and Pressure Drop Characteristics of H-type Finned Tube Banks

    Directory of Open Access Journals (Sweden)

    Heng Chen

    2014-11-01

    Full Text Available H-type finned tube heat exchanger elements maintain a high capacity for heat transfer, possess superior self-cleaning properties and retain the ability to effect flue gas waste heat recovery in boiler renovations. In this paper, the heat transfer and pressure drop characteristics of H-type finned tube banks are studied via an experimental open high-temperature wind tunnel system. The effects of fin width, fin height, fin pitch and air velocity on fin efficiency, convective heat transfer coefficient, integrated heat transfer capacity and pressure drop are examined. The results indicate that as air velocity, fin height and fin width increase, fin efficiency decreases. Convective heat transfer coefficient is proportional to fin pitch, but inversely proportional to fin height and fin width. Integrated heat transfer capacity is related to fin efficiency, convective heat transfer coefficient and finned ratio. Pressure drop increases with the increase of fin height and fin width. Finally, predictive correlations of fin efficiency, Nusselt number and Euler Number are developed based on the experimental data.

  17. Numerical Analysis on Adsorption Characteristics of Activated Carbon/Ethanol Pair in Finned Tube Type Adsorber

    Science.gov (United States)

    Makimoto, Naoya; Kariya, Keishi; Koyama, Shigeru

    The cycle performance of adsorption cooling system depends on the thermophysical properties of the adsorbent/refrigerant pair and configuration of the adsorber/desorber heat exchanger. In this study, a twodimensional analysis is carried out in order to clarify the performance of the finned tube type adsorber/desorber heat exchanger using a highly porous activated carbon powder (ACP)/ethanol pair. The simulation results show that the average cooling capacity per unit volume of adsorber/desorber heat exchanger and coefficient of performance (COP) can be improved by optimizing fin thickness, fin height, fin pitch and tube diameter. The performance of a single stage adsorption cooling system using ACP/ethanol pair is also compared with that of activated carbon fiber (ACF)/ethanol pair. It is found that the cooling capacities of each adsorbent/refrigerant pair increase with the decrease of adsorption/desorption time and the cooling capacity of ACP/ethanol pair is approximately 2.5 times as much as that of ACF/ethanol pair. It is also shown that COP of ACP/ethanol pair is superior to that of ACF/ethanol pair.

  18. An experimental study on condensation heat transfer of low-finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Kim, Nae Hyun [University of Inchon, Inchon (Korea, Republic of); Jung, In Kwon; Kim, Kyung Hoon [Kumoh National University of Technology, Kumi (Korea, Republic of)

    1995-05-01

    Low-fin tubes are widely used to enhance condensation heat transfer. In this study. condensation heat transfer experiment was conducted on the low-fin tube using R-11. Three different fin densities-787 fpm (fins per meter), 1102 fpm. 1378 fpm-were tested. The results show that low-fin tube enhances the condensation heat transfer considerably. The enhancement increases as the fin density increases. It was also found that the fin shape and height have a significant effect on the condensation heat transfer coefficient. slender or high fins showed a higher condensing heat transfer coefficient compared with fat, low fins. For the tube with 1378 fpm, however, excessive fin height decreased the condensing heat transfer coefficient. The reason may be attributed to the increasing condensate retention angle as the fin density increases. The experimental data are compared with exiting prediction models. Results show that Webb`s surface tension model predicted the data best (within {+-} 20 %), which confirms that surface tension plays the major role in low-fin tube condensation. (author). 13 refs., 12 figs., 1 tab.

  19. Experimental investigation into effects of ultrasonic vibration on pool boiling heat transfer performance of horizontal low-finned U-tube in TiO2/R141b nanofluid

    Science.gov (United States)

    Chang, Tong-Bou; Wang, Zi-Long

    2016-11-01

    An experimental investigation was performed into the pool boiling heat transfer performance of a low-finned U-tube immersed in TiO2/R141b nanofluid with four different nanoparticle loadings (0, 0.0001, 0.001, and 0.01 vol%). The energy-dispersive X-ray spectrometry results revealed that some of the TiO2 nanoparticles adhered to the heated surface during boiling, and therefore increased the thermal resistance. The heat transfer performance of the nanofluids with particle loadings of 0.0001, 0.001 and 0.01 vol% was thus found to be reduced by around 10, 20 and 50 %, respectively, compared to that of pure R141b refrigerant. Accordingly, an ultrasonic vibration crusher was used to inhibit the formation of the TiO2 nano-sorption layer on the U-tube surface. The ultrasonic vibration suppressed the deposition of TiO2 nanoparticles and improved the heat transfer performance of the nanofluids as a result. Of the four working fluids, the nanofluid with a particle loading of 0.0001 vol% yielded the optimal heat transfer performance (i.e., a heat transfer coefficient around 30 % higher than that of pure R141b refrigerant.)

  20. Heat Transfer between Horizontal Finned Tubes and a Gas-Solid Fluidized Bed

    Energy Technology Data Exchange (ETDEWEB)

    Grewal, N.S.; Cheung, T.K.; Saxena, S.C.

    1985-04-01

    The heat-transfer coefficients are measured between electrically heated V-thread tubes and square fluidized beds of alumina and silica sand. The effect of particle size, mass fluidizing velocity, V-thread pitch, and tube pitch on the heat transfer rate is investigated. One-dimensional and two-dimensional heat conduction models are developed for determining the temperature distribution in a V-thread fin. The models are used to calculate the corrected heat-transfer coefficients for the finned tubes. A correlation for the fin effectiveness factor is proposed and is found to be reliable to predict its value for finned tubes with geometry and orientation similar to that in the present investigation. The correlation in conjunction with the existing correlatins for the heat-transfer coefficient for smooth tubes is found, in general, to predict the coefficients for finned tubes immersed in a fluidized bed within + or - 25%.

  1. 对具有复杂流路布置的翅片管换热器的性能仿真与分析%Numerical simulation and analysis of performance of fin-and-tube heat exchanger with complex circuit arrangement

    Institute of Scientific and Technical Information of China (English)

    刘建; 魏文建; 丁国良; 王凯建

    2005-01-01

    With the help of the description methods in graph theory and the adaptive adjustment metnod, a steady sate simulation model for fin-and-tube heat exchanger with complex circuit arrangement was developed. This model could provide better compatibility and accuracy for the design of heat exchanger with complex circuit arrangement. Using this model, six typical fin-and-tube heat exchangers with different circuit arrangements were analyzed. The counter flow arrangement could not always achieve the best performance. With appropriate compound arrangement, the performance of heat exchanger could be improved by 2%-4%.

  2. Study of integral characteristics and efficiency of a heat exchanger of thermosyphon type with finned tubes

    Directory of Open Access Journals (Sweden)

    Iliev Iliya K.

    2016-01-01

    Full Text Available The experimental research aims at the analysis of the thermal performance of a gas-liquid heat exchanger in a pilot plant. Results of the conducted experiment with a finned tubes thermosyphon heat exchanger using natural gas are presented. The installation was mounted at the exit of a flue gas from an existing steam generator “PK-4” with total power of 2.88 MW in the boiler room of Vini, Sliven, Bulgaria. Different experiments were carried out at different loads of the steam generator in order to determine the efficiency of the heat exchanger. Based on these results the coefficient of heat transfer of flue gas to the finned tubes was determined, based on different modes of operation with crossed and straight pipe bundles. The effectiveness-number of transfer units method was used.

  3. Optimization of a Finned Shell and Tube Heat Exchanger Using a Multi-Objective Optimization Genetic Algorithm

    Directory of Open Access Journals (Sweden)

    Heidar Sadeghzadeh

    2015-08-01

    Full Text Available Heat transfer rate and cost significantly affect designs of shell and tube heat exchangers. From the viewpoint of engineering, an optimum design is obtained via maximum heat transfer rate and minimum cost. Here, an analysis of a radial, finned, shell and tube heat exchanger is carried out, considering nine design parameters: tube arrangement, tube diameter, tube pitch, tube length, number of tubes, fin height, fin thickness, baffle spacing ratio and number of fins per unit length of tube. The “Delaware modified” technique is used to determine heat transfer coefficients and the shell-side pressure drop. In this technique, the baffle cut is 20 percent and the baffle ratio limits range from 0.2 to 0.4. The optimization of the objective functions (maximum heat transfer rate and minimum total cost is performed using a non-dominated sorting genetic algorithm (NSGA-II, and compared against a one-objective algorithm, to find the best solutions. The results are depicted as a set of solutions on a Pareto front, and show that the heat transfer rate ranges from 3517 to 7075 kW. Also, the minimum and maximum objective functions are specified, allowing the designer to select the best points among these solutions based on requirements. Additionally, variations of shell-side pressure drop with total cost are depicted, and indicate that the pressure drop ranges from 3.8 to 46.7 kPa.

  4. 3-D NUMERICAL STUDY AND COMPARISON OF ECCENTRIC AND CONCENTRIC ANNULAR-FINNED TUBE HEAT EXCHANGERS

    OpenAIRE

    2015-01-01

    The use of 3-D computational fluid dynamics (CFD) is proposed to simulate the conjugate conduction-convection of heat transfer problems in eccentric annularfinned tube heat exchangers. The numerical simulation results allow us to evaluate the heat transfer coefficient over fin surfaces, the fin efficiency and the pressure drop. The aim of the present paper is to determine the optimum tube position in the circular fin that maximizes heat dissipation and minimizes pressure drop. In addition, th...

  5. Efficient heat-transfer surfaces assembled from partially finned flat-oval tubes

    Science.gov (United States)

    Pis'mennyi, E. N.

    2011-04-01

    The state of finned convective heat-transfer surfaces and prospects for using them in power engineering and industry are briefly reviewed. The characteristics of a heat-recovery economizer made of partially finned flat-oval tubes are presented by way of comparing them with design versions employing known types of finned tubes, and the results gained from its operation downstream of a PTVM-30M boiler are given.

  6. Effect of fin geometry on condensation of downward-flowing R123/R134a in a staggered bundle of horizontal low-finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H.; Takamatsu, H.; Takata, N. [Kyushu Univ., Institute of Advanced Material Study, Fukuoka (Japan)

    1999-07-01

    Experiments were conducted to obtain row-by-row heat and mass transfer data during condensation of downward-flowing zeotropic mixture R123/R134a in a staggered bundle of horizontal low-finned tubes. The vapor temperature and the mass fraction of R134a at the tube bundle inlet were about 50 deg C and 14%, respectively. The refrigerant mass velocity ranged from 9 to 33 kg/m{sup 2}s, and the condensation temperature difference from 2 to 10 K. Four kinds of low-finned tubes with different fin geometry were tested. The highest heat transfer coefficient was obtained with a tube which showed the highest performance for R123. However, the difference among the tubes was much smaller for the mixture than for R123. The heat transfer coefficient and the vapor-phase mass transfer coefficient decreased significantly with decreasing mass velocity. The mass transfer coefficient increased will condensation temperature difference, which was due to the effect of suction associated with condensation. On the basis of the analogy between heat and mass transfer, a dimensionless correlation of the mass transfer coefficient was developed for each tube. (authors)

  7. Experimental measurements for condensation of downward-flowing R123/R134a in a staggered bundle of horizontal low-finned tubes with four fin geometries

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H.; Takamatsu, H.; Takata, N. [Kyushu Univ., Kasuga, Fukuoka (Japan). Inst. of Advanced Material Study

    1999-07-01

    Experiments were conducted to obtain row-by-row heat and mass transfer data during condensation of downward-flowing zeotropic mixture R123/Rl34a in a staggered bundle of horizontal low-finned tubes. The vapor temperature and the mass fraction of R134a at the tube bundle inlet were about 50{sup o}C and 14%, respectively. The refrigerant mass velocity ranged from 9 to 34 kg m{sup -2} s{sup -1}, and the condensation temperature difference from 1.9 to 12 K. Four kinds of low-finned tubes with different fin geometry were tested. The highest heat transfer coefficient was obtained with a tube which showed the highest performance for R123. However, the difference among the tubes was much smaller for the mixture than for R123. The heat transfer coefficient and the vapor-phase mass transfer coefficient decreased significantly with decreasing mass velocity. The mass transfer coefficient increased with condensation temperature difference, which was due to the effect of suction associated with condensation. On the basis of the analogy between heat and mass transfer, a dimensionless correlation of the mass transfer coefficient was developed for each tube. (author)

  8. Numerical prediction of laminar flow and heat transfer in internally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Rustum, I.M.

    1990-02-01

    An investigation was carried out to provide a detailed analysis of laminar fluid flow and heat transfer in internally finned pipes. Three mathematical models were formulated for this purpose, and shown to be capable of simulating the actual situation of pressure drop and heat transfer in such tubes. Steady, laminar forced convection heat transfer in the thermal entrance region of internally finned tubes was investigated numerically for the case of fully developed hydrodynamics using the H1 and T thermal boundary conditions. Steady, laminar fluid flow in the hydrodynamic entrance region of internally finned tubes was investigated numerically. Results are presented for the smooth tube geometry and sixteen geometries corresponding to various combinations of relative fin heights and number of fins. Steady, laminar mixed convection in the fully developed region of horizontal internally finned tubes was investigated for the case of uniform heat input axially and uniform wall temperature circumferentially. Fluid flow and heat transfer characteristics were found to be dependent on a modified Grashof number, Prandtl number, relative fin height, and number of fins. Internal finning was found to retard the onset of significant free convective effects and to suppress the enhancement in friction factor and Nusselt number compared to smooth tubes. 54 refs., 93 figs., 12 tabs.

  9. Magnetic Heat Transfer Enhancements on Fin-Tube Heat Exchangers

    Institute of Scientific and Technical Information of China (English)

    Yan SU; C.T. HSU

    2007-01-01

    通过DNS方法解耦合的三维非稳态流动和固流体能量方程组,本文研究了两平行磁质平板和圆管所组成的肋片式圆管换热器单元与震荡流体间的传热过程.对不同的磁场频率和振幅的三维动态流热场的模拟结果表明增强磁场频率和振幅能很有效地增加周期平均传热强度达到强化传热的目的.%Two narrowly-gapped magnetic parallel plates embedding a circular disk was considered as a unit-cell to represent the fin-tube heat exchanger where heat from a circular tube was dissipated by a series of parallel equally-spaced thin plates in normal to the tube. The unsteady 3-D continuity,Navier-Stokes and energy equations for fluids and solids describing the convective heat transfer for the unit-cell geometry were solved numerically with DNS method. The present study aims on using oscillating flows and magnetic fields to enhance the heat transfer for various amplitudes and frequencies of the magnetic field. Results from cycle-averaged heat fluxes from the cylinder wall show that the increase in magnetic amplitude and frequency will greatly enhance the heat transfer. The effects of the oscillating magnetic field were discussed and the three dimensional flow and temperature fields were also presented.

  10. Finned tubes in purified gas heat exchangers of flue gas desulfurization plant

    Energy Technology Data Exchange (ETDEWEB)

    O' Donnell, J. Jr.; Meyer, T.H.

    1985-01-01

    The use of helical rolled, corrosion resistant finned tubes in the purified gas heat exchangers of flue gas desulfurization plant has considerable economic advantages over conventional heat exchangers with smooth tubes. As a result of a threefold larger external surface and hence improved heat transfer properties, heat exchangers with finned tubes can be made considerably smaller. The weight and space requirements are reduced and the pressure drop also falls owing to the smaller diameter. Thus piping, pumps, and fittings can all be made smaller. Moreover, deposition on the finned tubes is considerably lower. It is found that finned tubes can be recommended in all cases where the difference in heat transfer coefficients between the inside and the outside of the tube is considerable. (orig.).

  11. A Prediction Model for Condensation on Single Horizontal Rectangular Fin Tube

    Institute of Scientific and Technical Information of China (English)

    LiuXijuan; MaTongze; 等

    1997-01-01

    A model was established to predict condensation heat transfer coefficient on horizontal rectangularfinned tube.Drop-Off zone at the tube bottom was considered and determined,the known Honda (and Owen) expression of retention angle was also modified as a result of considering drop-off zone.Heat flux on fin tips in the unflooded region,fin flanks,fin spacings and fin tips in the flooded region were analyzed respectively.COndensation on fin tips in emphasized by considering the variation of film thickness along circumference as well as horizontally.FIn efficiency was considered in calculation.The prediction results were compared with several researchers' experimental data for three kinds of working fluids on seven different tube geometries and for various temperature differences,These data under about 60 test conditions were predicted with discrepancy of ±10% .Prediction by the present model for steam and R-113 condensation were compared with previous models.

  12. Laminar fluid flow and heat transfer in a fin-tube heat exchanger with vortex generators

    Energy Technology Data Exchange (ETDEWEB)

    Yanagihara, J.I.; Rodriques, R. Jr. [Polytechnic School of Univ. of Sao Paolo, Sao Paolo (Brazil). Dept. of Mechanical Engineering

    1996-12-31

    Development of heat transfer enhancement techniques for fin-tube heat exchangers has great importance in industry. In recent years, heat transfer augmentation by vortex generators has been considered for use in plate fin-tube heat exchangers. The present work describes a numerical investigation about the influence of delta winglet pairs of vortex generators on the flow structure and heat transfer of a plate fin-tube channel. The Navier-Stokes and Energy equations are solved by the finite volume method using a boundary-fitted coordinate system. The influence of vortex generators parameters such as position, angle of attack and aspect ratio were investigated. Local and global influences of vortex generators in heat transfer and flow losses were analyzed by comparison with a model using smooth fin. The results indicate great advantages of this type of geometry for application in plate fin-tube heat exchangers, in terms of large heat transfer enhancement and small pressure loss penalty. (author)

  13. 3-D NUMERICAL STUDY AND COMPARISON OF ECCENTRIC AND CONCENTRIC ANNULAR-FINNED TUBE HEAT EXCHANGERS

    Directory of Open Access Journals (Sweden)

    FAROUK TAHROUR

    2015-11-01

    Full Text Available The use of 3-D computational fluid dynamics (CFD is proposed to simulate the conjugate conduction-convection of heat transfer problems in eccentric annularfinned tube heat exchangers. The numerical simulation results allow us to evaluate the heat transfer coefficient over fin surfaces, the fin efficiency and the pressure drop. The aim of the present paper is to determine the optimum tube position in the circular fin that maximizes heat dissipation and minimizes pressure drop. In addition, this study analyzes the effects of fin spacing and fin tube diameter on heat transfer and flow characteristics for a range of Reynolds numbers, 4500≤Re≤22500. A satisfactory qualitative and quantitative agreement was obtained between the numerical predictions and the results published in the literature. For small fin spacings, the eccentric annular finned tube is more efficient than the concentric one. Among the cases examined, the average heat transfer coefficient of the eccentric annular-finned tube, for a tube shift St =12 mm and a Reynolds number Re = 9923, was 7.61% greater than that of the concentric one. This gain is associated with a 43.09% reduction in pressure drop.

  14. Experimental Study on Cooling Heat Transfer of Supercritical Carbon Dioxide Inside Horizontal Micro-Fin Tubes

    Science.gov (United States)

    Kuwahara, Ken; Higashiiu, Shinya; Ito, Daisuke; Koyama, Shigeru

    This paper deals with the experimental study on cooling heat transfer of supercritical carbon dioxide inside micro-fin tubes. The geometrical parameters in micro-fin tubes used in the present study are 6.02 mm in outer diameter, 4.76 mm to 5.11 mm in average inner diameter, 0.15 mm to 0.24 mm in fin height, 5 to 25 in helix angle, 46 to 52 in number of fins and 1.4 to 2.3 in area expansion ratio. Heat transfer coefficients were measured at 8-10 MPa in pressure, 360-690 kg/(m2•s) in mass velocity and 20-75 °C in CO2 temperature. The measured heat transfer coefficients of micro-fin tubes were 1.4 to 2 times higher than those of the smooth tube having 4.42 in inner diameter. The predicted heat transfer coefficients using the correlation equation, which was developed for single-phase turbulent fluid flow inside micro-fin-tubes, showed large deviations to the measured values. The new correlation to predict cooling heat transfer coefficient of supercritical carbon dioxide inside micro-fin tubes was developed taking into account the shape of fins based on experimental data empirically. This correlation equation agreed within ±20% of almost all of the experimental data.

  15. Flow structure of natural dehumidification over a horizontal finned-tube

    Science.gov (United States)

    Hirbodi, Kamran; Yaghoubi, Mahmood

    2016-08-01

    In the present study, structure of water drops formation, growth, coalescence and departure over a horizontal finned-tube during natural dehumidification is investigated experimentally. Starting time of repelling the drops as well as heat transfer rate and the rate of dripping condensates in quasi-steady-state conditions are presented. Furthermore, cold airflow pattern around the horizontal finned-tube is visualized by using smoke generation scheme during natural dehumidification process. The finned-tube has a length of 300 mm, and inner and outer fin diameters, fin thickness and fin spacing are 25.4, 56, 0.4 and 2 mm, respectively. The tests are conducted in an insulated control room with dimensions of 5.8 m × 3 m × 4 m. Ambient air temperature, relative humidity and fin base temperature are selected from 25 to 35 °C, from 40 to 70 % and from 4 to 8 °C, respectively. Observations show that natural condensation from humid air over the test case is completely dropwise. Droplets only form on the edge of the fin and lateral fin surfaces remain almost dry. Dehumidification process over the tested finned-tube is divided into four stages; nucleation, formation, growth and departure of drops. It is also observed that the condensate inundation leaves the tube bottom in the form of droplets. Smoke visualization depicts that humid airflows downward around the cold finned-tube surface without noticeable turbulence and separation in the initial stages of dehumidification process. But the airflow has some disturbances in the intermediate stage and especially during drop departure on the edge of the fins.

  16. Heat transfer with phase change around finned cylindrical tubes: Theory and experiments

    Energy Technology Data Exchange (ETDEWEB)

    Kamal, A.; Alves, C.L.F.; Ismail, R.

    1983-12-01

    In order to increase the heat transfer rate and reduce the convective effects in latent heat storage tanks externally finned cylinderical tubes are used where the working fluid passes inside the tubes and the finned part submerged in the phase change material. A mathematical model is developed using the enthalpy approach and the numerical treatment is done using an ADI technique. Numerical results showing the effect of fin thickness, number of fins, length of fin and ratio of diameters of inner to outer tube are obtained, analysed and discussed. It is found that fin thickness has very little effect on the heat transfer rate. Number of fins, length of fin and ratio of inner to outer diameters are found to be great effect as can be verified from attached grafs. An experimental rig is designed, installed and instrumented in order to verify the theoretical findings and the validity of the model. Various cupper tubes models are used with Ecusan parrafin as phase change material. Models with 3, 4, 5 and 7 fins are used. Fins of various length are also used. Experimental results obtained are plotted to compare with the theoretical results. The agreements is found to be good, as shown in the grafs. It is found that the increase of number of fins leads and length of fin to suppressing convective currents and increase the heat transfer and solidification rates. The thickness and fin material are found to have very little effect on the heat transfer and solidification rates. In the mean time the ratio of diameters of the inner and the outer tubes is found to increase the heat transfer and solidification rates.

  17. Carbon-foam finned tubes in air-water heat exchangers

    Energy Technology Data Exchange (ETDEWEB)

    Yu Qijun [Department of Mechanical and Materials Engineering, University of Western Ontario, London, ON, N6A 5B8 (Canada)]. E-mail: qyu4@eng.uwo.ca; Straatman, Anthony G. [Department of Mechanical and Materials Engineering, University of Western Ontario, London, ON, N6A 5B8 (Canada)]. E-mail: astraatman@eng.uwo.ca; Thompson, Brian E. [Department of Mechanical Engineering, University of Ottawa, Ottawa, ON, K1N 6N5 (Canada)]. E-mail: thompson@eng.uottawa.ca

    2006-02-01

    An engineering model is formulated to account for the effects of porosity and pore diameter on the hydrodynamic and thermal performance of a carbon-foam finned tube heat exchanger. The hydrodynamic and thermal resistances are obtained from well-established correlations that are extended herein to account for the influence of the porous carbon foam. The influence of the foam is characterized on the basis of a unit-cube geometric model that describes the internal structure, the exposed surface, the permeability and the effective conductivity as a function of porosity and pore diameter. The engineering model is validated by comparison with experiments that characterize heat transfer in an air-water radiator made from porous carbon foam. The model is also used in to conduct a parametric study to show the influence of the porosity and pore diameter of the foam. The parametric study suggests that in comparison to conventional aluminum finned-tube radiators, improvements of approximately 15% in thermal performance are possible without changing the frontal area, or the air flow rate and pressure drop. The engineering model developed herein can be used by engineers to assess quantitatively the suitability of porous carbon foam as a fin material in the design of air-water heat exchangers.

  18. Carbon-foam finned tubes in air-water heat exchangers

    Energy Technology Data Exchange (ETDEWEB)

    Yu, Qijun; Straatman, Anthony G. [Department of Mechanical and Materials Engineering, The University of Western Ontario, London, ON (Canada); Thompson, Brian E. [Department of Mechanical Engineering, The University of Ottawa, Ottawa, ON (Canada)

    2006-02-01

    An engineering model is formulated to account for the effects of porosity and pore diameter on the hydrodynamic and thermal performance of a carbon-foam finned tube heat exchanger. The hydrodynamic and thermal resistances are obtained from well-established correlations that are extended herein to account for the influence of the porous carbon foam. The influence of the foam is characterized on the basis of a unit-cube geometric model that describes the internal structure, the exposed surface, the permeability and the effective conductivity as a function of porosity and pore diameter. The engineering model is validated by comparison with experiments that characterize heat transfer in an air-water radiator made from porous carbon foam. The model is also used in to conduct a parametric study to show the influence of the porosity and pore diameter of the foam. The parametric study suggests that in comparison to conventional aluminum finned-tube radiators, improvements of approximately 15% in thermal performance are possible without changing the frontal area, or the air flow rate and pressure drop. The engineering model developed herein can be used by engineers to assess quantitatively the suitability of porous carbon foam as a fin material in the design of air-water heat exchangers. (author)

  19. Experimental study and modelling of heat transfer during condensation of pure fluid and binary mixture on a bundle of horizontal finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Belghazi, M.; Marvillet, C. [Commissariat a l' Energie Atomique, Grenoble (France). Groupement pour la Recherche sur les Echangeurs thermiques; Bontemps, A. [Universite Joseph Fourier, Grenoble (France). LEGI/GRETh

    2003-03-01

    An experimental investigation was conducted to measure the local heat transfer coefficient for each row in a trapezoidal finned horizontal tube bundle during condensation of both pure fluid (HFC 134a) and several compositions of the non-azeotropic binary mixture HFC 23/HFC 134a. The test section is a 13x3 (rows x columns) tube bundle and the heat transfer coefficient is measured using the modified Wilson plot method. The inlet vapour temperature is fixed at 40{sup o}C and the water flow rate in each active row ranges from 170 to 600 l/h. The test series cover five different finned tubes all commercially available, K11 (11 fins/inch), K19 (19 fins/inch), K26 (26 fins/inch), K32 (32 fins/inch), K40 (40 fins/inch) and their performances were compared. The experimental results were checked against available models predicting the heat transfer coefficient during condensation of pure fluids on banks of finned tubes. Modelling of heat exchange during condensation of binary mixtures on bundles of finned tubes based on the curve condensation model is presented. (author)

  20. Analysis of radiative heat transfer impact in cross-flow tube and fin heat exchangers

    Directory of Open Access Journals (Sweden)

    Hanuszkiewicz-Drapała Małgorzata

    2016-03-01

    Full Text Available A cross-flow, tube and fin heat exchanger of the water – air type is the subject of the analysis. The analysis had experimental and computational form and was aimed for evaluation of radiative heat transfer impact on the heat exchanger performance. The main element of the test facility was an enlarged recurrent segment of the heat exchanger under consideration. The main results of measurements are heat transfer rates, as well as temperature distributions on the surface of the first fin obtained by using the infrared camera. The experimental results have been next compared to computational ones coming from a numerical model of the test station. The model has been elaborated using computational fluid dynamics software. The computations have been accomplished for two cases: without radiative heat transfer and taking this phenomenon into account. Evaluation of the radiative heat transfer impact in considered system has been done by comparing all the received results.

  1. Analysis of radiative heat transfer impact in cross-flow tube and fin heat exchangers

    Science.gov (United States)

    Hanuszkiewicz-Drapała, Małgorzata; Bury, Tomasz; Widziewicz, Katarzyna

    2016-03-01

    A cross-flow, tube and fin heat exchanger of the water - air type is the subject of the analysis. The analysis had experimental and computational form and was aimed for evaluation of radiative heat transfer impact on the heat exchanger performance. The main element of the test facility was an enlarged recurrent segment of the heat exchanger under consideration. The main results of measurements are heat transfer rates, as well as temperature distributions on the surface of the first fin obtained by using the infrared camera. The experimental results have been next compared to computational ones coming from a numerical model of the test station. The model has been elaborated using computational fluid dynamics software. The computations have been accomplished for two cases: without radiative heat transfer and taking this phenomenon into account. Evaluation of the radiative heat transfer impact in considered system has been done by comparing all the received results.

  2. Heat transfer characteristics in micro-fin tube equipped with double twisted tapes: Effect of twisted tape and micro-fin tube arrangements

    Institute of Scientific and Technical Information of China (English)

    EIAMSA-ARD S.; WONGCHAREE K.

    2013-01-01

    An experimental study was carried out to investigate the influence of double twisted-tape inserts (DTs) in micro-fin tubes (MFs) on heat transfer,friction factor and thermal performance factor characteristics of the compound devices in the following configurations:(1) twisted tapes acted in the same direction (for co-swirl) while MF and twisted tapes acted in the same (parallel) direction (MF-CoDTs:P),(2) twisted tapes acted in the same direction (for co-swirl) while micro-fin tube and twisted tapes acted in opposite directions (MF-CoDTs:O) and (3) twisted tapes acted in opposite directions for counter swirl (MF-CDTs).The MF alone and the MF equipped with a single twisted tape in parallel/opposite arrangement were also considered for comparison.The experiments were conducted for the flows with the Reynolds numbers between 5 650 and 17 000,under uniform heat flux condition.The experimental results indicate that MF-CDTs induce stronger swirl/turbulence flow,resulting in higher heat transfer rate,friction factor and thermal performance factor than other combined devices.The thermal performance factors associated with the use of MF-CDTs were found to be higher than those associated with the uses of MF-CoDTs:P,MF-CoDTs:O and MF alone up to 9.3%,6.5% and 56.4%,respectively.The empirical correlations developed using the present experimental data for the Nusselt number,friction factor and thermal performance factor are also reported.

  3. Studi Analitik dan Numerik Perpindahan Panas pada Fin Trapesium (Studi Kasus pada Finned Tube Heat Exchanger

    Directory of Open Access Journals (Sweden)

    Ahmad Zaini

    2013-09-01

    Full Text Available Penambahan fin pada pipa penukar kalor merupakan suatu upaya memperbesar perpindahan kalor konduksi dan konveksi, dengan cara memperluas bidang geometri. Pada penelitian ini dianalisa secara analitik dan numerik perpindahan kalor pada fin dengan profil longitudinal tidak seragam atau berubah terhadap jarak dari dasar fin, dengan memvariasikan ketebalan ujung fin. Hasil dari kedua studi ini tidak jauh berbeda, pada keduanya menjelaskan bahwa fin dengan ketebalan ujung 0,9 mm (fin trapesium terbalik paling baik dari 5 variasi lainnya; serta perubahan temperatur paling besar terjadi pada sepertiga pertama dari panjang  fin, ini artinya pelepasan kalor terbesar terjadi pada daerah tersebut. Perbedaannya adalah pada persentase penurunan temperatur sepanjang  fin terhadap temperatur dasar fin, untuk ketebalan 0,9 mm pada studi analitik sebesar 91,92% dan pada studi numerik sebesar 91,78%. Hal ini berarti metode penyelesaian persamaan diferensial orde 2 dengan koefisien variabel dengan cara pembedahan koefisien variabel pada ODE, sudah benar dan valid. Namun bila ditinjau dari waktu yang diperlukan untuk komputasinya, studi analitik membutuhkan waktu lebih lama. Waktu yang diperlukan dalam komputasinya tergantung dari fungsi koefisien variabel.

  4. Experimental and parametric studies of a louvered fin and flat tube compact heat exchanger using computational fluid dynamics

    Directory of Open Access Journals (Sweden)

    P. Karthik

    2015-12-01

    Full Text Available The present study aimed to perform the parametric analysis on thermo-hydraulic performance of a compact heat exchanger using computational fluid dynamics (CFD. The analysis has been carried out at different frontal air velocities by varying the geometrical parameters such as fin pitch, transverse tube pitch, longitudinal tube pitch, louver pitch and louver angle. The air side performance of the heat exchanger has been evaluated by calculating Colburn factor (j and Fanning friction factor (f. The comparison of CFD results with the experimental data exhibited a good agreement and the influence of various geometrical parameters for the selected range of values on the pressure drop, heat transfer coefficient and goodness factor was analyzed. The results obtained from the analysis will be very useful to optimize the louvered fin and flat tube compact heat exchanger for better thermo-hydraulic performance analysis without the need of time consuming and expensive experimentation.

  5. Computation of the Nusselt number asymptotes for laminar forced convection flows in internally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Ledezma, G.A. [Duke Univ., Durham, NC (United States). Mechanical Engineering Dept.; Campo, A. [Idaho State Univ., Pocatello, ID (United States). Coll. of Engineering

    1999-04-01

    The utilization of internal longitudinal finned tubes has received unparallel attention in the heat transfer literature over the years as a result of its imminent application in high performance compact heat exchangers to enhance the heat transfer between laminar streams of viscous fluids and tube walls. Here, the central goal of this paper is to report a simple approximate way for the prediction of the two asymptotes for the local Nusselt number in laminar forced convection flows inside internal longitudinal finned tubes. The computational attributes of the Method Of Lines (MOL) are propitious for the determination of asymptotic temperature solutions and corresponding heat transfer rates (one for Z {r_arrow} 0 and the other for z {r_arrow} {infinity}). The two local Nusselt number sub-distributions, namely Nu{sub z{r_arrow}0} and Nu{sub z{r_arrow}{infinity}}, blend themselves into an approximate Nusselt number distribution that covers the entire z-domain in a natural way.

  6. Fluid flow and heat transfer of a power-law fluid in an internally finned tube with different fin lengths

    Science.gov (United States)

    Grabski, Jakub Krzysztof; Kołodziej, Jan Adam

    2016-06-01

    In the paper an analysis of fluid flow and heat transfer of a power-law fluid in an internally finned tube with different fin length is conducted. Nonlinear momentum equation of a power-law fluid flow and nonlinear energy equation are solved using the Picard iteration method. Then on each iteration step the solution of inhomogeneous equation consists of two parts: the general solution and the particular solution. Firstly the particular solution is obtained by interpolation of the inhomogeneous term by means of the radial basis functions and monomials. Then the general solution is obtained using the method of fundamental solutions and by fulfilling boundary conditions.

  7. Studi Eksperimen Analisa Performa Compact Heat Exchanger Louvered Fin Flat Tube untuk pemanfaatan Waste Energy

    OpenAIRE

    Taqwim Ismail; Ary Bachtiar Khrisna Putra

    2014-01-01

    Waste Heat Recovery merupakan instalasi yang digunakan untuk memanfaatkan kembali waste energy seperti exhaust gas. Penelitian dilakukan pada compact heat exchanger tipe louvered fin flat tube sebagai salah satu komponen penyusun waste heat recovery system. Eksperimen dilakukan dengan mendesain compact heat exchanger tipe louvered fin flat tube kemudian dilakukan pengujian pada compact heat exchanger yang telah didesain. Pengujian dilakukan dengan memberikan tiga variasi kecepatan putaran fan...

  8. An effectiveness-NTU technique for characterising a finned tubes PCM system using a CFD model

    OpenAIRE

    Tay, N. H. Steven; Belusko, M.; Castell, Albert; Cabeza, Luisa F.; Bruno, F.

    2014-01-01

    Numerical modelling is commonly used to design, analyse and optimise tube-in-tank phase change thermal energy storage systems with fins. A new simplified two dimensional mathematical model, based on the effectiveness-number of transfer units technique, has been developed to characterise tube-in-tank phase change material systems, with radial round fins. The model applies an empirically derived P factor which defines the proportion of the heat flow which is parallel and isothermal....

  9. Prediction of fluid flow and heat transfer in internally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Al-Hashem, M.Y.

    1993-01-01

    Fully developed fluid flow and heat transfer characteristics in internally finned tubes were investigated. Both laminar and turbulent flows were considered. Longitudinal fins of trapezoidal profile integrally attached to the tube wall are equally spaced circumferentially in the tube. The assumption of axially constant heat flux per unit length was applied. The tube wall temperature was assumed to be circumferentially uniform at any cross section but varies axially with the change of the bulk temperature. With a fin of finite conductivity, the temperature varies along the fin height. The influence of the ratio of the fin to fluid thermal conductivity ratio, K[sub fin]/K[sub fluid], was investigated for both laminar and turbulent flows. Results for laminar flow case were presented for a fin height to tube radius ratio H/R, ranging from 0.2 to 0.9; the number of fins, NFIN, was varied from 6 to 30; and fin half angles, beta, were varied from 1.5 to 3 degrees. It was found that for any specified geometry the Nusselt number is influenced by a single parameter, K[sub fin]/K[sub fluid]. A mixing length model developed by Ivanovic and Patankar was used to predict the results for turbulent fluid flow. Results were presented for a range of fin height to tube radius, H/R, which was varied from 0.2 to 0.4; NFIN ranged from 6 to 22; beta was selected as 1.5 and 3 degrees; and Reynolds number, Re, varied from 10,000 to 100,000. Predicted results for isothermal fins were shown to be in agreement with other researchers. The results provide extensive information on the influence of the fin to fluid thermal conductivities ratio. It is evident from the results that the assumption of isothermal fins is an inaccurate one, especially at high Reynolds number and either high H/R or low K[sub fin]/K[sub fluid] ratio.

  10. Large-eddy simulation of turbulent flows around a fin-tube heat exchanger enclosed by a compartment

    Science.gov (United States)

    Son, Changkeun; Song, Simon; Lee, Jeesoo; Kang, Seongwon

    2014-11-01

    The main objective of the present study is to analyze heat transfer and flow characteristics of a heat exchanger in an industrial application using high-fidelity simulation techniques. Large-eddy simulations (LES) were performed to investigate the turbulent flows around a fin-tube heat exchanger enclosed by a compartment. The complex geometry of the compartment poses a difficulty in a simulation as the local Re number is about two orders of different magnitude, and generates various scales of the 3-D vortices and complex flow patterns. Careful tests with both grid resolution and turbulent inflow boundary condition were performed in order to compare our results to the measured data from a MRV experiment as well as the results from RANS simulations. From interaction of the flow structures such as the 3-D vortices, a few interesting flow phenomena were observed which are different from a plain fin-tube heat exchanger, such as helical flows and a jet stream observed behind the fin-tube region. Also, performance of the heat exchanger was analyzed using the data from plain fin-tube heat exchangers. Based on this analysis, a numerical technique for heat exchanger was devised and tested to show a possibility of reducing the computational cost significantly, using a porous media model.

  11. Experimental analysis of ammonia condensation on smooth and integral-fin titanium tubes

    Energy Technology Data Exchange (ETDEWEB)

    Fernandez-Seara, Jose; Uhia, Francisco J.; Diz, Ruben [Area de Maquinas y Motores Termicos, E.T.S. de Ingenieros Industriales, University of Vigo, Campus Lagoas-Marcosende No 9, 36310 Vigo (Spain)

    2009-09-15

    This paper reports on the experimental research conducted to study the condensation of ammonia on smooth and integral-fin (32 fpi) titanium tubes of 19.05 mm outer diameter. Experiments were carried out at saturation temperatures of 30, 35, 40 and 45 C and wall subcoolings from 1 to 8 C. The results show that the condensation coefficients on the smooth tubes are well predicted by the Nusselt theory with an average error of +0.66% and within a deviation between -6.6% and +8.3%. The enhancement factors provided by the integral-fin tubes range from 0.77 to 1.22. The low enhancement factors are due to the high condensate retention between fins, which brings about flooded fractions of the tube perimeter from 62.9% to 73.2%, and the low thermal conductivity of titanium. The Briggs and Rose [1994. Effect of fin efficiency on a model for condensation heat transfer on a horizontal, integral-fin tube. Int. J. Heat Mass Transfer 37, 457-463.] model, which accounts for the conduction in the fins, predicts the experimental data with a mean overestimation of 20%. The analysis of the partial thermal resistances in the overall heat transfer process points out the convenience of enhancing the outside ammonia condensation when high water velocities are considered inside the tubes. (author)

  12. Theoretical model of film condensation in a bundle of horizontal low finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Honda, Hiroshi; Nozu, Shigeru; Takeda, Yasuhito

    1988-08-25

    A method for calculating flow behavior in a group of tubes was developed by modifying the calculation method for single tubes considering the flow characteristics of a condensate which flows down a series of vertical tubes with horizontal low fins, and the results of calculation by this method was compared with experimental values. The predicted value of the heat transfer coefficient obtained by calculation agreed well with values obtained by experiments with R12 and acetone. The theoretical values of n-butane and steam also agreed well with experimental values. According to the results of calculation given a practical condition, the heat transfer coefficient greatly depends on the fin spacing for R12 characterized by a low surface tension and a low condensation latent heat; also, it rapidly drops when the number of tubes exceeds a certain level if the fin spacing is narrow. The optimal fin spacing is about 0.3mm if the number of tubes is 2 to 15. For steam, the heat transfer coefficient increasing effect is considerably lower than for R12; the heat transfer coefficient does not vary so much with the fin spacing or the number of tubes; the optimal fin spacing is about 1.3mm. (6 figs, 11 refs)

  13. Heat transfer correlation for high-finned tubes in staggered arrangement; High fin tube chidori hairetsu no netsudentatsuritsu seirishiki ni tsuite

    Energy Technology Data Exchange (ETDEWEB)

    Hashizume, K. [Hiroshima Institute of Technology, Hiroshima (Japan)

    1995-07-25

    Existing correlations are reviewed for heat transfer of high-finned tubes in staggered arrangement, and compared with published experimental data. These data include those using tubes for air-coolers (AC) and for heat recovery heat exchangers in the high-temperature region (HRHX). Comparisons showed that none of the correlations can predict experimental data for both AC and for HRHX. Therefore, a new correlation is proposed which can predict almost all data within 10%. 5 refs., 6 figs., 3 tabs.

  14. Heat Transfer Characteristics of Laminar Flow in Internally Finned Tubes under Various Boundary Conditions

    Institute of Scientific and Technical Information of China (English)

    Ze-NingWang; Qiang-TaiZhou

    1994-01-01

    Numerical solutions for fully developed laminar flow in internally finned tubes with trapezoidal and triangular fin profiles were given with Finite Elemant Method(FEM):The heat transfer charactieristics were obtained and compared under the boundary conditions of uniform heat flux,univform wall tepmerature,and the third boundary condition with finite wall thermal conductivity considered.The numerical results show that boundary conditions have pronounced effects on the temperature field.Furthermore,a new mechanism on the heat transfer augmentation of internally finned tubes is proposed.

  15. A Study on Solidification and Melting of Water around Spine-fin Tube

    Science.gov (United States)

    Hirasawa, Yoshio; Takegoshi, Eisyun; Konya, Hiroshi; Tajima, Ikuo

    The authors have studied the phase change process of composite materials containing conductive solids in order to improve the heat transfer characteristics of phase change materials. In this study, experiments for the solidification and melting of water around a spine-fin tube are carried out, and the phase change volume and temperature distribution in the water are measured. As a result, the solidification and melting process are promoted considerably by the heat conduction of the fin and the natural convection in the lower side of the spine-fin tube for the melting process.

  16. Experimental Study on Frost Height of Round Plate Fin-Tube Heat Exchangers for Mobile Heat Pumps

    Directory of Open Access Journals (Sweden)

    Dong-Yeon Lee

    2012-09-01

    Full Text Available The objective of this study was to provide experimental data that could be used to predict frost growth and frost performance of a round plate fin-tube heat exchanger for low temperature heat pumps used in zero emission vehicles under cold weather conditions. In this study, round plate fin-tube heat exchangers were tested with variation of the fin space, air flow rate, relative humidity, and inlet air temperature. Frost height was measured and considered with the boundary layer interruption between fins. Frost height for 8.0 mm of fin space was increased by approximately 91.9% with an increase of relative humidity from 50.0% to 80.0%. The growth rate of frost height at 1.2 m3/min was observed to be 13.0% greater than that at 0.8 m3/min. Finally, the variation of the blockage ratio with fin space would be an important reference for designing advanced heat exchangers that operate under cold weather conditions.

  17. Determination of local heat transfer coefficient on the surface of longitudinally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Sobota, T.; Taler, J. [Cracow Univ. of Technology (Poland). Inst. of Process and Power Engineering

    2008-06-15

    The distribution of the heat transfer coefficient is calculated from temperature measurements at interior points of the solid, and the measured fluid temperature. The unknown parameters associated with the solution were selected to achieve the closest least squares agreement between the computed and measured temperatures using the Levenberg-Marquardt method. The nonlinear least - squares problem is parameterised by assuming the stair-case changes of the heat transfer coefficient on the boundary, or by expressing the space variations of the heat transfer coefficient in its functional form. The determination of the circumferential heat transfer coefficient distribution on the heated tube with two longitudinal fins in cross flow demonstrates the accuracy of the developed method. The actual experimental data were used. Experiments were performed with an array of vertical tubes arranged in staggered pattern. (orig.)

  18. Forced circulation air coolers with internally finned tubes; Ventilator-Luftkuehler mit innenberippten Rohren

    Energy Technology Data Exchange (ETDEWEB)

    Arnemann, M. [Forschungszentrum fuer Kaelte- und Umwelttechnik GmbH (FKU), Berlin (Germany)

    1998-04-01

    Tubes with internal fins have a much higher heat transfer during evaporation as compared with unfinned tubes. The findings served as a basis for the new development of the ``FHV high-performance forced circulation air cooler`` by Walter Roller GmbH and Co. The new evaporator type was designed on the basis of DIN 8955 and ENV 328 for evaporation temperatures of 0 C to -31 C. (orig.) [Deutsch] Im Vergleich zu glatten Rohren laesst sich durch den Einsatz von innenberippten Rohren der innere Waermeuebergang bei der Verdampfung nachweislich deutlich verbessern. Die Ergebnisse bildeten die Grundlage fuer die Neuentwicklung `FHV Hochleistungs-Luftkuehler` im Hause Walter Roller GmbH and Co. Die energetische Bewertung des neuen Verdampfertyps erfolgte in Anlehnung an die Normen DIN 8955 bzw. ENV 328 fuer Verdampfungstemperaturen zwischen 0 C und -31 C. (orig.)

  19. Evaluation of High Temperature Corrosion Resistance of Finned Tubes Made of Austenitic Steel And Nickel Alloys

    Directory of Open Access Journals (Sweden)

    Turowska A.

    2016-06-01

    Full Text Available The purpose of the paper was to evaluate the resistance to high temperature corrosion of laser welded joints of finned tubes made of austenitic steel (304,304H and nickel alloys (Inconel 600, Inconel 625. The scope of the paper covered the performance of corrosion resistance tests in the atmosphere of simulated exhaust gases of the following chemical composition: 0.2% HCl, 0.08% SO2, 9.0% O2 and N2 in the temperature of 800°C for 1000 hours. One found out that both tubes made of austenitic steel and those made of nickel alloy displayed good resistance to corrosion and could be applied in the energy industry.

  20. Parametric study on the performance of a heat exchanger with corrugated louvered fins

    Energy Technology Data Exchange (ETDEWEB)

    Qi, Zhao-gang; Chen, Jiang-ping; Chen, Zhi-jiu [Institute of Refrigeration and Cryogenics, Shanghai Jiao Tong University, No. 1954, Huashan Rd., Shanghai 200030 (China)

    2007-02-15

    The Taguchi method is a well-known parametric study tool in engineering quality and experimental design. This study analyzes five experimental factors (flow depth, ratio of fin pitch and fin thickness, tube pitch, number of louvers and angle of louver) affecting the heat transfer and pressure drop of a heat exchanger with corrugated louvered fins using the Taguchi method. Fifteen samples are selected from experimental database and the heat transfer and flow friction characteristics are analyzed. The results show that flow depth, ratio of fin pitch and fin thickness and the number of the louvers are the main factors that influence significantly the thermal hydraulic performance of the heat exchanger with corrugated louvered fins. Therefore, these three factors are considered as the main factors for an optimum design of a heat exchanger. (author)

  1. A method for numerically simulating the thermal state of a tube with punched helical-tape finning

    Science.gov (United States)

    Galushchak, I. V.; Gorbatenko, V. Ya.; Shevelev, A. A.

    2011-05-01

    A method for numerically simulating the thermal state of a tube with punched helical-tape finning and heat transfer from heating to heated medium through the finned tube is presented. Results of calculations carried out for one version of finning geometry under the conditions of heating nonboiling water by flue gases are given.

  2. Heat transfer and pressure drop performance of a finned-tube heat exchanger proposed for use in the NASA Lewis Altitude Wind Tunnel

    Science.gov (United States)

    Vanfossen, G. J.

    1985-01-01

    A segment of the heat exchanger proposed for use in the NASA Lewis Altitude Wind Tunnel (AWT) facility has been tested under dry and icing conditions. The heat exchanger has the largest pressure drop of any component in the AWT loop. It is therefore critical that its performance be known at all conditions before the final design of the AWT is complete. The heat exchanger segment is tested in the NASA Lewis Icing Research Tunnel (IRT) in order to provide an icing cloud environment similar to what will be encountered in the AWT. Dry heat transfer and pressure drop data are obtained and compared to correlations available in the literature. The effects of icing sprays on heat transfer and pressure drop are also investigated.

  3. Enhancement of heat transfer in condensation of refrigerant vapor on horizontal finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Ivanov, O.P.; Khizhnyakov, S.V. (Northwestern Polytechnic Inst. (SU))

    1991-01-01

    This paper reports on the technique for predicting the heat transfer coefficients in film condensation of Freons on horizontal tubes with different fin geometries that has been improved. The suggested technique allows for the spatial orientation of the different parts of the heat transfer area, the capillary contraction of condensate, and its holdup on the bottom zone of the horizontal tube.

  4. Effective Heat Transfer Enhancement in Finned Tube Heat Exchanger with Different Fin Profiles

    OpenAIRE

    2013-01-01

    During cross flow in a heat exchanger, heat transfer in the front portion of the tube is more compared to back portion of the tube. This is due to less formation of vortices at the backside of the tube. For uniform heat transfer to take place throughout the tube, it is necessary to increase the vortex formation at the rear side of the tube. The aim of this study is to explore the possibilities of improving the flow structure and thereby increasing uniform heat transfer...

  5. Filmwise Condensation on Low Integral-Fin Tubes of Different Diameter

    Science.gov (United States)

    1988-12-01

    41 5.1 SUMMARY OF SIEDER -TATE COEFFICIENTS ......................... 60 5.2 SUMMARY OF R- 113...smooth tube (m 2 ) Ci Sieder -Tate-type coefficient Cp specific heat at constant pressure (J/kg K) Df fin diameter (m) Dr root diameter (m) e fin height (m...coefficients be known. During this study, 46 Sieder -Tate -type and Nusselt-type equations were used to represent the inside and outside, respectively. ko.14

  6. Finned tube heat exchangers. (Latest citations from the EI Compendex*plus database). Published Search

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1996-04-01

    The bibliography contains citations concerning theoretical studies and applications of finned tubing in a variety of heat exchanger design configurations. The effects of turbulent and laminar flow are presented in terms of heat transfer for both external and internal finned surfaces. Energy conservation and waste heat recovery systems are featured and the use of refrigerants is also included. (Contains 50-250 citations and includes a subject term index and title list.) (Copyright NERAC, Inc. 1995)

  7. Experimental Investigation of Phase Change inside a Finned-Tube Heat Exchanger

    Directory of Open Access Journals (Sweden)

    M. Rahimi

    2014-01-01

    Full Text Available An experimental study is conducted in order to investigate melting and solidification processes of paraffin RT35 as phase change materials in a finned-tube. Therefore the effect of using fins in this study as well as some operational parameters is considered. The motivation of this study is to design and construct a novel storage unit and to compare it with a finless heat exchanger. A series of experiments are conducted to investigate the effect of increasing the inlet temperature and flow rate on the charging and discharging processes of the phase change material. It is shown that, using fins in phase change process enhances melting and solidification procedures. The trend of this variation is different for the heat exchangers; increasing the inlet temperature for the bare tube heat exchanger more effectively lowers melting time. Similarly, flow rate variation varies the solidification time more intensely for the bare tube heat exchanger.

  8. Studi Eksperimen Analisa Performa Compact Heat Exchanger Louvered Fin Flat Tube untuk pemanfaatan Waste Energy

    Directory of Open Access Journals (Sweden)

    Taqwim Ismail

    2014-03-01

    Full Text Available Waste Heat Recovery merupakan instalasi yang digunakan untuk memanfaatkan kembali waste energy seperti exhaust gas. Penelitian dilakukan pada compact heat exchanger tipe louvered fin flat tube sebagai salah satu komponen penyusun waste heat recovery system. Eksperimen dilakukan dengan mendesain compact heat exchanger tipe louvered fin flat tube kemudian dilakukan pengujian pada compact heat exchanger yang telah didesain. Pengujian dilakukan dengan memberikan tiga variasi kecepatan putaran fan sisi exhaust gas, yaitu 0.2, 0.3, dan 0.4 m/s untuk mengetahui unjuk kerja yang berbeda dari compact heat exchanger yang telah didesain.  Hasil yang didapatkan dari studi eksperimen ini adalah dimensi dari compact heat exchanger tipe louvered fin flat tube dan beberapa parameter yang menunjukkan unjuk kerja dari compact heat exchanger seperti nilai heat transfer baik dari sisi air maupun sisi exhaust gas, effectiveness, number of transfer unit (NTU, overall heat transfer coefficient, dan  ΔTLMTD dari compact heat exchanger.

  9. High-frequency welded finned tubes - finning of 9% chromium steel X10CrMoVNb91 (P91/T91)

    Energy Technology Data Exchange (ETDEWEB)

    Coussement, C.J. [Belgian Welding Inst., Gent (Belgium); Bruehl, F.H. [Mannesmann Carnoy N.V., Gent (Belgium); Donckt, E. van der [Mannesmann Carnoy N.V., Gent (Belgium)

    1995-07-01

    During the past two years, a research programme was set up to investigate the feasibility of producing, in an economical way, finned tubes in modified 9% chromium steel, by using the high frequency resistance welding (finning) process and to evaluate their properties and product reliability for the intended high temeprature application area, at temepratures above 530 C. The basic aim was to produce T91/P91 finned tubes and to demonstrate their applicability in the `as-welded` condition. Therefore, the influence of omitting any post weld heat treatment on the short and longer term behaviour was evaluated. The programm was performed by Mannesmann-Carnoy and realised in collaboration with the Research Centre of the Belgian Welding Institute, with support of the Minister of Economic Affairs of the Flemish Region. (orig.) [Deutsch] In den letzten zwei Jahren wurde ein Untersuchungsprogramm durchgefuehrt, in dem die Moeglichkeit einer wirtschaftlichen Herstellung von Rippenrohren aus 9%igem modifizierten Chromstahl untersucht wurde durch Anwendung des Hochfrequenz-Widerstandsschweissprozesses. Die Eigenschaften und die Zuverlaessigkeit des Produktes fuer die Anwendung im Hochtemperaturbereich (ueber 530 C) wird beurteilt. Es kamen T91/P91-Rippenrohre zum Einsatz, um ihre Verwendbarkeit im nicht waermebehandelten Zustand zu zeigen. Insbesondere wurde ueberprueft, welchen Einfluss der nicht waermebehandelten Zustand nach dem Schweissen auf das Kurz- und Langzeitverhalten der Rippenrohre hat. Das Programm wurde von Mannesmann Carnoy in Zusammenarbeit mit dem Untersuchungszentrum des belgischen Schweissinstitutes, und mit Unterstuetzung durch das Wirtschaftsministerium der flaemischen Regierung durchgefuehrt. (orig.)

  10. RESULTS OF INVESTIGATIONS ON THERMAL CHARACTERISTICS OF AIR HEATER BUNDLE MADE OF BIMETALLIC FINNED TUBES

    Directory of Open Access Journals (Sweden)

    V. B. Kuntysh

    2014-01-01

    Full Text Available The paper presents a scheme and description of a new aerodynamic stand that has a 300x300 mm cross-section operating channel. The stand is used for studying thermal and aerodynamic characteristics of bundles made of finned tubes of actual dimensions in crossflow. The paper provides results of an exploratory test pertaining to heat transfer and resistance of four row staggered bundle made of tubes with aluminium spiral fins having outside diameter of 26 mm which are used in the systems of ventilation, air-conditioning and heating of buildings and also in transport heat exchangers.

  11. Indirect Measurement of Local Condensing Heat-Transfer Coefficient Around Horizontal Finned Tubes

    Science.gov (United States)

    1987-09-01

    5.9 Effect of Tube Insulation on Sieder -Tate-Type Coefficient (C ) and Modified Coefficient (C.) for All Tubes •t Atmospheric Pressure...specific tube C Sleder-Tate-type coefficient in eqn. (4.2) C Modified Sieder -Tate-type coefficient in eqn. (5.2) D Tube diameter (m) D Equivalent diameter...an outside diameter equal to the fin root diameter). The Inside heat-transfer coefficent is given by a Sieder -Tate-type equation (4.2) and is

  12. Heat transfer characteristics of a new helically coiled crimped spiral finned tube heat exchanger

    Science.gov (United States)

    Srisawad, Kwanchanok; Wongwises, Somchai

    2009-02-01

    In the present study, the heat transfer characteristics in dry surface conditions of a new type of heat exchanger, namely a helically coiled finned tube heat exchanger, is experimentally investigated. The test section, which is a helically coiled fined tube heat exchanger, consists of a shell and a helical coil unit. The helical coil unit consists of four concentric helically coiled tubes of different diameters. Each tube is constructed by bending straight copper tube into a helical coil. Aluminium crimped spiral fins with thickness of 0.5 mm and outer diameter of 28.25 mm are placed around the tube. The edge of fin at the inner diameter is corrugated. Ambient air is used as a working fluid in the shell side while hot water is used for the tube-side. The test runs are done at air mass flow rates ranging between 0.04 and 0.13 kg/s. The water mass flow rates are between 0.2 and 0.4 kg/s. The water temperatures are between 40 and 50°C. The effects of the inlet conditions of both working fluids flowing through the heat exchanger on the heat transfer coefficients are discussed. The air-side heat transfer coefficient presented in term of the Colburn J factor is proportional to inlet-water temperature and water mass flow rate. The heat exchanger effectiveness tends to increase with increasing water mass flow rate and also slightly increases with increasing inlet water temperature.

  13. Performance enhancement of fin attached ice-on-coil type thermal storage tank for different fin orientations using constrained and unconstrained simulations

    Science.gov (United States)

    Kim, M. H.; Duong, X. Q.; Chung, J. D.

    2017-03-01

    One of the drawbacks in latent thermal energy storage system is the slow charging and discharging time due to the low thermal conductivity of the phase change materials (PCM). This study numerically investigated the PCM melting process inside a finned tube to determine enhanced heat transfer performance. The influences of fin length and fin numbers were investigated. Also, two different fin orientations, a vertical and horizontal type, were examined, using two different simulation methods, constrained and unconstrained. The unconstrained simulation, which considers the density difference between the solid and liquid PCM showed approximately 40 % faster melting rate than that of constrained simulation. For a precise estimation of discharging performance, unconstrained simulation is essential. Thermal instability was found in the liquid layer below the solid PCM, which is contrary to the linear stability theory, due to the strong convection driven by heat flux from the coil wall. As the fin length increases, the area affected by the fin becomes larger, thus the discharging time becomes shorter. The discharging performance also increased as the fin number increased, but the enhancement of discharging performance by more than two fins was not discernible. The horizontal type shortened the complete melting time by approximately 10 % compared to the vertical type.

  14. Performance enhancement of fin attached ice-on-coil type thermal storage tank for different fin orientations using constrained and unconstrained simulations

    Science.gov (United States)

    Kim, M. H.; Duong, X. Q.; Chung, J. D.

    2016-07-01

    One of the drawbacks in latent thermal energy storage system is the slow charging and discharging time due to the low thermal conductivity of the phase change materials (PCM). This study numerically investigated the PCM melting process inside a finned tube to determine enhanced heat transfer performance. The influences of fin length and fin numbers were investigated. Also, two different fin orientations, a vertical and horizontal type, were examined, using two different simulation methods, constrained and unconstrained. The unconstrained simulation, which considers the density difference between the solid and liquid PCM showed approximately 40 % faster melting rate than that of constrained simulation. For a precise estimation of discharging performance, unconstrained simulation is essential. Thermal instability was found in the liquid layer below the solid PCM, which is contrary to the linear stability theory, due to the strong convection driven by heat flux from the coil wall. As the fin length increases, the area affected by the fin becomes larger, thus the discharging time becomes shorter. The discharging performance also increased as the fin number increased, but the enhancement of discharging performance by more than two fins was not discernible. The horizontal type shortened the complete melting time by approximately 10 % compared to the vertical type.

  15. Boiling heat transfer correlations for refrigerant mixtures flowing inside micro-fin tubes

    Institute of Scientific and Technical Information of China (English)

    Xiaoyan ZHANG; Xingqun ZHANG; Yunguang CHEN; Xiuling YUAN

    2008-01-01

    Based on experimental results of ternary non-azeotropic refrigerant mixture R417A flowing and boiling in one smooth and two internally grooved horizontal tubes with different geometrical parameters, a boiling heat transfer correlations was developed for refrigerant mix-tures flowing inside micro-fin tubes by applying the enhancement factor in the present modified-Kattan model which was modified by the experimental data of R417A in a smooth tube. The comparison between the calculation and the experimental results indicates that the prediction by the present correlations is in good agreement with the experiment of refrigerant mixtures inside different micro-fin tubes with a standard deviation of ± 30% for vapor qualities below 80%.

  16. Genetic algorithm optimization for finned channel performance

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    Compared to a smooth channel, a finned channel provides a higher heat transfer coefficient; increasing the fin height enhances the heat transfer. However, this heat transfer enhancement is associated with an increase in the pressure drop. This leads to an increased pumping power requirement so that one may seek an optimum design for such systems. The main goal of this paper is to define the exact location and size of fins in such a way that a minimal pressure drop coincides with an optimal heat transfer based on the genetic algorithm. Each fin arrangement is considered a solution to the problem(an individual for genetic algorithm). An initial population is generated randomly at the first step. Then the algorithm has been searched among these solutions and made new solutions iteratively by its functions to find an optimum design as reported in this article.

  17. Heat-transfer correlations for high-finned tubes in staggered arrangements

    Energy Technology Data Exchange (ETDEWEB)

    Hashizume, Kenichi [Hiroshima Inst. of Tech. (Japan). Dept. of Mechanical Engineering

    1995-12-31

    Existing correlations are reviewed for heat transfer of high-finned tubes in staggered arrangements and compared with published experimental data. These data include those using tubes for air-coolers (AC) and for heat-recovery heat exchangers in the high-temperature region (HRHX). Comparisons showed that none of the correlations can predict experimental data for both AC and for HRHX. Therefore a new correlation is proposed which can predict almost all data within 10 percent.

  18. Further studies in filmwise condensation of steam on horizontal finned tubes

    OpenAIRE

    Swensen, Keith Andrew

    1992-01-01

    Approved for public release; distribution is unlimited Over the years, there has been significant variation in the filmwise steam condensation data at NOS on horizontal low0integral finned tubes. With a view to increasing the accuracy of the data, inserts were used inside the tubes to reduce inside thermal resistance; however, significant discrepancies then occurred in the calculated outside coefficient when compared to data taken without an insert. These discrepancies arose due to the d...

  19. Effects of Working Fluid,Tubeside Enhancement and Bundle Depth on the Optimized Fin Geometry of a Horizontal Condenser Tube

    Institute of Scientific and Technical Information of China (English)

    H.Honda; T.Fukuda

    1992-01-01

    A theoretical study has been made to optimize the fin geometry of a horizontal finned tube which is to be used for condensers that handle the vapor load of a liquid phase change cooling module,Systematic numerical calculations of the vapor to coolant heat transfer coefficinet.Three dielctric fluids(R-113,FC-72,and FC-87) at atmospheric pressure were selected as the working fluids.For a single tube with optimized fin geometry,the average heat flux increased in the order of FC-87,R-113 and FC-72.Both the optimum fin height and optimum fin spacing incresaed with increasing vertical bundle depth.

  20. Natural convection and radiation heat transfer of an externally-finned tube vertically placed in a chamber

    Science.gov (United States)

    Qiu, Yan; Tian, Maocheng; Guo, Zhixiong

    2013-03-01

    A three-dimensional numerical study was made to investigate effects of fin angle, fin surface emissivity, and tube wall temperature on heat transfer enhancement for a longitudinal externally-finned tube placed vertically in a small chamber. The numerical model was first validated through comparison with experimental measurements and the appropriateness of general boundary conditions was examined. The numerical results show that the mean Nusselt number increases with Rayleigh number for all the fin angles investigated. The maximum heat transfer rate per mass occurs when the fin angle is about 60° for fin surface emissivity between 0.7 and 0.8 and 55° when the surface emissivity increases to 0.9. With increasing tube wall temperature, both the natural convection and radiation heat transfer are enhanced, but the fraction of radiation heat transfer decreases in the temperature range studied. Radiation fraction increases with increasing fin surface emissivity. Both convection and radiation heat transfer modes are important.

  1. Degradation of finned tubes heat exchangers in presence of non condensable gases and aerosols

    Energy Technology Data Exchange (ETDEWEB)

    Jose L Munoz-Cobo; Pena, J. [Universidad Politecnica de Valencia, Department of Chemical and Nuclear Engineering, Camino de Vera 14, Valencia 46022 (Spain); Luis E Herranz [CIEMAT, Departmen of Nuclear Fision, Avenida Complutense 22, Madrid 28040 (Spain)

    2005-07-01

    is formulated based on a diffusion layer modeling. Finally this paper presents a Monte Carlo method implemented in the Fortran code TAEROSOL that is able to compute the amount of aerosol mass that is deposited by impaction on the top of the finned tubes. The model results are compared with available experimental data of the CONGA European project. Finally we want to mention that Monte Carlo calculations and fluid flow calculations with the code TAEROSOL were performed to compute the amount of aerosols deposited on the top of the fins by impaction during the aerosol phase of Suckow et al. experiments. Also we compute the aerosol mass deposited by diffusiophoresis and settling. The calculations performed show that the mass deposited by settling is always smaller than 3 g in all the cases, and that impaction and diffusiophoresis mechanisms are the main deposition mechanisms for aerosols in CONGA experiments. (authors)

  2. Optimum parameters of transversely finned tubes in the case of simultaneous sooling by natural convection and radiations

    Energy Technology Data Exchange (ETDEWEB)

    Volodin, V.I.; Mikhalevich, A.A.; Nesterenko, V.B.

    1983-01-01

    The optimum parameters of minimum-weight finned tubes for the case of heat transfer by free convection and radiation are determined using the mathematical model with boundary conditions of the 3-type by the method of calculational experiment. The effects of the coolant and air temperatures diameter and thickness of the bimetallic wall, contamination and other factors on optimal finning parameters are investigated. It is obtained that for the case of heat transfer by free convection and radiation, the optimum finning parameters for the heat transfer surface of minimum-weight tubes by absolute value are larger than those of tube finning with forced convection.

  3. Compensation of flow maldistribution in fin-and-tube evaporators for residential air-conditioning

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Brix, Wiebke; Elmegaard, Brian;

    2011-01-01

    Compensation of flow maldistribution in multi-channel fin-and-tube evaporators for residential air-conditioning is investigated by numerical modeling. The considered sources of maldistribution are distribution of the liquid and vapor phases in the distributor and non-uniform airflow distribution...

  4. Comparison of fin-and-tube interlaced and face split evaporators with flow maldistribution and compensation

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Elmegaard, Brian; Larsen, Lars Finn Sloth

    2013-01-01

    Flow maldistribution in fin-and tube evaporators for residential air-conditioning is investigated by numerical simulation. In particular, the interlaced and the face split evaporator are compared in flow maldistribution conditions. The considered sources of maldistribution are the liquid...

  5. Analysis and design of a flat central finned-tube radiator

    Science.gov (United States)

    Auer, B. M.; Haller, H. C.; Krebs, R. P.

    1971-01-01

    Computer program based on fixed conductance parameter yields minimum weight design. Second program employs variable conductance parameter and variable ratio of fin length to tube outside radius, and is used for radiator designs with geometric limitations. Major outputs of the two programs are given.

  6. Comparative Study of Effect of Fin Arrangement on Propulsion Performance of Bio-inspired Underwater Vehicles with Multiple SMA Fins

    Directory of Open Access Journals (Sweden)

    Jian-hui He

    2015-09-01

    Full Text Available A biologically inspired underwater vehicle (BIUV was built using multiple lightweight bio inspired shape memory alloy (SMA fins. An unsteady 3D computational fluid dynamics (CFD method using an unstructured, grid-based, and unsteady Navier-Stokes solver with automatic adaptive re-meshing was adopted to compute unsteady flow. The hydrodynamics of multiple fins at a certain Reynolds number (Re = Uc/ν, where U is the upstream flow velocity, c is the chord length, and ν is the kinematic viscosity was studied and simulated using CFD to estimate hydrodynamic forces and characterize flow and vortex patterns created by the fins. Two common arrangements of multiple fins on the BIUV were considered: a posterior fin that is parallel to the anterior fins (case 1 and a posterior fin that is perpendicular to the anterior fins (case 2. First, the influence of the distance between two anterior undulating fins on the propulsion performance of both arrangements of multiple fins on the BIUV was investigated. The effect of the distance between the anterior undulating fins and the posterior oscillating fin was also analysed. The length of the posterior oscillating fin was varied and the fin surface area was held constant (24 mm2 to illustrate the influence of this parameter. Finally, the effect of frequency, amplitude, and wave number of anterior undulating fins on the non-dimensional drag coefficient of the posterior oscillating fin was investigated. Based on the flow structures, the reasons for the different performances of the BIUV are discussed. BIUV performances largely depend on the arrangements of multiple fins and the gap between the fins. Dimension and kinematic parameters also affect the performance of the BIUV. The results provide a physical insight into the understanding of fin interaction in fish or BIUVs that are propelled by multiple fins.

  7. Thermal behavior of crimped spiral fin tube bank under dehumidifying process: A case study of inline arrangement

    OpenAIRE

    2004-01-01

    Cross flow heat exchangers having crimped spiral fin and inline arrangement configurations under dehumidification are studied. The effect of tube diameter, fin spacing, fin height, transverse tube pitch are examined. From the experiment, it is found that the heat transfer and the frictional characteristics of the heat exchanger under dehumidification is close to that of the non-dehumidifying process. However, the air stream pressure drop and the heat transfer coefficient of the wet surface he...

  8. Mass- and heat transfer at water trickled finned tubes. Waerme- und Stoffaustausch an wasserberieselten Rippenrohren

    Energy Technology Data Exchange (ETDEWEB)

    Vilser, L.

    1982-11-22

    At five finned tubes of different geometries measurements were made of the heat and mass transfer during spraying with water and simultaneous passing of an air stream. Mass flow, air temperature, air moisture and air velocity were varied. From the results of the measurements the overall heat flux, the heat flux removed by the spray film, the heat flux transfered to the air by convection, the amount of evaporated water, the heat transfer coefficient between tube wall and spray film, the heat transfer coefficient between spray film and air stream, the mass transfer coefficient and the pressure drop in the air stream were calculated. The results are presented in diagrams, the heat transfer coefficient between spray film and air and the mass transfer coefficient are described by formulae. The comparison of the heat flux densities at the five different tubes shows that for the combination of dry cooling and spraying of the finned tubes, tubes with a small inner tube diameter and small height of the fins are most suited. The assumption frequently made, that the heat transfer coefficient between a gas flow and a spray film may be described by the mathematical interrelationships valid for the gas flow at a stationary wall is true only to a very limited extent. The same is valid for the determination of the pressure loss at the gas side. With a theoretical model it was tried to evaluate the phenomena at the finned tube by means of calculation. Starting from an overall concept described in the introduction formulations for solutions of partial problems were elaborated and results are presented. Because of the necessary simplifications a correlation with the results of the measurements was only achieved in subdomains. Possible starting points for improving the mathematical model are qualitatively described.

  9. Effects of winglets to augment tube wall heat transfer in louvered fin heat exchangers

    Energy Technology Data Exchange (ETDEWEB)

    Sanders, Paul A.; Thole, Karen A. [Virginia Tech, Blacksburg, VA (United States). Mechanical Engineering Department

    2006-10-15

    The louvered fin heat exchanger, a type of compact heat exchanger, has been used heavily in the automotive and air conditioning industries for the last several decades. The majority of past research, aimed towards improving louvered fin exchanger efficiency, has focused on optimizing various parameters of the louvered fin. The experimental study presented in this paper concentrates instead on augmenting the heat transfer along the tube wall of the compact heat exchanger through the use of winglets placed on the louvers. The experiments were completed on a 20 times scaled model of an idealized louvered fin exchanger with a fin pitch to louver pitch ratio of 0.76 and a louver angle of 27{sup o}. The Reynolds numbers tested, based on louver pitch, were between 230 and 1016. A number of geometrical winglet parameters, including angle of attack, aspect ratio, direction, and shape, were all evaluated based on heat transfer augmentation, friction factor augmentation, and efficiency index (combination of both augmentations). In an attempt to optimize these winglet parameters, tube wall heat transfer augmentations as high as 39% were achieved with associated friction factor augmentations as high as 23%. (author)

  10. Convective Boiling of Near-Azeotropic Refrigerant R410A in the Horizontal Micro-fin Tube

    Institute of Scientific and Technical Information of China (English)

    DUAN Xue-tao; MA Hu-gen; WU Zhi-min; WANG Fang

    2007-01-01

    Using near-azeotropic refrigerant R410A as the working fluid, the experimental studies on the horizontal micro-fin tubes were conducted. Several factors affecting heat transfer coefficients were analyzed, and the characteristics of flow boiling of the refrigerant in the horizontal micro-fin tubes were discussed. The local heat transfer coefficients increase with mass flux, heat flux and quality. And the heat transfer enhancement factor of those testing tubes is about 1.6 to 2.2.

  11. Heat Transfer Enhancement for Finned-Tube Heat Exchangers with Vortex Generators: Experimental and Numerical Results

    Energy Technology Data Exchange (ETDEWEB)

    O' Brien, James Edward; Sohal, Manohar Singh; Huff, George Albert

    2002-08-01

    A combined experimental and numerical investigation is under way to investigate heat transfer enhancement techniques that may be applicable to large-scale air-cooled condensers such as those used in geothermal power applications. The research is focused on whether air-side heat transfer can be improved through the use of finsurface vortex generators (winglets,) while maintaining low heat exchanger pressure drop. A transient heat transfer visualization and measurement technique has been employed in order to obtain detailed distributions of local heat transfer coefficients on model fin surfaces. Pressure drop measurements have also been acquired in a separate multiple-tube row apparatus. In addition, numerical modeling techniques have been developed to allow prediction of local and average heat transfer for these low-Reynolds-number flows with and without winglets. Representative experimental and numerical results presented in this paper reveal quantitative details of local fin-surface heat transfer in the vicinity of a circular tube with a single delta winglet pair downstream of the cylinder. The winglets were triangular (delta) with a 1:2 height/length aspect ratio and a height equal to 90% of the channel height. Overall mean fin-surface Nusselt-number results indicate a significant level of heat transfer enhancement (average enhancement ratio 35%) associated with the deployment of the winglets with oval tubes. Pressure drop measurements have also been obtained for a variety of tube and winglet configurations using a single-channel flow apparatus that includes four tube rows in a staggered array. Comparisons of heat transfer and pressure drop results for the elliptical tube versus a circular tube with and without winglets are provided. Heat transfer and pressure-drop results have been obtained for flow Reynolds numbers based on channel height and mean flow velocity ranging from 700 to 6500.

  12. Heat Transfer Enhancement for Finned-tube Heat Exchangers with Winglets

    Energy Technology Data Exchange (ETDEWEB)

    O' Brien, James Edward; Sohal, Manohar Singh

    2000-11-01

    This paper presents the results of an experimental study of forced convection heat transfer in a narrow rectangular duct fitted with a circular tube and/or a delta-winglet pair. The duct was designed to simulate a single passage in a fin-tube heat exchanger. Heat transfer measurements were obtained using a transient technique in which a heated airflow is suddenly introduced to the test section. High-resolution local fin-surface temperature distributions were obtained at several times after initiation of the transient using an imaging infrared camera. Corresponding local fin-surface heat transfer coefficient distributions were then calculated from a locally applied one-dimensional semi-infinite inverse heat conduction model. Heat transfer results were obtained over an airflow rate ranging from 1.51 x 10-3 to 14.0 x 10-3 kg/s. These flow rates correspond to a duct-height Reynolds number range of 670 – 6300 with a duct height of 1.106 cm and a duct width-toheight ratio, W/H, of 11.25. The test cylinder was sized such that the diameter-to-duct height ratio, D/H is 5. Results presented in this paper reveal visual and quantitative details of local fin-surface heat transfer distributions in the vicinity of a circular tube, a delta-winglet pair, and a combination of a circular tube and a delta-winglet pair. Comparisons of local and average heat transfer distributions for the circular tube with and without winglets are provided. Overall mean finsurface Nusselt-number results indicate a significant level of heat transfer enhancement associated with the deployment of the winglets with the circular cylinder. At the lowest Reynolds numbers (which correspond to the laminar operating conditions of existing geothermal air-cooled condensers), the enhancement level is nearly a factor of two. At higher Reynolds numbers, the enhancement level is close to 50%.

  13. Heat transfer and temperature distributions on finned tubes in cross flow. Waermeuebergangs- und Temperaturverteilungen an querangestroemten Rippenrohren

    Energy Technology Data Exchange (ETDEWEB)

    Schuez, G.

    1992-01-01

    The present paper deals with the flow and transport processes in high-performance heat exchanger tubes provided with external fins in cross flow. These have a broad area of applications, e.g. in chemical industry, in refrigeration, air conditioning and drying engineering, in the automotive industry, and on a commercial scale in dry cooling towers of power stations. Enhanced performance of heat exchangers can be obtained in three ways - in accordance with the defining equation of convective heat transfer - with the same wall material, fluid, and flow rate, namely by: increasing the wall surface area, e.g. by providing them with fins; intensifying the heat transfer; increasing the driving temperature difference. (orig.)

  14. 翅片螺距对锯齿螺旋翅片换热管特性的影响%Effects of fin pitch on heat transfer and flow resistance of serrated spiral-finned-tube banks

    Institute of Scientific and Technical Information of China (English)

    马有福; 袁益超; 陈昱; 刘海磊; 康明

    2011-01-01

    Serrated spiral-finned-tube, developed from solid spiral-finned-tube, has been widely applied in large-scale heat-exchange facility due to its advantages such as easier manufacture, more extended heat transfer surfaces, higher heat transfer coefficient and fin efficiency. For the effects of fin pitch on heat transfer and flow resistance of serrated spiral-finned-tube banks (SSBs) , nine SSBs with staggered layouts in terms of various fin pitch were tested based on the analysis on its influencing mechanism. The experimental results are as follows. At the same fin-side Re, Nu increases 19% and Eu decreases 8% with the fin pitch increased from 3. 831mm to 4.167mm. The effect of fin pitch on fin-side JVm becomes little when the fin pitch is larger than 4 mm since the gas penetrates the fin-gap more easily and fully flushes the fin-surface. The comprehensive heat transfer performance index j/f (ratio of Colburn heat transfer factor and friction factor) of fin-side first increases and then decreases as Re increases, with higher j/f in Re = 7000-10000. At the same fin-side Re, the index j/f is higher as the fin pitch is larger, increased about 28% with the fin pitch increased from 3. 831 mm to 4. 167 mm. The experimental results were compared with the correlations in literature. The correlations for Nu and Eu on SSBs with staggered layouts,which take fin pitch? Transverse pitch and longitudinal pitch of tube banks into accounts* were presented for engineering applications.%在连续螺旋翅片管基础上发展而来的锯齿螺旋翅片管具有易于制造、翅化比大,传热系数和翅片效率更高等优点,已广泛应用于各类大型气体换热设备中.为获得翅片螺距对锯齿螺旋翅片换热管特性的影响,在分析其影响机理的基础上对5个锯齿螺旋翅片管错列管束进行了实验研究.实验结果表明:在实验研究的翅片螺距范围(3.831~4.167 mm),相同Re下随翅片螺距增大,管束翅侧Nu增大19%,Eu减小8

  15. HeatTransfer Coefficients and Pressure Drops of The Finned Tube Heat Exchangers with Small Diameter Pipes

    Science.gov (United States)

    Tanaka, Hiroyoshi; Aoyama, Shigeo; Koma, Hachirou; Adachi, Masaaki

    In order to enhance the heat transfer coefficient of the fin used in the finned tube heat exchanger, newly designed fin surfaces, especially, with small diameter (≅4mm) pipes are developed. The experiments are made by the transient testing technique, and used the plastic fins scaling up 4 times of the actual metal fin size. The data of the heat transfer coefficient and the pressure drop are transformed to the actual metal fin data. The fin with the anomalous staggered pipe arrangement and the bridge-like cutting-out with inclined leg portion from stream line is found to have very high overall heat transfer coefficient which is about 1.8-fold increase in comparison with the conventional Louvered fin. In this paper the reason why such enhancement is caused is clarified by mean of the calculation based on the rectangular duct flow. The calculated values are coincident with the data of the experiment well.

  16. Flexible nanoscale high-performance FinFETs

    KAUST Repository

    Sevilla, Galo T.

    2014-10-28

    With the emergence of the Internet of Things (IoT), flexible high-performance nanoscale electronics are more desired. At the moment, FinFET is the most advanced transistor architecture used in the state-of-the-art microprocessors. Therefore, we show a soft-etch based substrate thinning process to transform silicon-on-insulator (SOI) based nanoscale FinFET into flexible FinFET and then conduct comprehensive electrical characterization under various bending conditions to understand its electrical performance. Our study shows that back-etch based substrate thinning process is gentler than traditional abrasive back-grinding process; it can attain ultraflexibility and the electrical characteristics of the flexible nanoscale FinFET show no performance degradation compared to its rigid bulk counterpart indicating its readiness to be used for flexible high-performance electronics.

  17. Inverse heat transfer problem in digital temperature control in plate fin and tube heat exchangers

    Science.gov (United States)

    Taler, Dawid; Sury, Adam

    2011-12-01

    The aim of the paper is a steady-state inverse heat transfer problem for plate-fin and tube heat exchangers. The objective of the process control is to adjust the number of fan revolutions per minute so that the water temperature at the heat exchanger outlet is equal to a preset value. Two control techniques were developed. The first is based on the presented mathematical model of the heat exchanger while the second is a digital proportional-integral-derivative (PID) control. The first procedure is very stable. The digital PID controller becomes unstable if the water volumetric flow rate changes significantly. The developed techniques were implemented in digital control system of the water exit temperature in a plate fin and tube heat exchanger. The measured exit temperature of the water was very close to the set value of the temperature if the first method was used. The experiments showed that the PID controller works also well but becomes frequently unstable.

  18. Heat transfer enhancement by a multilobe vortex generator in internally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Tsui, Y.Y.; Leu, S.W. [National Chiao Tung Univ., Hsinchu (Taiwan, Province of China). Dept. of Mechanical Engineering

    1999-04-01

    A three-dimensional computational method is employed to study the flow and heat transfer in internally finned tubes with a multilobe vortex generator inserted. Governing equations are discretized using the finite volume method. The irregular lobe geometry is treated using curvilinear nonstaggered grids. The linear interpolation method is adopted to calculate face velocities. The results show that secondary flows induced by the lobes are transformed to become axial vortices downstream of the vortex generator. As a consequence of the transport by the vortex flow, the core flow is moved to the fins and the tube wall, while the wall flow moves to the core. In this way, both heat transfer and flow mixing are enhanced. When the fin height is increased, the axial vortex is more restricted in the centerline region, and the strength of the vortex flow, represented by circulation, is decreased. In turn, the total pressure loss is also decreased. However, the heat transfer increases with fin height. Consequently, efficiency is greatly promoted.

  19. Film-wise condensation of R134a and R23/R134a mixture on horizontal finned tubes, influence of fin spacing

    Energy Technology Data Exchange (ETDEWEB)

    Belghazi, M.; Signe, J.C.; Marvillet, Ch. [CEA/Grenoble, Dept. de Thermohydraulique et de Physique (DTP-GRETh), 38 (France); Bontemps, A. [Universite Joseph-Fourier, Institut Universitaire de Technologie 1Grenoble I, 38 (France)

    1999-07-01

    The condensation of a pure fluid (R123a) and of a zeotropic mixture (R134a/R123) outside an horizontal bundle of finned tubes have been studied to understand the behaviour of the new refrigerants. Experimental results with pure R134a and several compositions of mixture R134a/R123 have been obtained during condensation on a bundle equipped with finned tubes of three different types: K26 (1024-fpm), K19(748-fpm), K11(433-fpm). The experimental data show the important effect of fin spacing and the different tubes has been made. The experimental data have also been compared to values calculated with the classical Bell and Ghaly model and a good agreement has been noticed. (authors)

  20. Bond resistance and design temperatures for high-finned tubes - A reappraisal

    Energy Technology Data Exchange (ETDEWEB)

    Taborek, J.

    1987-01-01

    The subject of bond resistances and maximum acceptable operating temperatures for various types of high-finned tubes is updated from the status of the last pertinent publications in the 1960s. The formation mechanism of the bond resistance under high and low temperatures is analyzed. Presently accepted industrial practices are critically evaluated. The lack of progress in the standardization of test procedures is noted with regret.

  1. Numerical investigation of forced convection of nano fluid flow in horizontal U-longitudinal finned tube heat exchanger

    Science.gov (United States)

    Qasim, S. M.; Sahar, A. F. A.; Firas, A. A.

    2015-11-01

    A numerical study has been carried out to investigate the heat transfer by laminar forced convection of nanofluid taking Titania (TiO2) and Alumina (Al2O3) as nanoparticles and the water as based fluid in a three dimensional plain and U-longitudinal finned tube heat exchanger. A Solid WORKS PREMIUM 2012 is used to draw the geometries of plain tube heat exchanger or U-longitudinal copper finned tube heat exchanger. Four U-longitudinal copper fins have 100 cm long, 3.8cm height and 1mm thickness are attached to a straight copper tube of 100 cm length, 2.2 cm inner diameter and 2.39 cm outer diameter. The governing equations which used as continuity, momentum and energy equations under assumptions are utilized to predict the flow field, temperature distribution, and heat transfer of the heat exchanger. The finite volume approach is used to obtain all the computational results using commercial ANSYS Fluent copy package 14.0 with assist of solid works and Gambit software program. The effect of various parameters on the performance of heat exchanger are investigated numerically such as Reynolds' number (ranging from 270 to 1900), volume consternation of nanoparticles (0.2%, 0.4%, 0.6%, 0.8%), type of nanoparticles, and mass flow rate of nanofluid in the hot region of heat exchanger. For 0.8% consternation of nanoparticles, heat transfer has significant enhancement in both nanofluids. It can be found about 7.3% for TiO2 and about 7.5% for Al2O3 compared with the water only as a working fluid.

  2. Flow induced vibrations in heat exchangers equipped with helical finned tubes; Stroemungsinduzierte Schwingungen in Spiralrippenrohrbuendelwaermetauschern

    Energy Technology Data Exchange (ETDEWEB)

    Fischer, M.

    2003-08-01

    Flow-induced vibrations resulting from acoustic resonance or fluid-elastic instability cause severe damage to finned-tube heat exchangers. There are hardly any publications on spiral finned tubes. This contribution presents experimental data on intrinsic frequencies and damping of spiral finned tubes as well as equations for calculating intrinsic frequencies. Stability limits for fluid-elastic instabilities were defined in flow experiments. Examples are presented to illustrate the applicability of the calculation method in preventing vibration-induced damage. [German] Stroemungsinduzierte Schwingungen in Rippenrohrwaermetauschern aufgrund von akustischer Resonanz bzw. fluidelastischer Instabilitaet fuehren immer wieder zu schweren Schadensfaellen. Hinsichtlich ihres Schwingungsverhaltens sind Spiralrippenrohre in der Literatur bislang vernachlaessigt worden, obwohl sie in der industriellen Anwendung immer mehr an Bedeutung gewinnen. Im vorliegenden Beitrag werden die Eigenfrequenzen und Daempfungen von Spiralrippenrohren experimentell untersucht und Berechnungsformeln fuer die Eigenfrequenzen angegeben. In Stroemungsexperimenten werden Stabilitaetsgrenzen fuer fluidelastische Instabilitaeten ermittelt. Anhand einiger Beispielfaelle wird aufgezeigt, dass das daraus entwickelte Berechnungsschema zur Absicherung gegen Schwingungsschaeden geeignet ist. (orig.)

  3. NUMERICAL AND EXPERIMENTAL STUDIES OF INFLUENCE OF THE CAUDAL FIN SHAPE ON THE PROPULSION PERFORMANCE OF A FLAPPING CAUDAL FIN

    Institute of Scientific and Technical Information of China (English)

    ZHANG Xi; SU Yu-min; WANG Zhao-li

    2011-01-01

    This article presents a comprehensive study of the effects of the caudal fin shape on the propulsion performance of a eandal fin in harmonic heaving and pitching.A numerical simulation based on an unsteady panel method was carried out to analyze the hydrodynamic performance of flapping caudal fins of three shapes (the whale caudal fin with the largest projected area, the dolphin caudal fin with the median projected area, and the tuna caudal fin with the smallest projected area).Then, a series of hydrodynamic experiments for three caudal fin shapes were performed.Both computational and experimental results indicate that the tuna caudal fin produces the highest efficiency.However the mean thrust coefficient of the tuna caudal fin is the smallest.It is found that although the mean thrust coefficient for the tuna caudal fin is not large, the input power of the tuna caudal fin is also quite small.So the tuna caudal fin achieves a high efficiency.

  4. Heat transfer characteristics and entropy generation for wing-shaped-tubes with longitudinal external fins in cross-flow

    Energy Technology Data Exchange (ETDEWEB)

    Ahmed, Sayed Ahmed E. Sayed; Mesalhy, Osama M.; Abdelatief, Mohamed A. [Zagazig University, Zagazig (Egypt)

    2016-06-15

    A numerical study is conducted to clarify heat transfer characteristics, effectiveness and entropy generation for a bundle of wingshaped-tubes attached to Longitudinal fins (LF) at downstream side. The air-side Re{sub a} ranged from 1.8 x 10{sup 3} to 9.7 x 10{sup 3} . The fin height (h{sub f}) and fin thickness (δ) have been changed as: (2 mm <= hf <= 12 mm) and (1.5 mm <= δ <= 3.5 mm). The analysis of entropy generation is based on the principle of minimizing the rate of total entropy generation that includes the generation of entropy due to heat transfer and friction losses. The temperature field around the wing-shaped-tubes with (LF) is predicted using commercial CFD FLUENT 6.3.26 software package. Correlations of Nu{sub a}, St{sub a}, and Bejan number (Be), as well as the irreversibility distribution ratio (Φ) in terms of Re{sub a} and design parameters for the studied bundle are presented. Results indicated that, installing fins with heights from 2 to 12 mm results in an increase in Nu{sub a} from 11 to 36% comparing with that of wing-shaped tubes without fins (NOF). The highest and lowest values of effectiveness(ε) at every value of the considered Re{sub a} range are occurred at hf = 6 mm and (NOF), espectively. The wing-shaped-tubes heat exchanger with hf = 6 mm has the highest values of (ε), efficiency index (η) and area goodness factor (G{sub a}) and also the lowest values of Φ and hence the best performance comparing with other arrangements. The minimum values of Φ are occurred at hf = 6 mm. (Be) decreases with increasing Re{sub a} for all studied hf. The heat transfer irreversibility predominates for (1800 <= Re{sub a} <= 4200) while the opposite is true for (6950 < Re{sub a} <= 9700). δ has negligible effect on Nu{sub a} and heat transfer irreversibility. Comparisons between the experimental and numerical results of the present study and those, previously, obtained for similar available studies showed good agreements.

  5. The Effect of Fin Pitch on Fluid Elastic Instability of Tube Arrays Subjected to Cross Flow of Water

    Science.gov (United States)

    Desai, Sandeep Rangrao; Pavitran, Sampat

    2016-07-01

    Failure of tubes in shell and tube exchangers is attributed to flow induced vibrations of such tubes. There are different excitations mechanisms due to which flow induced vibration occurs and among such mechanisms, fluid elastic instability is the most prominent one as it causes the most violent vibrations and may lead to rapid tube failures within short time. Fluid elastic instability is the fluid-structure interaction phenomenon which occurs when energy input by the fluid force exceeds energy expended in damping. This point is referred as instability threshold and corresponding velocity is referred as critical velocity. Once flow velocity exceeds critical flow velocity, the vibration amplitude increases very rapidly with flow velocity. An experimental program is carried out to determine the critical velocity at instability for plain and finned tube arrays subjected to cross flow of water. The tube array geometry is parallel triangular with cantilever end condition and pitch ratios considered are 2.6 and 2.1. The objective of research is to determine the effect of increase in pitch ratio on instability threshold for plain tube arrays and to assess the effect of addition of fins as well as increase in fin density on instability threshold for finned tube arrays. Plain tube array with two different pitch ratios; 2.1 and 2.6 and finned tube arrays with same pitch ratio; 2.6 but with two different fin pitches; such as fine (10 fpi) and coarse (4 fpi) are considered for the experimentation. Connors' equation that relates critical velocity at instability to different parameters, on which instability depends, has been used as the basis for analysis and the concept of effective diameter is used for the present investigation. The modal parameters are first suitably modified using natural frequency reduction setup that is already designed and developed to reduce natural frequency and hence to achieve experimental simulation of fluid elastic instability within the limited

  6. Numerical analysis of heat and mass transfer in a compact finned tubes air heat exchanger under dehumidification conditions

    Energy Technology Data Exchange (ETDEWEB)

    Benelmir, Riad; Mokraoui, Salim [Henri Poincare University, Faculty of Sciences and Technology, Lab. LERMAB, Vandoeuvre-Les-Nancy (France)

    2012-04-15

    A simulation model of a fin-and-tube heat exchanger is presented. The effect of the relative humidity, air speed, fin base temperature, and inlet air temperature on the estimation of the overall heat-transfer coefficient and fin efficiency under wet conditions is also investigated. This model considers a non-uniform airflow velocity as well as a variable sensible heat transfer coefficient. (orig.)

  7. Numerical analysis of heat and mass transfer in a compact finned tubes air heat exchanger under dehumidification conditions

    Science.gov (United States)

    Benelmir, Riad; Mokraoui, Salim

    2012-04-01

    A simulation model of a fin-and-tube heat exchanger is presented. The effect of the relative humidity, air speed, fin base temperature, and inlet air temperature on the estimation of the overall heat-transfer coefficient and fin efficiency under wet conditions is also investigated. This model considers a non-uniform airflow velocity as well as a variable sensible heat transfer coefficient.

  8. Hydrodynamic properties of fin whale flippers predict maximum rolling performance.

    Science.gov (United States)

    Segre, Paolo S; Cade, David E; Fish, Frank E; Potvin, Jean; Allen, Ann N; Calambokidis, John; Friedlaender, Ari S; Goldbogen, Jeremy A

    2016-11-01

    Maneuverability is one of the most important and least understood aspects of animal locomotion. The hydrofoil-like flippers of cetaceans are thought to function as control surfaces that effect maneuvers, but quantitative tests of this hypothesis have been lacking. Here, we constructed a simple hydrodynamic model to predict the longitudinal-axis roll performance of fin whales, and we tested its predictions against kinematic data recorded by on-board movement sensors from 27 free-swimming fin whales. We found that for a given swimming speed and roll excursion, the roll velocity of fin whales calculated from our field data agrees well with that predicted by our hydrodynamic model. Although fluke and body torsion may further influence performance, our results indicate that lift generated by the flippers is sufficient to drive most of the longitudinal-axis rolls used by fin whales for feeding and maneuvering.

  9. Condensation of Downward-Flowing Zeotropic Mixture HCFC-123/HFC-134a on a Staggered Bundle of Horizontal Low-Finned Tubes

    Science.gov (United States)

    Honda, Hiroshi; Takamatsu, Hiroshi; Takata, Nobuo

    Expenmentswere conducted to obtain row-by-row heat transfer data during condensation of downward-flowing zeotropic refrigerant mixture HCFC-123/HFC-134 a on a staggered bundle of horizontal low-finned tubes. The vapor temperature and the HFC-134a m ass fraction at the tube bundle inlet were maintained at about 50°C and 14% respectively. The refrigerant mass velocity ranged from 9 to 33 kg/m2s, and the condensation temperature difference from 2 to 12K. Four kinds of low-finned tubes with different fin geometry were tested. The highest heat transfer coefficient was obtained with a tube which showed the highest performance for HCFC-123. However, the effect of fin geometry was much smaller for the mixture than for HCFC-123. The heat transfer coefficient and the vapor-phase mass transfer coefficient decreased significantly with decreasing mass velocity. On the other hand, the mass transfer coefficient increased with condensation temperature difference. This was due to the effect of suction associated with condensation. On the basis of the analogy between heat and mass transfer, a dimensionless correlation of the mass transfer coefficient was developed for each tube.

  10. Multi-objective optimization of a plain fin-and-tube heat exchanger using genetic algorithm

    Science.gov (United States)

    Juan, Du; Qin, Qian Zuo

    2014-04-01

    In the present paper, a plate fin-and-tube heat exchanger (PFTHE) is considered for optimization with air and water as working fluid, four geometric variables are taken as parameters for optimization, a Genetic Algorithm (GA) was used to search for the optimal structure sizes of the PFTHE, the maximum total heat transfer rate and the minimum total pressure drop are taken as objective functions in GA, respectively. Performance of the optimized result was evaluated and correspondingly the total heat transfer rate, the total pressure drop, the heat transfer coefficient and the local Nusselt number, j-factor and friction factor ξ are calculated respectively. Results show that the total heat transfer rate of the optimized heat exchanger increased by about 2.1-9.2% comparing with the original one, the heat transfer coefficient increased by about 8.2-14.7% and the total pressure drop decreased by about 4.4-8% in the range of Re = 1200-14000.

  11. Statistical analysis of entropy generation in longitudinally finned tube heat exchanger with shell side nanofluid by a single phase approach

    OpenAIRE

    Konchada Pavan Kumar; Pv Vinay; Bhemuni Varaprasad

    2016-01-01

    The presence of nanoparticles in heat exchangers ascertained increment in heat transfer. The present work focuses on heat transfer in a longitudinal finned tube heat exchanger. Experimentation is done on longitudinal finned tube heat exchanger with pure water as working fluid and the outcome is compared numerically using computational fluid dynamics (CFD) package based on finite volume method for different flow rates. Further 0.8% volume fraction of aluminum oxide (Al2O3) nanofluid is conside...

  12. Numerical Analysis of Aerodynamic Characteristics of the Finned Surfaces with Cross-inclined Fins

    Directory of Open Access Journals (Sweden)

    Lagutin A. E.

    2016-12-01

    Full Text Available This paper presents results of numerical research and analyses air-side hydraulic performance of tube bundles with cross inclined fins. The numerical simulation of the fin-tube heat exchanger was performed using the Comsol Femlab software. The results of modeling show the influence of fin inclination angle and tube pitch on hydraulic characteristics of finned surfaces. A series of numerical tests were carried out for tube bundles with different inclination angles (γ =900, 850, 650, 60, the fin pitch u=4 mm. The results indicate that tube bundles with cross inclined fins can significantly enhance the average integral value of the air flow rate in channel between fins in comparison with conventional straight fins. Aerodynamic processes on both sides of modificated channel between inclined fins were analyzed. The verification procedures for received results of numerical modeling with experimental data were performed.

  13. Blower/air cooler with internally finned tubes; Ventilator-Luftkuehler mit innenberippten Rohren

    Energy Technology Data Exchange (ETDEWEB)

    Arnemann, M. [FKU - Forschungszentrum fuer Kaelte- und Umwelttechnik, Berlin (Germany)

    1997-12-31

    Heat transfer is higher in finned tubes than in smooth tubes. In order to assess the extent of improvement, internal heat tranfer coefficients and pressure losses of smooth and finned tubes were investigated on behalf of Walter Roller GmbH and Co. Two blower-type air coolers of identical design (except for the tubes) were investigated in a calorimeter using R22 and different refrigerant mass flows, evaporation temperatures and air temperatures. The results are the basis for new develoments by Walter Roller. Energetic assessment of the new type of evaporator was made on the basis of the DIN 8955 and ENV 328 standards. The results and findings are presented. (orig.) [Deutsch] Der Einsatz von innenberippten Rohren laesst im Vergleich mit glatten Rohren einen deutlich verbesserten inneren Waermeuebergang erwarten. Zur Abschaetzung der Groessenordnung dieser Verbesserungen wurden im Auftrag der Firma Walter Roller GmbH and Co. die inneren Waermeuebergangskoeffizienten und die Druckverluste von glatten und innenberippten Rohren experimentell bestimmt. Dazu wurden zwei bis auf die Rohre baugleiche Ventilator-Luftkuehler ineinem Kalorimeter untersucht. Mit dem Kaeltemittel R22 wurden fuer verschiedene Kaeltemittelmassenstroeme, Verdampfungstemperaturen und Lufttemperaturen die Kennzahlen bestimmt, die zur Charakterisierung der Rohre dienlich sind. Die Ergebnisse bildeten die Grundlage fuer eine Neuentwicklung im Hause Walter Roller. Die energetische Bewertung des neuen Verdampfertyps erfolgte in Anlehnung an die Normen DIN 8955 bzw. ENV 328. Die Untersuchungen und die Ergebnisse werden praesentiert. (orig.)

  14. Numerical Simulation and Experimental Research on Fin-tube Heat Exchanger with Combining Wide and Narrow Fins%宽片与窄片组合的翅片管换热器数值模拟与实验研究

    Institute of Scientific and Technical Information of China (English)

    张智; 赵夫峰; 王三辉; 曾小朗

    2014-01-01

    Based on the CFD analysis of the traditional fin-tube heat exchanger with 7 mm diameter tubes, a new fin-tube heat exchanger with combining wide and narrow fins was put forward. These two kinds of fin-tube heat exchangers were simulated with CFD software. The numerical simulation results showed that the air-side heat transfer performance of the fin-tube heat exchanger with combining wide and narrow fins was higher than that of traditional fin-tube heat exchanger, but the air-side pressure drop was lower. The experimental results showed that the performances of the new and traditional heat exchanger are almost the same.%基于对传统的7 mm 管径翅片管换热器的CFD分析,本文提出了一种新的宽片与窄片组合的翅片管换热器,并对这二种翅片管换热器用 CFD 软件进行了数值模拟。数值研究结果表明:宽片与窄片组合的翅片管换热器比常规翅片管换热器的空气侧换热性能好,但是它的空气侧压降较低。整机实验结果表明:二者性能几乎相当。

  15. Experimental investigation of enhanced heat transfer for fined circular tube heat exchanger with rectangular fins

    Institute of Scientific and Technical Information of China (English)

    LI Yong-xing; YANG Dong; CHEN Ting-kuan

    2006-01-01

    Presents a set of data for flow and heat transfer of finned-tube bundle under the condition of high air flow velocity. Air flow and heat transfer over a 4 ×4 ( columns × rows) finned-tube heat exchanger with rectangular fins was investigated experimentally in a wind tunnel with constant wall temperatures condition. The air flow velocity based on the minimum flow cross-section area over flow channel ranged from 13.8 to 50. 2 m/s,the heat transfer rate ranged from 21.8 to 47. 1 kW, and the air temperatures increase ranged from 10. 9 to 19. 8°C. The present results were compared with results calculated from correlations proposed by CSPE. For air flow velocity less than 25 m/s, these two results of heat transfer agreed well with each other, whereas for larger velocity, our test data disagreed with the CSPE correlations. For the friction factor, present data are much higher than the predicted results in the whole range. Finally, correlations for friction factors and heat transfer coefficients are proposed based on the experimental results.

  16. Compound forming technology of outside 3D integral fin of copper tubes

    Institute of Scientific and Technical Information of China (English)

    XIANG Jian-hua; TANG Yong; YE Bang-yan; ZHOU Wei; YAN Hui; HU Zhi-hua

    2009-01-01

    Using rolling-ploughing-extrusion compound processing methods, a 3D integral-fin structure on outside surface of red copper tube with diameter of 16.0 mm and wall thickness of 1.5 mm was obtained. When both rolling depth and ploughing-extrusion (P-E) depth were 0.2 mm, rotating speed was 50 r/min, feed speed was 0.16 mm/r, 3D fin structures with height of 0.25 mm were gotten. Two different fin structures were obtained in grooves formed with rolling-ploughing-extrusion compound forming technology and observed by scanning electron microscope(SEM). One is the compound structure with V-shaped groove and U-shaped groove, and the other is the single structure with V-shaped grooves. Two kinds of groove structures obtained by rolling processing and ploughing extrusion processing are restricted together by groove interval and rolling depth, and pitch and P-E depth, respectively. Based on the analysis of interaction of rolling and P-E processing, it is found from the result that the outside 3D integral-fin can be achieved by rolling-ploughing-extrusion compound processing when single V-shaped groove structures are formed by both rolling and P-E processing.

  17. Numerical calculation and measuring of transport phenomena as integral parameters in cross-flowed finned tube heat exchangers; Numerische Berechnung und Messung der Transportvorgaenge sowie integraler Kenngroessen in quer angestroemten Rippenrohrwaermeuebertragern

    Energy Technology Data Exchange (ETDEWEB)

    Geiser, P.

    2003-07-01

    For the first row of extended finned tubes in cross flow, both the heat and mass transport and the integral pressure loss are determined. The tube shape, the dimensions of fin and tube, the positioning of tube and fin, the fin spacing, the thermal conductivity and the flow velocity are varied. For numerical simulation of the three-dimensional local transport phenomena, the balance equations for mass, momentum and energy are solved with the help of the commercial software FIDAP, taking account of the temperature-dependence of the material properties. From the resulting velocity, pressure and temperature fields in the configurations of the finned tube, derived characteristic parameters such as friction factor, integral fluid and fin temperature, fin efficiency, heat transfer coefficient, heat flux and fin-performance factor are determined with the help of self-developed evaluation programs. The numerical calculations of heat transfer and pressure loss show that a good correspondence with measured values in normal industrial applications for Re{<=}2000 is achieved. Local mass and heat transport in the fin duct is made visible via methods of convective mass transfer and is quantified for individual cases. For measurement purposes, enlarged models of the finned tubes are made of easily workable materials and set up in modular fashion so that tube shapes of very varied kinds can be investigated. Tube contours used in industrial applications are compared with a large number of new developments from the point of view of fluid dynamics and thermal properties. Local transport processes in the fin duct such as horseshoe vortices or separation areas which are of decisive significance for thermal performance can be made visible by means of the convective mass transfer method employed. The investigations have shown that finned tubes with large-radius of leading tube-profiles and large distances between the leading edge of the fin and the tube itself, as well as large fin

  18. Heat and fluid flow characteristics of an oval fin-and-tube heat exchanger with large diameters for textile machine dryer

    Science.gov (United States)

    Bae, Kyung Jin; Cha, Dong An; Kwon, Oh Kyung

    2016-11-01

    The objectives of this paper are to develop correlations between heat transfer and pressure drop for oval finned-tube heat exchanger with large diameters (larger than 20 mm) used in a textile machine dryer. Numerical tests using ANSYS CFX are performed for four different parameters; tube size, fin pitch, transverse tube pitch and longitudinal tube pitch. The numerical results showed that the Nusselt number and the friction factor are in a range of -16.2 ~ +3.1 to -7.7 ~ +3.9 %, respectively, compared with experimental results. It was found that the Nusselt number linearly increased with increasing Reynolds number, but the friction factor slightly decreased with increasing Reynolds number. It was also found that the variation of longitudinal tube pitch has little effect on the Nusselt number and friction factor than other parameters (below 2.0 and 2.5 %, respectively). This study proposed a new Nusselt number and friction factor correlation of the oval finned-tube heat exchanger with large diameters for textile machine dryer.

  19. Heat transfer and pressure drop characteristics of plain finned heat exchangers having 5.0 mm tubes

    Energy Technology Data Exchange (ETDEWEB)

    Kim, Nae Hyun; Ham, Jung Ho; Oh, Wang Ku [Incheon Univ., Incheon (Korea, Republic of); Choi, Yong Hwa; Gaku, Hayase [Samsung Electric Company, Suwon (Korea, Republic of)

    2007-07-01

    In this study, pressure drop and heat transfer characteristics of plain finned heat exchangers having 5.0 diameter (fin collar 5.3 mm) tubes were investigated. Six samples having different fin pitches and tube rows were tested. The fin pitch had a negligible effect on j and f factors. Both j and f factors decreased as the number of tube row increased, although the difference was not significant for the f factor. When compared with the previous 7.3 mm diameter data, both the present j and f factors yielded lower values. However, the j/f ratio was larger at low Reynolds numbers. Possible reasoning is provided from the flow pattern consideration. Comparison with existing correlations were made.

  20. Linear correlation of heat transfer and friction in helically-finned tubes using five simple groups of parameters

    Energy Technology Data Exchange (ETDEWEB)

    Zdaniuk, Gregory J. [Ramboll Whitbybird Ltd., 60 Newman Street, London W1T 3DA (United Kingdom); Luck, Rogelio; Chamra, Louay M. [Department of Mechanical Engineering, Mississippi State University, 210 Carpenter Engineering Building, P.O. Box ME, MS 39762-5925 (United States)

    2008-07-01

    A linear regression approach was used to correlate experimentally-determined Colburn j-factors and Fanning friction factors for flow of liquid water in helically-finned tubes. Experimental data came from eight enhanced tubes with helix angles between 25 and 48 , number of fin starts between 10 and 45, fin height-to-diameter ratios between 0.0199 and 0.0327, and Reynolds numbers ranging from 12,000 to 60,000. The current study revealed that, in helically-finned tubes, logarithms of both friction and Colburn j-factors can be correlated with linear combinations of the same five simple groups of parameters and a constant. The proposed functional relationship was tested with independent experimental data yielding excellent results. (author)

  1. Beneficial design of unbaffled shell-and-tube heat exchangers for attachment of longitudinal fins with trapezoidal profile

    Directory of Open Access Journals (Sweden)

    Balaram Kundu

    2015-03-01

    Full Text Available A parametric variation followed with Kern’s method of design of extended surface heat exchanger has been made for an unbaffled shell-and-tube heat exchanger problem. For this analysis, the rectangular and trapezoidal fin shapes longitudinally attached to the fin tubes are taken. In comparison with the attachment of trapezoidal fins, it is found that the heat transfer rate was lesser than the rectangular cross section by keeping a constant outer diameter of the shell along with all other constraints of a heat exchanger design, namely, number of passes, tube outer diameter, tube pitch layout, etc. But when the total volume of the fin over a tube was kept constraint, using trapezoidal fins the heat transfer rate is found to be increased and consequently the pressure drop decreases much more than in the case of fins with rectangular cross section. This optimization has shown beneficial results in all the cases of different constraints of heat exchanger design analysis.

  2. A computer program for designing fin-and-tube heat exchanger for EGR cooler application

    Science.gov (United States)

    Syaiful, Marwan, M. A.; Tandian, N. P.; Bae, M.

    2016-03-01

    EGR (exhaust gas recirculation) cooler is a kind of heat exchanger that is used to cool exhaust gas recirculation prior to be mixed with fresh air in an intake manifold of vehicle in order to obtain good reduction of NOxemissions. A fin-and-tube heat exchanger is more preferred as an EGR cooler than a shell-and-tube heat exchanger in this study due to its compactness. Manually designing many configurations of fin-and-tube heat exchanger for EGR cooler application consumes a lot of time and is high cost. Therefore, a computer aided design process of EGR cooler is required to overcome this problem. The EGR cooler design process was started by arranging the sequences of calculation algorithm in a computer program. A cooling media for this EGR cooler is air. The design is based on the effectiveness-number transfer unit (NTU) method. The EGR cooler design gives the geometry, heat transfer surface area, heat transfer coefficient and pressure drop of the EGR cooler. Comparison of the EGR cooler Nusselt number obtained in this study and that reported in literature shows less than 6.2% discrepancy.

  3. Experimental investigation of forced-convection in a finned rhombic tube of the flat-plate solar collectors

    DEFF Research Database (Denmark)

    Taherian, Hessam; Yazdanshenas, Eshagh

    2006-01-01

    Due to scarcity of literature on forced-convection heat transfer in a solar collector with rhombic cross-section absorbing tubes, a series of experiments was arranged and conducted to determine heat transfer coefficient. In this study, a typical rhombic cross-section finned tube of flat......-plate collectors used as the test section. Two correlations were proposed for the Nusselt number as a function of the Reynolds number and the Prandtl number based on hydraulic diameter for various heat fluxes. The temperature distribution along the finned tube for the fluid and the wall were also illustrated....

  4. Effects of fin pitch on heat transfer and flow resistance of twisted-serrated spiral finned tube banks%翅片螺距对折齿型螺旋翅片管束性能的影响

    Institute of Scientific and Technical Information of China (English)

    王学刚; 袁益超

    2016-01-01

    为了提高平齿型翅片管的强化传热效果,通过改变其锯齿的扭转方向和偏折角度得到了折齿型螺旋翅片管。利用数值模拟和模化试验相结合的方法对基管外径分别为38 mm和51 mm的折齿型螺旋翅片管束进行研究,得到了翅片螺距对折齿型螺旋翅片管束的换热与阻力性能的影响规律和最优翅片螺距。结果表明:翅片螺距 Pf在3.63~8.47 mm范围内,空气侧Nusselt数Nu随Pf增大呈先递增后递减的趋势;当Pf大于6.35 mm时,翅片螺距增大对Nu的影响相对已不明显;空气侧Euler数Eu随Pf增大而减小。对于基管外径分别为38 mm和51 mm的折齿型螺旋翅片管束,Pf为6.35 mm时其性能指标Nu·f−1/3均最大,因此Pf=6.35 mm是最优翅片螺距。%In order to improve the heat transfer enhancement of serrated spiral-finned-tube, twisted-serrated spiral finned tube was fabricated by changing the deflection angle and the twisted direction of serration. Twisted-serrated spiral finned tube banks with the diameters of 38 mm and 51 mm were researched by numerical simulation combined with modeling experiments. The influence of fin pitch on heat transfer and resistance characteristics of twisted-serrated spiral finned tube was obtained. The results showed thatNu at air-side increased firstly and then decreased with the increase of fin pitch from 3.63—8.47 mm. The effects of fin pitch onNu at air-side was weaker when the fin pitch was larger than 6.35 mm.Eu at air-side decreased with increasing fin pitch. For twisted-serrated spiral finned tube banks with the diameters of 38 mm and 51 mm, comprehensive performance indexNu·f−1/3 was the maximum when the fin pitch is 6.35 mm. Thus, Pf=6.35 mm was the optimum fin pitch within the range of 3.63—8.47 mm.

  5. Heat transfer from a horizontal finned tube bundle in bubbling fluidized beds of small and large particles

    Energy Technology Data Exchange (ETDEWEB)

    Devaru, C.B. [Jayachamaraja College of Engineering, Mysore (India). Dept. of Mechanical Engineering; Kolar, A.K. [Indian Inst. of Technology, Madras (India). Dept. of Mechanical Engineering

    1995-12-31

    Steady state average heat transfer coefficient measurements were made by the local thermal simulation technique in a cold, square, bubbling air-fluidized bed (0.305 m x 0.305 m) with immersed horizontal finned tube bundles (in-line and staggered) with integral 60{degree} V-thread. Studies were conducted using beds of small (average particle diameter less than 1 mm) sand particles and of large (average particle diameter greater thin 1 mm) particles (raagi, mustard, millet and coriander). The fin pitch varied from 0.8 to 5.0 mm and the fin height varied from 0.69 to 4.4 mm. The tube pitch ratios used were 1.75 and 3.5. The influence of bed particle diameter, fluidizing velocity, fin pitch, and tube pitch ratio on average heat transfer coefficient was studied. Fin pitch and bed particle diameter are the most significant parameters affecting heat transfer coefficient within the range of experimental conditions. Bed pressure drop depends only on static bed height. New direct correlations, incorporating easily measurable quantities, for average heat transfer coefficient for finned tube bundles (in-line and staggered) are proposed.

  6. In-service inspection method for low-finned ferritic stainless steel tubes for new heat exchanger

    Energy Technology Data Exchange (ETDEWEB)

    Iwai, O.; Goto, M. [Toshiba Corp., Yokohama (Japan)

    1994-12-31

    Conventional inner eddy current test cannot obtain sufficient evaluation for low finned ferritic stainless steel tube inspection. The authors tried various methods and developed special partial saturation eddy current method. This paper summarizes typical experimental results of fundamental studies and trials, and introduces developed ECT data acquisition and evaluation system. Moisture Separator Heater (MSH) used in ABWR (Advanced Boiling Water Reactor) plant is a new type heat exchanger to increase plant thermal efficiency. There are four single tubesheet heaters in a MSH vessel. Each heater has hundreds of low finned tubes made of ferritic stainless steel. In nuclear power plants, non-magnetic materials (austenitic stainless steel, titanium, aluminum brass, etc.,) are mainly used as heat exchanger tubes such as the tubes of feedwater heater, condenser, evaporator and so on. Conventional ECT (Eddy Current Test) method are easily applied for the inspection of these heat exchanger tubes. In recent years, the authors started using ferritic stainless steel tube for new heat exchangers such as MSH because of its superior heat transfer efficiency. However, high permeability of ferritic stainless steel prevents the inspection of these tubes using conventional ECT method. To inspect MSH tubes periodically is important to confirm and maintain reliability of MSH. They tried applying various inspection methods and have developed special ECT method for low finned ferritic stainless steel tubes.

  7. Heat transfer augmentation along the tube wall of a louvered fin heat exchanger using practical delta winglets

    Energy Technology Data Exchange (ETDEWEB)

    Lawson, Michael J.; Thole, Karen A. [Mechanical and Nuclear Engineering Department, The Pennsylvania State University, University Park, PA 16802 (United States)

    2008-05-15

    Delta winglets are known to induce the formation of streamwise vortices and increase heat transfer between a working fluid and the surface on which the winglets are placed. This study investigates the use of delta winglets to augment heat transfer on the tube surface of louvered fin heat exchangers. It is shown that delta winglets placed on louvered fins produce augmentations in heat transfer along the tube wall as high as 47% with a corresponding increase of 19% in pressure losses. Manufacturing constraints are considered in this study whereby piercings in the louvered fins resulting from stamping the winglets into the louvered fins are simulated. Comparisons of measured heat transfer coefficients with and without piercings indicate that piercings reduce average heat transfer augmentations, but significant increases still occur with respect to no winglets present. (author)

  8. Exergy destruction analysis of a vortices generator in a gas liquid finned tube heat exchanger: an experimental study

    Science.gov (United States)

    Ghazikhani, M.; Khazaee, I.; Monazzam, S. M. S.; Takdehghan, H.

    2016-11-01

    In the present work, the effect of using different shapes of vortices generator (VG) on a gas liquid finned heat exchanger is investigated experimentally with irreversibility analysis. In this project the ambient air with mass flow rates of 0.047-0.072 kg/s is forced across the finned tube heat exchanger. Hot water with constant flow rate of 240 L/h is circulated inside heat exchanger tubes with inlet temperature range of 45-73 °C. The tests are carried out on the flat finned heat exchanger and then repeated on the VG finned heat exchanger. The results show that using the vortex generator can decrease the ratio of air side irreversibility to heat transfer (ASIHR) of the heat exchanger. Also the results show that the IASIHR is >1.05 for all air mass flow rates, which means that ASIHR for the initial heat exchanger is higher than 5 % greater than that of improved heat exchanger.

  9. Flow and Heat Transfer Characteristics Comparison Between Flat Wave-Fin Tube and Corrugated-Fin Flat Tube%平直翅片管与波浪翅片管流动换热性能比较

    Institute of Scientific and Technical Information of China (English)

    张璟; 李宴君; 温娟; 唐大伟

    2011-01-01

    扁管外焊蛇形平直翅片是直接空冷凝汽器翅片管的一种常见形式,为进一步提高空冷凝汽器的冷凝效率,建立了波浪翅片扁管的三维物理数学模型。通过数值模拟,获得了不同空气入口流速下,波浪翅片扁管和平直翅片扁管外冷却空气的流场和温度场,通过对流换热系数和流动损失的对比分析表明,波浪翅片扁管在空气侧换热系数和流动损失方面比平直翅片扁管有一定的优势,在低风速的工况下,优势较为明显。%The flat wave-fin tube condenser is well applied in direct-cooled power plants, In order to further enhance the condensing efficiency of air cooled condensers, a three dimensional physicomathematical model of a corrugated-fin tube has been established. The air flow and temperature fields outside the fiat wave-fin tube and corrugated-fin tube were numerically simulated at different inlet air velocities. Through comparison of the convection heat transfer coefficient and the flow loss etc., it shows that the corrugated-fin flat tube boast certain superiority in aspects of the heat transfer coefficient and the flow loss to the air side as compared with that of the flat wave-fin tube. In the case of low inlet air velocity, the advantage was more obvious.

  10. Impacts of plasma-induced damage due to UV light irradiation during etching on Ge fin fabrication and device performance of Ge fin field-effect transistors

    Science.gov (United States)

    Mizubayashi, Wataru; Noda, Shuichi; Ishikawa, Yuki; Nishi, Takashi; Kikuchi, Akio; Ota, Hiroyuki; Su, Ping-Hsun; Li, Yiming; Samukawa, Seiji; Endo, Kazuhiko

    2017-02-01

    We investigated the impacts of plasma-induced damage due to UV light irradiation during etching on Ge fin fabrication and the device performance of Ge fin field-effect transistors (Ge FinFETs). UV light irradiation during etching affected the shape of the Ge fin and the surface roughness of the Ge fin sidewall. A vertical and smooth Ge fin could be fabricated by neutral beam etching without UV light irradiation. The performances of Ge FinFETs fabricated by neutral beam etching were markedly improved as compared to those of Ge FinFETs fabricated by inductively coupled plasma etching, in which the UV light has an impact.

  11. Heat transfer measurements on smooth and finned tubes in a standard apparatus for boiling experiments. Waermeuebergangsmessungen an Glatt- und Rippenrohren in einer Standardapparatur fuer Siedeversuche

    Energy Technology Data Exchange (ETDEWEB)

    Fath, W.

    1986-07-28

    The use of Rankine cycles with refrigerants or other organic working fluids for waste heat recovery has been a matter of discussion lately. The evaporating pressure is higher in these systems than in conventional application of finned tubes, so the problems of heat transfer in nucleate boiling on finned tubes are investigated here. Measurements were made on smooth and finned tubes and on surface-treated smooth and finned tubes. Refrigerant R-22 was used for the experiments; the measurements cover a wide range of pressures. (HAG).

  12. Heat-transfer coefficients for air flowing in round tubes, in rectangular ducts, and around finned cylinders

    Science.gov (United States)

    Drexel, Rober E; Mcadams, William H

    1945-01-01

    Report reviews published data and presents some new data on heat transfer to air flowing in round tubes, in rectangular ducts, and around finned cylinders. The available data for heat transfer to air in straight ducts of rectangular and circular cross section have been correlated in plots of Stanton number versus Reynolds number to provide a background for the study of the data for finned cylinders. Equations are recommended for both the streamlined and turbulent regions, and data are presented for the transition region between turbulent and laminar flow. Use of hexagonal ends on round tubes causes the characteristics of laminar flow to extend to high Reynolds numbers. Average coefficients for the entire finned cylinder have been calculated from the average temperature at the base of the fins and an equation which was derived to allow for the effectiveness of the fins. The available results for each finned cylinder are correlated herein in terms of graphs of Stanton number versus Reynolds number. In general, for a given Reynolds number, the Stanton number increases with increases in both spacing and width of the fins, and is apparently independent of cylinder diameter and temperature difference. For a given coefficient of heat transfer improved baffles and rough or wavy surfaces give a substantial reduction in pumping power per unit of heat transfer surface and a somewhat smaller decrease in pressure drop. (author)

  13. Numerical Analysis of Flow Distribution in a Sodium Chamber of a Finned-tube Sodium-to-Air Heat Exchanger

    Energy Technology Data Exchange (ETDEWEB)

    Jo, Youngchul; Son, Seokkwon; Kim, Hyungmo; Eoh, Jaehyuk; Jeong, Jiyoung [Korea Atomic Energy Research Institute, Daejeon (Korea, Republic of)

    2015-10-15

    DHR systems consist of two diverse heat removal loops such as passive and active DHR systems, and the heat load imposed on the primary sodium pool is safely rejected into the environment through different kinds of sodium-to-air heat exchangers, e.g. M-shape and helical-coil type air-coolers. The former is called as an FHX(Forced-draft sodium-to-air Heat Exchanger) and the latter is simply called as an AHX(natural-draft sodium-to-Air Heat Exchanger). In a general sodium-to-air heat exchanger design, convection resistance in a shell-side air flow path becomes dominant factor affecting the mechanism of conjugate heat transfer from the sodium flow inside the tube to the air path across the sodium tube wall. Hence verification of the flow and heat transfer characteristics is one of the most important tasks to demonstrate decay heat removal performance. To confirm a kind of ultimate heat sink heat exchanger, a medium-scale Sodium thermal-hydraulic Experiment Loop for Finned-tube sodium-to-Air Heat exchanger (here after called the SELFA) has been designed and is recently being constructed at KAERI site. The introduction of the flow baffle inside the upper sodium chamber of the model FHX unit in the SELFA facility is briefly proposed and discussed as well. The present study aims at introducing a flow baffle design inside the upper sodium chamber to make more equalized flowrates flowing into each heat transfer tube of the model FHX unit. In the cases without the flow baffle geometry, it was observed lager discrepancies in flowrates at the heat transfer tubes. However it was also found that those kinds of discrepancies could be definitely decreased at around 1/10 by employing a flow baffle.

  14. Numerical Simulation of Heat Transfer in Finned Tube of Heat Recovery Unit Using Fluid-Solid Coupled Method

    Directory of Open Access Journals (Sweden)

    Lin Wei

    2015-01-01

    Full Text Available Heat recovery unit (HRU is a heat exchange device in drying process. In HRU, room air is preheated by waste hot air and then transported to drying oven to remove moisture, which helps to save both energy and time. The main purpose of this paper is to build a heat transfer model of HRU and study its characteristics. A numerical method based on fluid-solid coupling was used to calculate the heat transfer between tube and fluids, and the actual structure was simplified to improve computation efficiency. The results were validated by theoretical calculation and experiments. Effects of Reynolds number (Re on outlet temperature, Nusselt number, and pressure drop were investigated. It was found that the thermal resistance of shell side is large, by reducing which the total heat transfer coefficient can be improved. The difference between finned tube and smooth tube is in the shell side. Larger Re of shell side leads to good heat transfer performance but also larger pressure drop which increases the flow resistance.

  15. High performance flexible CMOS SOI FinFETs

    KAUST Repository

    Fahad, Hossain M.

    2014-06-01

    We demonstrate the first ever CMOS compatible soft etch back based high performance flexible CMOS SOI FinFETs. The move from planar to non-planar FinFETs has enabled continued scaling down to the 14 nm technology node. This has been possible due to the reduction in off-state leakage and reduced short channel effects on account of the superior electrostatic charge control of multiple gates. At the same time, flexible electronics is an exciting expansion opportunity for next generation electronics. However, a fully integrated low-cost system will need to maintain ultra-large-scale-integration density, high performance and reliability - same as today\\'s traditional electronics. Up until recently, this field has been mainly dominated by very weak performance organic electronics enabled by low temperature processes, conducive to low melting point plastics. Now however, we show the world\\'s highest performing flexible version of 3D FinFET CMOS using a state-of-the-art CMOS compatible fabrication technique for high performance ultra-mobile consumer applications with stylish design. © 2014 IEEE.

  16. Experimental investigation on condensation heat transfer of R134a on single horizontal copper and stainless steel three-dimensional finned tubes

    Science.gov (United States)

    Qin, Peng; Zhang, Zhengguo; Xu, Tao; Gao, Xuenong; Wang, Shuangfeng

    2013-07-01

    Condensation heat transfer characteristics of R134a on the horizontal copper and stainless steel three-dimensional (3D) finned tubes are experimentally investigated. The objective is to obtain the basic data for film condensation of R134a on low and high thermal conductivity 3D enhanced tubes. Experiments were carried out at saturation temperatures of 39 °C and wall subcoolings from 3.2 to 10.5 °C. The results show that the condensation heat transfer coefficients on the smooth copper and stainless steel tubes are smaller than those predicted by the Nusselt analysis by 4.4% and 4.8%, respectively. The average enhancement factors provided by the copper and stainless steel 3D finned tubes are 7.86 and 3.34, respectively. The copper 3D finned tube has higher enhancement factor than that of the stainless steel 3D finned tube, due to its high fin and thermal conductivity.

  17. Volume Averaging Theory (VAT) based modeling and closure evaluation for fin-and-tube heat exchangers

    Science.gov (United States)

    Zhou, Feng; Catton, Ivan

    2012-10-01

    A fin-and-tube heat exchanger was modeled based on Volume Averaging Theory (VAT) in such a way that the details of the original structure was replaced by their averaged counterparts, so that the VAT based governing equations can be efficiently solved for a wide range of parameters. To complete the VAT based model, proper closure is needed, which is related to a local friction factor and a heat transfer coefficient of a Representative Elementary Volume (REV). The terms in the closure expressions are complex and sometimes relating experimental data to the closure terms is difficult. In this work we use CFD to evaluate the rigorously derived closure terms over one of the selected REVs. The objective is to show how heat exchangers can be modeled as a porous media and how CFD can be used in place of a detailed, often formidable, experimental effort to obtain closure for the model.

  18. Heat Transfer in a Fin-Tube Type Heat Exchanger with Multiple Inlet Ports

    Science.gov (United States)

    Umekawa, Hisashi; Ozawa, Mamoru; Kawamoto, Akira; Takifuji, Tomonori; Kataoka, Masaki

    Numerical simulation of gas flow in a fin-tube type heat exchanger model has been conducted. The simulation model is two-dimensional and has three inlet ports at the lower boundary and one exit port at the upper boundary. The flow field is partitioned into several sub-channels by spacers. In order to realize the uniform temperature distribution at the exit port and relatively uniform heat transfer rate among the spacers,It is necessary to arrange so that the higher temperature fluid is injected from center port at lower velocity and the lower temperature fluid is injected from both side ports at higher velocity. The thermal flow visualization experiment with thermosensitive liquid-crystal sheet has confirmed the simulation results.

  19. Experimental and numerical investigation of a louvered fin and elliptical tube compact heat exchanger

    Directory of Open Access Journals (Sweden)

    Pooranachandran Karthik

    2015-01-01

    Full Text Available In the present work, an experimental investigation is carried out to analyze the heat transfer characteristics of a louvered fin and elliptical tube compact heat exchanger used as a radiator in an internal combustion engine. Experiments are conducted by positioning the radiator in an open-loop wind tunnel. A total of 24 sets of air, water flow rate combinations are tested, and the temperature drops of air and water were acquired. A numerical analysis has been carried out using Fluent software (a general purpose computational fluid dynamics simulation tool for three chosen data from the experiments. The numerical air-side temperature drop is compared with those of the experimental values. A good agreement between the experimental and numerical results validates the present computational methodology.

  20. Experimental study on heat transfer enhancement of a helically baffled heat exchanger combined with three-dimensional finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Zhang Zhnegguo; Xu Tao; Fang Xiaoming [South China University of Technology, Guangzhou (China). Ministry of Education

    2004-10-01

    Heat transfer and pressure drop of helically baffled heat exchanger combined with petal-shaped finned tubes for oil (ISO VG-32) cooling with water as coolant was experimentally studied. The tube side heat transfer coefficient was obtained by a modified Wilson plot technique. Results were presented as plots of the shell side heat transfer coefficient based on the actual outside surface area of tube bundle and pressure drop against volumetric flow rate of oil. Under experimental conditions, the maximum shell side heat transfer coefficient is 2265 W/m{sup 2} K, the corresponding shell side pressure drop is 91 kPa. The preliminary heat transfer enhancement mechanisms were discussed for oil flow helically on outside surface of petal-shaped finned tubes. (author)

  1. Experimental study of an externally finned tube with internal heat transfer enhancement for phase change thermal energy storage

    Science.gov (United States)

    Martinelli, M.; Bentivoglio, F.; Couturier, R.; Fourmigué, J.-F.; Marty, P.

    2016-09-01

    After having presented the design of a latent heat thermal energy storage system (LHTESS) for district heating, experimental results of a vertical tube-in-shell LHTESS are discussed. The tube is radially finned on its external wall to enhance the heat transfer in the phase change material. The test rig is operated with flow conditions corresponding to the proposed design. As the internal flow of heat transfer fluid (HTF) appears to be laminar and is highly influenced by buoyancy forces, which results in mixed convection regime, cross-sectional area reducers are installed inside the HTF tube in order to reduce the Rayleigh number and thus natural convection. Experimental results are presented for two finned tubes, with and without internal heat transfer enhancement respectively.

  2. Air side thermal performance of wavy fin heat exchangers produced by selective laser melting

    Science.gov (United States)

    Kuehndel, J.; Kerler, B.; Karcher, C.

    2016-09-01

    Wavy fins are widely used for off-road vehicle coolers, due to their dust resistance. In this study, heat exchanger elements with wavy fins were examined in an experimental study. Due to independence of tooling and degrees of freedom in design, rapid prototyping technique selective laser melting was used to produce heat exchanger elements with high dimensional accuracy. Tests were conducted for air side Reynolds number Re of 1400-7400 varying wavy amplitude and wave length at a constant water flow rate of 9.0m3/h inside the tubes. The effects of wavy amplitude and wave length on the air side thermal performance were studied. Experimental correlation equations for Nu and ­ were derived by regression analysis.

  3. Improved thermal performance of a hydronic radiant panel heating system by the optimization of tube shapes

    Institute of Scientific and Technical Information of China (English)

    Young T. CHAE; Kwang Ho LEE; Jae Sung PARK

    2011-01-01

    The thermal performance enhancement of the hydronic radiant floor heating system by tube shape refinements is investigated in this paper. Both analytical and detailed numerical modelings are carried out to predict the performance of the radiant system. While the simple analytical model briefly investigates the possibility of the effect of the tube shape improvement with the parametric analysis, the commercial computational fluid dynamics (CFD) code (Ansys/CFX) is used to perform the detailed 3D analysis under different tube shape conditions. The fin thickness, the number of fins, and the tube thermal conductivity turn out to have significant effects on the radiant system performance. The potential energy saving impacts of the tube shape refinements are also discussed. The tube shape improvement turns out to increase the floor surface temperature and to decrease the hot water temperature drop across the system, resulting in heating energy savings.

  4. Selection of structure parameters for H-finned tube%H型鳍片管结构参数选取方法

    Institute of Scientific and Technical Information of China (English)

    赵斌; 赵利杰; 王庆功; 晁俊楠; 吕俊复

    2015-01-01

    Two indicators were proposed to evaluate the performance of H-type finned tube,i.e. the heat exchange per unit mass and the recovered heat transfer per unit power of the fan, and a selection method was derived to determine the structure parameters for the H-type finned tube. Numerical studies were performed to investigate the H-type finned tube with different fin widths and pitches. The results show that with the increase of fin width, the heat transfer per unit mass of finned tube increases first and then deceases, and when this indicator reaches the maximum value with different fin pitches, the fin width is between 55 and 60 mm. With the increase of fin width, the recovered heat transfer per unit power of the fan also increases first and then deceases, but when this indicator reaches the maximum value with different fin pitches, the fin width increases gradually. The fin pitch has the minimum value when both indicators reach the maximum value, so the two indicators as well as the manufacturing process and fouling characteristics should be taken into consideration for selecting the structure parameters.%提出了单位质量鳍片管换热量与引风单位耗功所回收热量两个评价H型鳍片管性能的主要指标,给出了H型鳍片管结构参数选取的方法.通过对不同鳍片宽度与鳍片间距的H型鳍片管进行数值研究发现,单位质量鳍片管换热量随鳍片宽度的增加先增加后降低,并且在不同鳍片间距下,该指标达到最大值时所对应的鳍片宽度均在55~60 mm;引风单位耗功所回收热量随鳍片宽度的变化也呈现出先增加后降低的趋势,但在不同鳍片间距下,该指标达到最大值时所对应的鳍片宽度逐渐增加.当两个指标达到最大值时,所对应的鳍片间距均为最小值,因此,在选取鳍片管结构参数时,应根据单位质量鳍片管换热量与引风单位耗功所回收热量两个指标并兼顾制造工艺与热量回收区域的积灰状况进行选取.

  5. Experimental study on enhancing convective heat transfer at outer asymmetrical finned tubes%非对称翅片管式换热器管外对流传热强化实验研究

    Institute of Scientific and Technical Information of China (English)

    王云雷; 何光艳; 张保生

    2015-01-01

    提出一种新型非对称翅片管式换热器,通过不同工况的实验,研究其传热过程和传热效果,并通过计算传热系数比较其与环状翅片管管束和光管管束的传热性能。结果表明:非对称翅片管对流体的扰动强于环状翅片管和光管;相同参数条件下,非对称翅片管换热器的换热效果优于环状翅片管和光管式换热器;采取相同面积的换热面,非对称翅片管换热器比环状翅片管换热器更加紧凑。%A new kind of asymmetrical finned tube heat exchanger was designed.The heat transfer process and effect of the asymmetrical finned tube were experimentally studied under four working conditions.Mo-reover,its heat transfer performance was compared with that of the ring-fin tube and smooth tube,through the heat transfer coefficient calculation.The results show that,this asymmetrical finned tube does stronger disturbance to the flow than the ring-fin tube and smooth tube,it has better heat transfer effect than the other two tubes,and with the same heating surface area,it is more compact than the ring-fin tube.

  6. Numerical Study on Hydrodynamic Performance of Bionic Caudal Fin

    Directory of Open Access Journals (Sweden)

    Kai Zhou

    2016-01-01

    Full Text Available In this work, numerical simulations are conducted to reveal the hydrodynamic mechanism of caudal fin propulsion. In the modeling of a bionic caudal fin, a universal kinematics model with three degrees of freedom is adopted and the flexible deformation in the spanwise direction is considered. Navier-Stokes equations are used to solve the unsteady fluid flow and dynamic mesh method is applied to track the locomotion. The force coefficients, torque coefficient, and flow field characteristics are extracted and analyzed. Then the thrust efficiency is calculated. In order to verify validity and feasibility of the algorithm, hydrodynamic performance of flapping foil is analyzed. The present results of flapping foil compare well with those in experimental researches. After that, the influences of amplitude of angle of attack, amplitude of heave motion, Strouhal number, and spanwise flexibility are analyzed. The results show that, the performance can be improved by adjusting the motion and flexibility parameters. The spanwise flexibility of caudal fin can increase thrust force with high propulsive efficiency.

  7. Thermal behavior of crimped spiral fin tube bank under dehumidifying process: A case study of inline arrangement

    Directory of Open Access Journals (Sweden)

    Atipoang Nuntaphan

    2004-05-01

    Full Text Available Cross flow heat exchangers having crimped spiral fin and inline arrangement configurations under dehumidification are studied. The effect of tube diameter, fin spacing, fin height, transverse tube pitch are examined. From the experiment, it is found that the heat transfer and the frictional characteristics of the heat exchanger under dehumidification is close to that of the non-dehumidifying process. However, the air stream pressure drop and the heat transfer coefficient of the wet surface heat exchanger are higher and lower than those of the dry surface respectively. Moreover, equations are developed for predicting the f and the j factors of a tested heat exchanger. Results from the developed equations agree well with the experimental data.

  8. Numerical modelling and analysing of conjugate radiation- convective heat transfer of fin-tube radiator of spacecraft

    Science.gov (United States)

    Delcov, A.; Hodenkov, A.; Zhuikov, D.

    2015-10-01

    This paper covered the problem of assessing the effectiveness of the section of the fin-tube radiator of space thermal control system. The task of calculating the conjugate radiation-convective heat transfer is presented. The results of numerical simulation are described.

  9. Comparison of fin-and-tube interlaced and face split evaporators with flow mal-distribution and compensation

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Elmegaard, Brian; Larsen, L.F.S.

    2011-01-01

    Flow mal-distribution in fin-and tube evaporators for residential air-conditioning is investigated by numerical simulation. In particularly, the interlaced and the face split evaporator are compared in flow maldistribution conditions. The considered sources of mal-distribution are: Liquid...

  10. Experiments on Void Fraction of CO2 Flow Boiling in a Horizontal Micro-fin Tube

    Science.gov (United States)

    Kondou, Chieko; Higashiiue, Shinya; Kuwahara, Ken; Koyama, Shigeru

    This paper deals with an experimental investigation on the void fraction of CO2 flow boiling in a horizontal micro-fin tube. The mean void fraction in the insulated 400 mm length sampling section, which is located next to the test evaporator, has measured by the quick closing valve method. The experimental data have been obtained in mass flux range of 200 to 455 kg/(m2s) and the refrigerant pressure range of 3.5 to 5.0 MPa. It is confirmed that the relation between void fraction and quality is affected by both mass flux and pressure. The experimental results are also compared with two previous correlations for horizontal smooth tubes, which are proposed by Butterworth and Smith. The present data satisfactorily agreed with Butterworth's correlation in the range of quality from 0.03 to 0.99. However, Smith's correlation is found to predict slightly higher than present data. As a trial, the empirical correlation of void fraction, based on the experimental slip ratios, is proposed.

  11. 翅化比对扁管翅片管性能的影响%Effect on Flat-fin Tube′s Performance of Finned Ratio

    Institute of Scientific and Technical Information of China (English)

    卢芳; 苗刚; 张向南; 常春梅; 邹建东; 张彦军

    2015-01-01

    利用CFD进行数值模拟、分析和研究,求解不同翅化比对扁管翅片管换热系数、空气侧压降的影响,确定不同翅化比下扁管翅片管的性能。换热系数模拟结果与试验数据误差为5%~15%,空气侧压降模拟结果与试验数据误差为5%~18%,证明该模拟方法的正确性。经分析求得当翅化比β为13.36~14.83时,翅片管的性能达到较为理想状态,其空气侧压降为68.87~67.58 Pa,换热系数为28.46~27.67 W/( m2· K)。%In order to determine the performance of the flat-fin tube, the heat transfer coefficient, the pressure drop of air side under diffient finned ratio with CFD were solved.The error of heat transfer coeffi-cient and pressure drop of air side between simulation results and experimental data ranges are 5%~15%and 5%~18%,which prove the feasibility of the simulation method.The performance of the flat-fin tube achieves ideal state when the finned ratio are between 13.36~14.83,the pressure drop of air side are 68.87~67.58 Pa,the heat transfer coefficient are 28.46~27.67 W/(m2· K).

  12. Formation mechanism of external finned tubes by extrusion-plough method

    Institute of Scientific and Technical Information of China (English)

    TANG Yong; LU Long-sheng; PAN Min-qing; LIU Xiao-kang; LIU Xiao-qing

    2006-01-01

    The formation mechanism of bulge on the work's surface during the extrusion process was analyzed. The bulge's size and the reasons for abscission were studied. The results show that the abscission of bulge from works is resulted from the integrated actions of pressure and friction between the plough tool and works. During the extrusion-plough process, it is noticed that four kinds of fins are appeared, which are gestation fin, multi-dimensional fin, tumor and overlap fin, when using different machining parameters. And multi-dimensional fin which has high heat transmission efficiency is a kind of complicated fin with cockscomb-like 3D substructure fin on the tip of 3D macrostructure fin. Based on the studies of those four kinds of fins, the conditions of their formation are concluded, as well as the formation mechanism is obtained.

  13. Heat-Transfer and Friction Measurements with Variable Properties for Airflow Normal to Finned and Unfinned Tube Banks

    Science.gov (United States)

    Ragsdale, Robert G.

    1958-01-01

    A single-line correlation of both the heat-transfer and pressure- drop data for electrically heated unfinned tubes is obtained by evaluating the density in the Reynolds number, specific heat, thermal conductivity, and viscosity at the film temperature, and the density in the friction coefficient at the bulk temperature. The heat-transfer data for finned tubes also exhibit an effect of physical-property variation which is removed by evaluating all properties, including density, at the primary surface temperature, and using k* = 0.015 square root of T/530 for the thermal conductivity of air where T is the absolute temperature. The pressure drop for finned tubes is correlated by the use of bulk density in both the Reynolds number and friction coefficient. The data reported are for Reynolds numbers from 2000 to 35,000, surface temperatures from 600 to 1400 R, and an air inlet temperature of 530 R.

  14. Heat transfer and flow characteristics of fin-tube bundles with and without winglet-type vortex generators

    Energy Technology Data Exchange (ETDEWEB)

    Kwak, K.M.; Torii, K.; Nishino, K. [Department of Mechanical Engineering, Yokohama National University, 79-5 Tokiwadai, Hodogaya-ku, Yokohama, 240-8501 (Japan)

    2002-11-01

    The objective of this research is to investigate the effect of longitudinal vortices that can be applied to the heat transfer enhancement for fin-tube heat exchangers such as air-cooled condensers. A multichannel test core was designed and fabricated for the determination of overall heat transfer and pressure loss with circular tubes and winglet vortex generators. Heat transfer results were obtained using a transient method referred to as the modified single-blow method. For a three-row tube bundle in an in-line arrangement without winglets, the heat transfer and the pressure loss were 72% and 210% higher, respectively, than for a multichannel test core without any built-in tube or winglet. These increases were caused by vortices around the tube banks. The corresponding increases for a staggered tube bundle are 95% and 310%, respectively. The triangular winglets recommended by the previous studies in a fin-tube bundle in an in-line arrangement increase the overall heat transfer 10-25% and the pressure loss 20-35% for the Reynolds numbers ranging from 300 to 2700. (orig.)

  15. The Influence of the Punched Delta Wings on Flow Pattern and Heat Transfer Characteristic in a Fin-and-Oval-Tube Heat Exchanger

    Directory of Open Access Journals (Sweden)

    Amnart Boonloi

    2015-01-01

    Full Text Available 3D numerical investigations are performed to study the heat transfer, friction factor, and thermal performance of a fin-and-oval heat exchanger with punched delta wings for a range of 500 ≤ Re ≤ 2500 (based on the hydraulic diameter. The influences of the punched angles, 20°, 30°, and 45°, flow directions, wing tips pointing downstream and upstream, and pitch ratios, 2, 3, 4, 5, and 6, are investigated. The results show that the use of the punched delta wings in the fin-and-oval-tube heat exchanger leads to an enhancement in the heat transfer and friction loss as compared to the plain fin for all cases (Nu/Nu0 and f/f0 higher than 1. The enhancements of the heat transfer and friction factor are around 1.01–1.22 and 1.37–2.65 times higher than the base case, respectively. The punched delta wings create the vortex flows through the test section that helps enhance the strength of the impinging flow on the tube walls. The impingement of the fluid flow is an important key to augment the heat transfer rate and thermal performance in the heat exchanger.

  16. Numerical estimation of heat transfer characteristics for two-row plate-finned tube heat exchangers with experimental data

    Science.gov (United States)

    Chen, Han-Taw; Lu, Chih-Han; Huang, Yao-Sheng; Liu, Kuo-Chi

    2016-05-01

    This study applies a three-dimensional computational fluid dynamics commercial software in conjunction with various flow models to estimate the heat transfer and fluid flow characteristics of the two-row plate-finned tube heat exchanger in staggered arrangement. The effect of air speed and fin spacing on the results obtained is investigated. Temperature and velocity distributions of air between the two fins and heat transfer coefficient on the fins are determined using the laminar flow and RNG k-ɛ turbulence models. More accurate results can be obtained, if the heat transfer coefficient obtained is close to the inverse results and matches existing correlations. Furthermore, the fin temperature measured at the selected locations also coincides with the experimental temperature data. The results obtained using the RNG k-ɛ turbulence model are more accurate than those using the laminar flow model. An interesting finding is the number of grid points may also need to change with fin spacing and air speed.

  17. EXPERIMENTAL STUDY ON ENHANCED HEAT TRANSFER WITH NI-BASED IMPLANTED SPIRAL FINNED TUBES

    Institute of Scientific and Technical Information of China (English)

    Sun Feng-zhong; Huang Xin-yuan; Wang Nai-hua; Shi Yue-tao; Ping Ya-ming

    2003-01-01

    The new type of heat exchanger elements-Ni-based Implanted Spiral Finned Turbes (NISFT) was studied and tested, which can contribute to increase the efficiency and reliability. The relation of Nu, Eu and Re with different fin pitch, fin height, transverse pitch and longitudinal pitch were gained, which constituted the basic foundation for the engineering application of NISFT.

  18. Studi Eksperimen Analisa Performa Compact Heat Exchanger Circular Tubes Continuous Plate Fin Untuk Pemanfaatan Waste Energy

    Directory of Open Access Journals (Sweden)

    Rachmadi Gewa Saputra

    2014-03-01

    Full Text Available Harga minyak dunia cenderung mengalami peningkatan dalam beberapa tahun terakhir sehingga manusia berfikir untuk memanfaatkan setiap penggunaan minyak bumi. Dengan berkembangnya teknologi saat ini waste energy yang berupa gas hasil pembakaran pada engine dapat dimanfaatkan menjadi bentuk energi lain menggunakan heat recovery system. Pada tugas akhir ini dilakukan desain sebuah heat exchanger tipe circular tubes continuous plate fin dengan susunan tube aligned yang digunakan untuk menyerap waste energy yang berupa exhaust gas. Untuk mendapatkan dimensi desain yang sesuai digunakan metode ΔTLMTD. Metode ini digunakan untuk menentukan nilai dari overall heat transfer  desain dari heat exchanger, kemudian dilakukan perhitungan untuk nilai overall heat transfer hitung. Setelah didapatkan nilai dari overall heat transfer secara desain dan hitung maka dilakukan iterasi untuk mendapatkan dimensi heat exchanger yang memiliki nilai error paling kecil antara nilai overall heat transfer desain dan hitung. Untuk pengujian performa dari heat exchanger yang telah didesain maka dilakukan variasi kacepatan exhaust gas yang melewati heat exchanger, yaitu 0.4 m/s, 0.3 m/s, dan 0.2 m/s. Exhaust gas yang digunakan memiliki temperatur 280oC. Pada tugas akhir ini didapatkan desain compact heat exchanger dengan dimensi panjang 0.38 m, lebar 0.45 m, dan tebal 0.04m. Setelah dilakukan pengujian dengan memvariasikan kecepatan dari exhaust gas yang melewati heat exchanger maka didapatkan bahwa nilai dari qaktual dari heat exchanger mengalami kenaikan dengan bertambahnya reynolds number akibat bertambahnya kecepatan exhaust gas, kemudian nilai dari effectiveness akan mengalami penurunan untuk setiap kenaikan dari reynold number exhaust gas. Selain itu nilai dari NTU heat exchanger juga mengalami penurunan dengan bertambahnya reynold number exhaust gas. Untuk nilai overall heat transfer dari heat exchanger yang didesain akan mengalami kenaikan akibat bertambahnya nilai

  19. 温度交变对翅片管换热器性能影响的实验研究%Experimental Study on Influence of Temperature Alternating by Turns on Tube-fin Heat Exchanger

    Institute of Scientific and Technical Information of China (English)

    胡兵; 赵宇; 王勤韧; 陈江平

    2011-01-01

    The effects of temperature alternating by turns on the total heat transfer coefficient and pressure drop performance of finned coil type evaporators used in bus are studied by experiments on a copper fin evaporator and an aluminum fin evaporator. The results show that the pressure drop of the new copper fin evaporator is larger than that of the new aluminum fin evaporator, but after temperature alternating by turns the long-term pressure drop properties of copper fin evaporator are almost identical with that of aluminum fin evaporator. Temperature alternating by turns will lead to heat transfer performance degradation for tube-fin evaporator, and heat transfer performance reduce most aluminum fin evaporator reduce 1091.5W while copper fin evaporator reduce 704.8W, when the air volume is 400m3/h. Comparing with the new fin-tube evaporators, the total heat transfer coefficient of heat exchanger decreased by 8.1%~25.2% after temperature alternating for copper fin evaporator while by 10.6%~40.7% for aluminum fin evaporator. Copper fin evaporator has better long-term characteristics than aluminum fin evaporator.%试验研究了温度交变对铜管-铜翅片蒸发器和铜管-铝翅片蒸发器空气侧压降和换热性能的影响.实验结果表明,全新铜管-铜翅片蒸发器空气侧压降比全新铜管-铝翅片蒸发器空气侧压降大,但温度交变后两者空气侧压降几乎一致,具有相同的长效压降特性;温度交变会导致铜管-铜翅片蒸发器和铜管-铝翅片蒸发器换热性能下降,在风量为400m3/h时减少的最多,铝翅片蒸发器减少1091.5W,铜翅片蒸发器减少704.8W;与温度交变前相比,铜翅片蒸发器换热系数下降8.1%~25.2%,铝翅片蒸发器换热系数下降10.6%~40.7%,铜管-铜翅片蒸发器具有更好的长效特性.

  20. Experimental study on thermal performance of micro pin fin heat sinks with various shapes

    Science.gov (United States)

    Hua, Junye; Li, Gui; Zhao, Xiaobao; Li, Qihe

    2017-03-01

    This paper presents a visualization experimental study on the heat transfer characteristics of various shapes of micro pin fins, including the circular, ellipse, diamond, square and triangle shape micro pin fin arrays with various equivalent diameters and pin fin density. The influences study of different sizes and shapes of pin fin on Nusselt number and heat transfer coefficient have been conducted. The results show that with the increase of the flow rate, the temperature of the bottom of the experimental section decreases. And the Nusselt number of different shapes of micro pin fins increases with the increase of Re. In which, the heat transfer performance of the ellipse shape pin fin appears better among the other shapes of pin fins. However, the higher pin fin of the ellipse shape density leads to a weaker flow performance. Besides, the micro-scale heat transfer correlation between the Nusselt number and the Reynolds number is fitted based on the experimental data.

  1. Experimental Study on Heat Transfer and Pressure Drop Characteristics of Four Types of Plate Fin-and-Tube Heat Exchanger Surfaces

    Institute of Scientific and Technical Information of China (English)

    1994-01-01

    In this paper,air side heat transfer and pressure drop characteristics of twelve three-row plate fin-and-tube heat exchanger cores of four types of fin configurations have been experimentally investigated .The heat transfer and friction factor correlations for the twelve cores are provided in a wide range of Reynolds number.It is found that in the range of Reynolds number tested.the Nusselt number of the slotted fin surface is the largest and that of the plain plate fin is the lowest while the Nusselt numbers of two types of wavy fins are somewhere in between.

  2. Effect of Longitudinal-External-Fins on Fluid Flow Characteristics for Wing-Shaped Tubes Bundle in Crossflow

    Directory of Open Access Journals (Sweden)

    Sayed Ahmed E. Sayed Ahmed

    2015-01-01

    Full Text Available A numerical study is conducted to clarify fluid-flow characteristics, pressure drop coefficient (Pdc, and the average skin friction coefficient (Cf,m for wing-shaped-tubes bundle with longitudinal fins at downstream side of the tube using the commercial CFD FLUENT software package. The air-side Rea ranges from 1800 to 9700. The tubes are employed with various fin heights (hf and fin thicknesses (δ such as 2 mm ≤ hf ≤ 12 mm and 1.5 mm ≤ δ ≤ 3.5 mm at the considered Rea range. Results indicate that ΔPa increases with Rea for all hf. Pdc decreases with Rea for all hf values for 1800 ≤ Rea ≤ 4200 and then increases for 4200 ≤ Rea ≤ 10000. Lowest values of ΔPa, Pdc, and pumping power (PP occurred at hf = 6 mm. Values of Pdc for hf = 6 mm are lower than those of NOF and hf = 2 mm by about 73 % and 32 %, respectively, at Rea = 4000. Cf,m decreases with Rea. δ has negligible effect on Cf,m. ΔPa increases for 1.5 mm ≤ δ ≤ 2.5 mm while ΔPa decreases with 2.5 mm < δ ≤ 3.5 mm for the considered Rea range except for Rea = 1850.

  3. 低翅片管换热过程的数值模拟及其结果分析%Numerical simulation of heat transfer process for low finned tube and its result analysis

    Institute of Scientific and Technical Information of China (English)

    钟建华; 唐治立; 林师朋; 刘艳霞; 袁志燕

    2014-01-01

    以用于冷凝器中的低翅片管为研究对象,利用ANSYS中的流体传热分析模块FLOTRAN CFD,建立管内通R22制冷剂,管外通空气的翅片管换热过程的二维模型,并对其进行流固耦合模拟分析。研究采用正交实验的方法,探究了换热过程中流场与温度场的分布状况,并结合传热学、流体学理论对结果进行了分析,研究表明:在等热流的情况下,翅片管的换热性能明显优于光管,在指定范围内,翅片管换热性能随翅片间距的增加而增强,随翅片厚度的增大而减弱,随翅片高度的增大而增强,但管外压降却随翅高的增大而显著变大,综合考虑换热性能与压降,对翅片管的结构参数进行了优化。%With the low finned tubes used in the condenser as the research object , the two-dimensional model with the refrigerant (R22) flow in tube and the air flow outside tube is established by using the fluid heat transfer analysis module of ANSYS FLOTRAN CFD, and its fluid-structure interaction simulation is analyzed. Orthogonal experiments are performed to study the distribution of the flow field and temperature field for the heat transfer process. The following conclusions are drawn from the analysis with the heat transfer theory and fluerics theory:the heat transfer performance of finned tube is significantly better than that of the light pipe with the same heat flux;the heat transfer performance of finned tube is enhanced with the increase of the fin spacing and fin height and weakened with the increase of fin thickness within the specified range;but the pressure drop outside the tube is significantly weakened with the increase of fin height. The structure parameters of finned tube can be optimized with the overall consideration of the heat transfer performance and pressure drop.

  4. Geometrical optimization and mould wear effect on HPD type steel offset strip fin performance

    Energy Technology Data Exchange (ETDEWEB)

    Lihua, Guo; Jiangping, Chen; Feng, Qin; Zhijiu, Chen [Institute of Refrigeration and Cryogenics Engineering, Shanghai Jiao Tong University, 1954 Huashan Road, Shanghai 200030 (China)

    2007-09-15

    Aiming at studying the influence and importance of the geometrical parameters on steel HPD type offset strip fin performance, this paper reports experimental and numerical studies at low Reynolds number. A novel test rig with electrically heated single layer fin assembly as test object was constructed. Only the effects of fin height and fin wavelength on the fin characteristics were considered because of the pressing mould limitation. Through comparisons of experimental, simulated and Muzychka's results, the tendencies agree well. The deviations between them are due to the difference of fin material and the influences of the pressing mould process technique on the fins. Based on the Taguchi method and uniform design, the importance of the geometrical factors on the fin thermal-hydraulic performance was investigated. The sequence of degrees of effect for each parameter is s, h, {alpha}, s{sub 0}, b and t. The paper obtained the optimum model and numerically proved its validity among the considered ranges. Eleven sample fins were collected during different periods of the mould life time, and the influences of mould wear on fin friction performance were examined. The mould wear includes three stages, and the performance of fins pressed during 100 thousand times to 1,050 thousand times is more stable. The recommended life time for the mould type is about 1,050 thousand times. (author)

  5. Steam generator tubing NDE performance

    Energy Technology Data Exchange (ETDEWEB)

    Henry, G. [Electric Power Research Institute, Charlotte, NC (United States); Welty, C.S. Jr. [Electric Power Research Institute, Palo Alto, CA (United States)

    1997-02-01

    Steam generator (SG) non-destructive examination (NDE) is a fundamental element in the broader SG in-service inspection (ISI) process, a cornerstone in the management of PWR steam generators. Based on objective performance measures (tube leak forced outages and SG-related capacity factor loss), ISI performance has shown a continually improving trend over the years. Performance of the NDE element is a function of the fundamental capability of the technique, and the ability of the analysis portion of the process in field implementation of the technique. The technology continues to improve in several areas, e.g. system sensitivity, data collection rates, probe/coil design, and data analysis software. With these improvements comes the attendant requirement for qualification of the technique on the damage form(s) to which it will be applied, and for training and qualification of the data analysis element of the ISI process on the field implementation of the technique. The introduction of data transfer via fiber optic line allows for remote data acquisition and analysis, thus improving the efficiency of analysis for a limited pool of data analysts. This paper provides an overview of the current status of SG NDE, and identifies several important issues to be addressed.

  6. Experimental Study on Flow Boiling of CO2 and CO2-PAG Oil Mixture in Smooth and Micro-fin Tubes

    Science.gov (United States)

    Koyama, Shigeru; Ito, Daisuke; Lee, Sang-Mu; Kuwahara, Ken; Saeki, Chikara

    In this study, experiments on the flow boiling of nearly pure CO2 and CO2-PAG oil mixture are carried out using a 2.064 m long double-pipe counter-flow heat exchanger, in which the refrigerant flows inside the inner tube and the heat source water flows counter-currently in the outer annulus. A smooth copper tube and a micro-fin copper tube are used as the inner tube. In case of nearly pure CO2, the present experimental results of heat transfer coefficient in smooth tube with rough surface agree well with the predicted results using Yu et al. correlation [5], in which the surface roughness effect is taken into account. It is also confirmed that the values of heat transfer coefficient for both smooth and micro-fin tubes are almost analogous, while the values of pressure drop for micro-fin tube are slightly higher than those of smooth tube. By comparing the experimental results between nearly pure CO2 and CO2-oil mixture, it is confirmed that the oil concentration effects on heat transfer coefficient and pressure drop in micro-fin tube have different characteristics from those of smooth tube.

  7. 翅片结构对双向开缝翅片管换热器性能的影响%Effects of fin structure on heat transfer and resistance characteristics of super slit finned tube heat exchangers

    Institute of Scientific and Technical Information of China (English)

    屠琦琅; 袁益超; 胡晓红

    2016-01-01

    To understand the effect of fin structure on heat transfer and resistance, numerical simulation and validation experiments were performed on super slit finned tube heat exchangers with different fin pitchesPf and slit heightsSh. WhenRewas less than 7200, heat transfer and resistance performance was improved withPf increase. WhenRewas greater than 7200, heat transfer was improved but resistance was declined withPf decrease. In case ofSh increase, heat transfer declined first and enhanced later, whereas resistance showed an opposite trend. With regard to five super slit finned tube heat exchangers with different fin structures, the comprehensive flow and heat transfer performance were improved while the actual heat transfer area was decreased withPf increase, which a consideration of all factors should be required. A good agreement was observed between the numerical simulation and experimental results whenRe was in the range of 2734—6712, indicating that the numerical simulation method could predict the heat transfer and resistance characteristics of super slit finned tube heat exchangers. These results would set a basis for optimization between structure and performance of these heat exchangers.%为了获得翅片结构对双向开缝翅片管换热器传热与阻力性能的影响规律,对不同翅片间距Pf和开缝高度Sh的双向开缝翅片管换热器进行了数值模拟,并对数值模拟结果进行了模化试验验证。结果表明:当Re7200时,减小Pf会提高其传热性能,降低其阻力性能;随着Sh的增加,双向开缝翅片管换热器的传热性能先降低后提高,阻力性能先提高后降低;对于不同翅片结构的5种双向开缝翅片管换热器,Pf越大,综合流动传热性能越高,但实际换热面积会减小,需综合考虑;在Re=2734~6712范围内数值模拟与试验结果吻合较好,数值模拟能较准确地反映双向开缝翅片管换热器的传热与阻力特性。研究成

  8. Thermal performance of functionally graded parabolic annular fins having constant weight

    Energy Technology Data Exchange (ETDEWEB)

    Gaba, Vivek Kumar; Tiwari, Anil Kumar; Bhowmick, Shubhankar [National Institute of Technology Raipur, Raipur (India)

    2014-10-15

    The proposed work reports the performance of parabolic annular fins of constant weight made of functionally graded materials. The work involves computation of temperature gradient, efficiency and effectiveness of such fins and compares the performances for different functionally graded parabolic fin profiles obtained by varying grading parameters and profile parameters respectively keeping the weight of the fins constant. The functional grading of thermal conductivity is based on a power function of radial co-ordinate which consists of parameters, namely grading parameters, varying which different grading combinations are studied. A general second order ordinary differential equation has been derived for all the profiles and material grading. The efficiency and effectiveness of the annular fins of different profile and grading combinations have been calculated and plotted and the results reveal the dependence of fin performance on profile and grading parameter.

  9. Simulation on Thermal Integrity of the Fin/Tube Brazed Joint of Heat Exchangers

    Institute of Scientific and Technical Information of China (English)

    Yiyu QIAN; Feng GAO; Fengjiang WANG; Hui ZHAO

    2003-01-01

    In the applications of heat exchangers, the fin efficiency of heat transfer is the key issue. Thermal distribution withinthe brazed joints in heat exchanger under loading conditions is investigated in this paper. Simulated results showedthat the therma

  10. Study on Heat Transfer Computation and Industrial Application of Longitudinal Finned Tube%纵向翅片管传热计算研究与工业应用

    Institute of Scientific and Technical Information of China (English)

    李大树; 仇性启; 赵天宇; 祁风雷

    2011-01-01

    主要研究了纵向翅片管的传热计算流程及工程应用.根据纵向翅片管的基本传热机理,系统深入地总结了纵向翅片管在不同传热条件下换热系数的计算方法,提出了纵向翅片管换热器的设计流程;通过具体工程实例,纵向翅片管换热器的设计理论得到验证,同时计算结果表明,与传统的光管相比,纵向翅片管传热系数高,设备传热性能好,是一种行之有效的节能途径,具有良好的应用前景.%This paper focus on heat transfer calculating procedure and application of longitudinal finned tube. Based on the radical heat-transfer mechanism of longitudinal finned tube, the method of calculate the convective heat-transfer coefficient of longitudinal finned tube under different heat transfer conditions is concluded systematically and in-depth knowledge and the design method flow of longitudinal finned tube heat exchanger is put forward. Though the design of specific project, the design theory is verified, and the results also show that the longitudinal finned tube is higher in its heat transfer coefficient compared to the traditional tube. Therefore the longitudinal finned tube heat exchanger has a higher heat transfer properly, and the application of longitudinal finned tube is an effective energy-saving way which has an extensive prospect.

  11. Flow and heat transfer in compact offset strip fin surfaces

    Institute of Scientific and Technical Information of China (English)

    Junqi DONG; Jiangping CHEN; Zhijiu CHEN

    2008-01-01

    Experimental studies of air-side heat transfer and pressure drop characteristics of offset strip fins and flat tube heat exchangers were performed. A series of tests were conducted for 9 heat exchangers with different fin space, fin height, fin strip length and flow length, at a constant tube-side water flow rate of 2.5 m3/h. The char-acteristics of the heat transfer and pressure drop of differ-ent fin space, fin height and fin length were analyzed and compared. The curves of the heat transfer coefficients vs. The pumping power per unit frontal area were then plot-ted. Moreover, the enhanced heat transfer mechanism of offset strip fins was analyzed using field synergy theory. The results showed that fin length and flow length have more obviously effect on the thermal hydraulic character-istics of offset strip fins.

  12. The Effect of Circular Finned Tube Heat Transfer Enhancement by Using Longitudinal Vortex Generators%纵向涡发生器对圆形翅片管换热强化的影响

    Institute of Scientific and Technical Information of China (English)

    于恩播; 孙铁; 张素香

    2012-01-01

    The fluid flow and heat transfer process of circular finned tube with longitudinal vortex generators(LVGs) were numerically simulated with the CFD calculation software FLUENT, then compared with the normal circular finned tube. The simulation results show that the performance of circular finned tube with longitudinal vortex generators is far better than that of the normal circular finned tube. It can be explained from the view point of field synergy principle, which says that the longitudinal vortex generators can enhance effect of heat transfer because it reduces the angle between velocity and fluid temperature gradient.%利用CFD计算软件FLUENT对带有纵向涡发生器的圆形翅片管的流体流动和传热过程进行数值模拟,并与普通圆形翅片管加以对比.结果表明,带有纵向涡发生器的翅片管换热效果明显优于普通翅片管.应用场协同原理解释认为,纵向涡发生器使流体速度和温度梯度之间夹角减小,改善了速度场和温度场的协同性,从而增强了换热效果.

  13. Thermal performance of a porus radial fin with natural convection and radiative heat losses

    Directory of Open Access Journals (Sweden)

    Darvishi M.T.

    2015-01-01

    Full Text Available An analytic (series solution is developed to describe the thermal performance of a porous radial fin with natural convection in the fluid saturating the fin and radiation heat loss from the top and bottom surfaces of the fin. The HAM results for the temperature distribution and base heat flux are compared with the direct numerical results and found to be very accurate.

  14. Investigation on the heat transfer characteristics during flow boiling of liquefied natural gas in a vertical micro-fin tube

    Science.gov (United States)

    Xu, Bin; Shi, Yumei; Chen, Dongsheng

    2014-03-01

    This paper presents an experimental investigation on the heat transfer characteristics of liquefied natural gas flow boiling in a vertical micro-fin tube. The effect of heat flux, mass flux and inlet pressure on the flow boiling heat transfer coefficients was analyzed. The Kim, Koyama, and two kinds of Wellsandt correlations with different Ftp coefficients were used to predict the flow boiling heat transfer coefficients. The predicted results showed that the Koyama correlation was the most accurate over the range of experimental conditions.

  15. A High Efficiency, Miniaturized Ka Band Traveling Wave Tube Based on a Novel Finned Ladder RF Circuit Design

    Science.gov (United States)

    Wintucky, E. G.; Wilson, J. D.; Vaden, K. R.; Force, D. A.; Freeman, J. C.; Lesny, G. G.; Kory, C. L.; Chevalier, C. T.; Ebihara, B.; Dayton, J. A.; Williams, W. D. (Technical Monitor)

    2001-01-01

    Space communications architectures are being planned to meet the high rate data distribution requirements of future NASA Enterprise missions. These will require the use of traveling wave tube amplifiers (TWTAs) to provide the high frequency, RF (radio frequency) power and efficiency needed for many of the communications links. A program addressing these requirements is currently underway at NASA Glenn Research Center (GRC) for the development of a high efficiency, 20 watt, 32 GHz TWT of reduced size and weight that is based on a novel high gain n circuit design, termed the 'finned ladder'.

  16. Heat transfer enhancement accompanying pressure-loss reduction with winglet-type vortex generators for fin-tube heat exchangers

    Energy Technology Data Exchange (ETDEWEB)

    Torii, K.; Kwak, K.M.; Nishino, K. [Yokohama National Univ. (Japan). Dept. of Mechanical Engineering

    2002-08-01

    This paper proposes a novel technique that can augment heat transfer but nevertheless can reduce pressure-loss in a fin-tube heat exchanger with circular tubes in a relatively low Reynolds number flow, by deploying delta winglet-type vortex generators. The winglets are placed with a heretofore-unused orientation for the purpose of augmentation of heat transfer. This orientation is known as ''common flow up'' configuration. The proposed configuration causes significant separation delay, reduces form drag, and removes the zone of poor heat transfer from the near-wake of the tubes. This enhancement strategy has been successfully verified by experiments in the proposed configuration. In case of staggered tube banks, the heat transfer was augmented by 30% to 10%, and yet the pressure loss was reduced by 55% to 34% for the Reynolds number (based on two times channel height) ranging from 350 to 2100, when the present winglets were added. In case of in-line tube banks, these were found to be 20% to 10% augmentation, and 15% to 8% reduction, respectively. (author)

  17. Optimization of triangular fins with/without longitudinal perforate for thermal performance enhancement

    Energy Technology Data Exchange (ETDEWEB)

    Shadlaghni, A.; Tavakoli, M. R.; Farzaneh, M.; Salimpour, M. R. [Isfahan University, Isfahan (Iran, Islamic Republic of)

    2016-04-15

    This study aimed at determining a suitable pattern to allow for a better design of the fins used in heat sinks. Flow was considered laminar and steady, and the studied heat transfer mechanism was forced convection. Considering a fixed fin volume, the shape of fin cross section and its dimensions were optimized to maximize the heat transfer rate in a given physical condition. Numerical results showed that at a constant fin base area, heat transfer rate was higher in a fin with a triangular cross section compared to the fins with rectangular or trapezoidal cross sections. Investigation of optimum dimensional ratio in triangular fins showed that an increased height/thickness ratio enhanced the heat transfer rate. The effect of vertical position of the longitudinal perforations with different cross sections but similar volume ratios on the thermal performance of triangular fins was also examined. Results showed that perforation enhanced the thermal performance of the fins. Perforations with square and circular cross sections had almost identical thermal performances and dissipated more heat compared to those with triangular perforations.

  18. 采用铜铝复合管的翅片管换热器性能试验研究%Experimental research on substitute of aluminum clad copper tube in finned tube heat exchanger

    Institute of Scientific and Technical Information of China (English)

    金听祥; 曹玉龙

    2012-01-01

    针对铜铝复合管(ACC管)在空调用翅片管换热器中替代铜管应用进行了试验研究.分别对Φ7.94mm型管的全铜管、过冷段铜铝复合管、全铜铝复合管三种换热器进行了性能比较和成本分析.研究结果表明,在风速和风量不变的情况下,过冷段铜铝复合管换热器能力为8634.22W,高于全铜铝复合管的换热器的8389.36W,低于全铜管换热器的8989.07W.制冷剂侧能力测试中,过冷段铜铝复合管换热器平均值为8.885kW,与全铜铝复合管换热器平均值8.775kW相比高1.24%,与全铜管换热器平均值9.101kW相比低2.37%,与能力测试结果基本一致.与原换热器铜管相比,在相同条件下,铜铝复合管可以降低管材成本29.5%.综上所述,过冷段采用铜铝复合管的换热器能够取代铜管换热器应用在空调中,在不影响其换热性能的基础上,降低成本效果明显.%In this paper, the aluminum clad copper tube was investigated to replace copper tube as finned tube heat exchanger. The heat transfer performance and cost of three types of finned tube heat exchangers adopting copper tube, subcooled portion with aluminum clad copper lube and all aluminum clad copper tube with φ7. 94mm diameter were compared. The experimental results show that with the same wind speed and air volume, the capacity of the heat exchanger with aluminum clad copper tube in subcooled portion in air side is 8634.22W, higher than that of the heat exchanger with all aluminum clad copper tube, and lower than that of the heat exchanger with copper tube. Meanwhile, the capacity of the heat exchanger with aluminum clad copper tube in subcooled portion in the refrigerant side is 8. 885kW, which is 1.24% higher than that of the heat exchanger with all aluminum clad copper tube and 2. 37% lower than that of the heat exchanger with copper tube. At the same conditions, the costs of a-luminum clad copper tube can be reduced 29.5% compared with copper tube. In

  19. Experimental Investigation of Heat Transfer Characteristics of Louver Fin-and-tube Heat Exchanger with 5 mm Diameter Tubes under Wet Conditions%采用窗片的5 mm管换热器在湿工况下换热性能的实验研究

    Institute of Scientific and Technical Information of China (English)

    高晶丹; 丁国良; 吴伟; 胡海涛; 高屹峰; 宋吉

    2012-01-01

      The heat transfer characteristics of fin-and-tube heat exchangers with 5 mm diameter tubes under wet conditions were investigated by experiments on 11 louver fin-and-tube heat exchangers. The effects of fin pitch and inlet relative humidity on air-side performance were analyzed. The results indicated that the effect of inlet relative humidity on the heat transfer rate is small, and heat transfer rate decreases with the increase of fin pitch, which is more obvious than that of fin-and-tube heat exchanger with 7 mm or larger diameter tubes. The water bridge was observed at the bottom of fin in experiments;however, it did not occur on the fin with 7 mm or large diameter tubes. A correlation for j factor was developed to predict the heat transfer performance of fin-and-tube heat exchanger with 5 mm diameter tubes. The deviations of the proposed j correlation are within ±20%.%  在湿工况下,对11个采用百叶窗翅片的5 mm管换热器进行了实验研究,并分析了翅片间距、进口空气相对湿度等因素对空气侧换热性能的影响。研究结果表明:换热量随翅片间距的增加而减小,且比7 mm管或更大管径换热器更明显;换热量受进口空气相对湿度的影响小;在翅片底部出现水桥,而在7 mm管或者更大管径换热器中不曾出现。根据实验数据开发了预测5 mm翅片管换热器换热性能的j因子关联式,误差在±20%以内。

  20. Performance characteristics of pulse tube refrigerators

    Science.gov (United States)

    Huang, B. J.; Tzeng, T. M.

    In the present study experiments were carried out to investigate the performance characteristics of pulse tube refrigerators. It was found that the cool-down time tc during the transient or start-up period is dominated by the time constant of the pulse tube wall τpt and that the dynamics of a basic pulse tube (BPT) refrigerator approaches that of a first-order system. For steady state operation, the cold-end temperature TL was found to vary with τpt, and the cooling load QL increases monotonically with increasing τpt. This indicates that heat pumped by the gas from the cold to the hot end increases with decreasing hpt (i.e. less energy exchange between the gas and wall). The process of heat storage or release of the pulse tube wall is thus shown to have a negative effect on the performance of a BPT refrigerator. It was thus found experimentally that the gas compression/expansion process inside the pulse tube, which is similar to a Brayton cycle but lies between isothermal and adiabatic, can explain the performance of BPT refrigerators. The present experiment also shows that the performance of a pulse tube refrigerator at transient and steady states is mainly dominated by the time constant of the pulse tube wall τpt.

  1. Statistical analysis of entropy generation in longitudinally finned tube heat exchanger with shell side nanofluid by a single phase approach

    Science.gov (United States)

    Konchada, Pavan Kumar; Pv, Vinay; Bhemuni, Varaprasad

    2016-06-01

    The presence of nanoparticles in heat exchangers ascertained increment in heat transfer. The present work focuses on heat transfer in a longitudinal finned tube heat exchanger. Experimentation is done on longitudinal finned tube heat exchanger with pure water as working fluid and the outcome is compared numerically using computational fluid dynamics (CFD) package based on finite volume method for different flow rates. Further 0.8% volume fraction of aluminum oxide (Al2O3) nanofluid is considered on shell side. The simulated nanofluid analysis has been carried out using single phase approach in CFD by updating the user-defined functions and expressions with thermophysical properties of the selected nanofluid. These results are thereafter compared against the results obtained for pure water as shell side fluid. Entropy generated due to heat transfer and fluid flow is calculated for the nanofluid. Analysis of entropy generation is carried out using the Taguchi technique. Analysis of variance (ANOVA) results show that the inlet temperature on shell side has more pronounced effect on entropy generation.

  2. Indoor solar thermal energy saving time with phase change material in a horizontal shell and finned-tube heat exchanger.

    Science.gov (United States)

    Paria, S; Sarhan, A A D; Goodarzi, M S; Baradaran, S; Rahmanian, B; Yarmand, H; Alavi, M A; Kazi, S N; Metselaar, H S C

    2015-01-01

    An experimental as well as numerical investigation was conducted on the melting/solidification processes of a stationary phase change material (PCM) in a shell around a finned-tube heat exchanger system. The PCM was stored in the horizontal annular space between a shell and finned-tube where distilled water was employed as the heat transfer fluid (HTF). The focus of this study was on the behavior of PCM for storage (charging or melting) and removal (discharging or solidification), as well as the effect of flow rate on the charged and discharged solar thermal energy. The impact of the Reynolds number was determined and the results were compared with each other to reveal the changes in amount of stored thermal energy with the variation of heat transfer fluid flow rates. The results showed that, by increasing the Reynolds number from 1000 to 2000, the total melting time decreases by 58%. The process of solidification also will speed up with increasing Reynolds number in the discharging process. The results also indicated that the fluctuation of gradient temperature decreased and became smooth with increasing Reynolds number. As a result, by increasing the Reynolds number in the charging process, the theoretical efficiency rises.

  3. Indoor Solar Thermal Energy Saving Time with Phase Change Material in a Horizontal Shell and Finned-Tube Heat Exchanger

    Directory of Open Access Journals (Sweden)

    S. Paria

    2015-01-01

    Full Text Available An experimental as well as numerical investigation was conducted on the melting/solidification processes of a stationary phase change material (PCM in a shell around a finned-tube heat exchanger system. The PCM was stored in the horizontal annular space between a shell and finned-tube where distilled water was employed as the heat transfer fluid (HTF. The focus of this study was on the behavior of PCM for storage (charging or melting and removal (discharging or solidification, as well as the effect of flow rate on the charged and discharged solar thermal energy. The impact of the Reynolds number was determined and the results were compared with each other to reveal the changes in amount of stored thermal energy with the variation of heat transfer fluid flow rates. The results showed that, by increasing the Reynolds number from 1000 to 2000, the total melting time decreases by 58%. The process of solidification also will speed up with increasing Reynolds number in the discharging process. The results also indicated that the fluctuation of gradient temperature decreased and became smooth with increasing Reynolds number. As a result, by increasing the Reynolds number in the charging process, the theoretical efficiency rises.

  4. Statistical analysis of entropy generation in longitudinally finned tube heat exchanger with shell side nanofluid by a single phase approach

    Directory of Open Access Journals (Sweden)

    Konchada Pavan Kumar

    2016-06-01

    Full Text Available The presence of nanoparticles in heat exchangers ascertained increment in heat transfer. The present work focuses on heat transfer in a longitudinal finned tube heat exchanger. Experimentation is done on longitudinal finned tube heat exchanger with pure water as working fluid and the outcome is compared numerically using computational fluid dynamics (CFD package based on finite volume method for different flow rates. Further 0.8% volume fraction of aluminum oxide (Al2O3 nanofluid is considered on shell side. The simulated nanofluid analysis has been carried out using single phase approach in CFD by updating the user-defined functions and expressions with thermophysical properties of the selected nanofluid. These results are thereafter compared against the results obtained for pure water as shell side fluid. Entropy generated due to heat transfer and fluid flow is calculated for the nanofluid. Analysis of entropy generation is carried out using the Taguchi technique. Analysis of variance (ANOVA results show that the inlet temperature on shell side has more pronounced effect on entropy generation.

  5. Investigation of heat transfer characteristics of finned tubes in an air cooler; Kuki reikyakuki no dennetsu tokusei ni kansuru kenkyu

    Energy Technology Data Exchange (ETDEWEB)

    Akiyoshi, R.; Hori, M.; Ishida, H.; Hagiwara, K. [Ishikawajima-Harima Heavy Industries Co. Ltd., Tokyo (Japan)

    1997-03-01

    Heat transfer characteristics of a multitubular heat exchanger are investigated for the purpose of continuously cooling air below 0{degree}C. The air duct used in the test is rectangular, 302mm in width and 322mm in height, made of an acrylic resin so that the frosted part may be seen by the eyes and that transmission of heat from the duct into the air may be suppressed. The heat transfer tube is a horizontal tube provided with fins. The refrigerant is a brine kept at a specified temperature, supplied to the most downstream row of the heat transfer tube to run in series so that it will flow contrary to the air. Under the conditions where the steam in the air does not condense, the heat transmission rate increases along with the air speed, quantatively agreeing with what has been obtained in the past. Under the conditions where the steam in the air condenses, the heat transmission rate is two times higher than the rate in the case of no condensation when the air speed is low and, when the air speed is high, approximately equal to the rate in the case of no condensation. Between the two, there is a domain where the heat transmission rate decreases with an increase in the air speed. Spraying the brine on the heat transfer tube prevents frosting even when the heat transfer surface temperature is 0{degree}C or lower, letting heat through. 9 refs., 6 figs.

  6. R290空调小管径翅片管换热器的设计方法%Design Method of Fin-and-tube Heat Exchanger with Smaller Diameter Tubes in R290 Air Conditioner

    Institute of Scientific and Technical Information of China (English)

    2012-01-01

    R290 is a potential alternative refrigerant for R22, however using R290 may result in the risk of firing. Promoting the use of smaller diameter tubes in R290 room air conditioner is an effective way to reduce refrigerant charge to avoid the risk of firing, but may cause reduction of air conditioner system performance, so it is needed to propose a design method of heat exchanger with smaller diameter tubes. The method of designing fin-and-tube heat exchanger with smaller tubes is proposed in this study. The method includes designing of fin configuration and designing of refrigerant circuits. In the design method, the fin configuration is designed by CFD-based method, and the refrigerant circuits are designed by distributed-parameter model based on graph theory. An evaporator of 5 mm diameter tubes was designed, and the performance of an air conditioner with the designed evaporator was tested to verify the rationality of design method.%  R290是R22潜在的优良替代制冷剂,但有高可燃性的缺点。采用小管径换热器可有效降低制冷剂充注量,保证R290空调使用安全,但小管径的采用可能会导致空调换热性能下降,因此,有必要提出小管径换热器的设计方法。本文提出了空调小管径换热器的设计方法,包括翅片结构设计和制冷剂流路设计。在设计方法中,采用基于CFD的方法设计翅片结构,采用基于图论的三维分布参数模型设计制冷剂流路。为验证设计方法的合理性,根据设计方法设计了5mm管蒸发器,并对采用5mm管蒸发器的空调整机进行了测试。

  7. Research on Structural Optimi zation fo Flat-tube Fins of an Ai r-cooler%扁管空冷器翅片结构优化研究

    Institute of Scientific and Technical Information of China (English)

    杜弘; 杨鹏; 张升平

    2013-01-01

    基于带翅片的扁管空冷器的传热过程,对带翅片的扁管建立模型,并利用该模型在不同的翅片长度及不同风速下进行数值模拟,分析了翅片长度的选择与迎面风速的关系。分析结果表明,当翅片长度增加到一定值后,通过增加翅片长度的手段来强化换热性能收效很小;在低迎面风速下,翅片长度不要过长;在高迎面风速下,仍存在较大的传热温差,空气出口温度的增加只能通过增加翅片长度来完成。%The relationship between the length of the fin and the windward velocity is analyzed , the model of the flat tube with fins is established and a numeric simulation study is made under the condition of different fin lengths and different wind speeds according to the heat transfer of theair -cooler with finned flat-tubes.Results show that, to strengthen heat transfer perform-ance by increasing the fin length can only lead to alittle benefit when the fin length increases to a certain value.The fin length shouldn′t be too long under lower wind speed.Under higher windspeed , there is still a heat ransfer temperature difference, however , the outlet air temperature rises only by increasing the finlength .

  8. Performance analysis of pin fins with temperature dependent thermal parameters using the variation of parameters method

    Directory of Open Access Journals (Sweden)

    Cihat Arslantürk

    2016-08-01

    Full Text Available The performance of pin fins transferring heat by convection and radiation and having variable thermal conductivity, variable emissivity and variable heat transfer coefficient was investigated in the present paper. Nondimensionalizing the fin equation, the problem parameters which affect the fin performance were obtained. Dimensionless nonlinear fin equation was solved with the variation of parameters method, which is quite new in the solution of nonlinear heat transfer problems. The solution of variation of parameters method was compared with known analytical solutions and some numerical solution. The comparisons showed that the solutions are seen to be perfectly compatible. The effects of problem parameters were investigated on the heat transfer rate and fin efficiency and results were presented graphically.

  9. Heat transfer and pressure drop comparison of louver- and plain-finned heat exchangers where one fluid passes through flattened tubes

    Directory of Open Access Journals (Sweden)

    J.M. Gorman

    2015-03-01

    Full Text Available Louvered fins constitute a major methodology for heat transfer enhancement. Of critical significance in evaluating the worthiness of such fins is the comparison between the heat transfer and pressure drop for a thus-finned heat exchanger with the baseline case of a counterpart plain-finned heat exchanger. Up to the present, it appears that such comparisons are confined to heat exchangers in which one of the participating fluids passes through circular tubes. In another basic geometry in which louvered fins have been employed, the aforementioned participating fluid passes through flattened tubes which are virtually rectangular in cross section. The focus of the present paper is to obtain results for the latter basic geometry for both louver-fin-based heat exchangers and counterpart plain-fin-based heat exchangers. The results were obtained by means of numerical simulation over a range of Reynolds numbers spanning approximately a factor of five. Over this range, enhancements of the heat transfer rate ranged from factors of approximately 2.2–2.8. Over this same Reynolds number range, the pressure drop increased by factors of 2.3–3.6. This outcome is attributable to the fact that the rate of heat transfer is less sensitive to the velocity than is the pressure drop.

  10. Influence of surface roughness and tube diameter on pool boiling at single plain and finned tubes. Zum Einfluss der Oberflaechenrauhigkeit und des Rohrdurchmessers beim Blasensieden an einzelnen Glatt- und Rippenrohren

    Energy Technology Data Exchange (ETDEWEB)

    Gorenflo, D.; Schoemann, H.; Sokol, P.; Caplanis, S. (Paderborn Univ. (Gesamthochschule) (Germany, F.R.). Lab. fuer Waerme- und Kaeltetechnik)

    1990-09-18

    Heat transfer with pool boiling of hexane was measured for single-plain and finned steel tubes with great diameter and very rough, sandblasted surface. The results show that the heat transfer coefficients calculated for the outer surfaces of both tubes are higher in the case of the finned tube at high heat fluxes, and gradually diminish down to the values of the plain tube until natural convection without bubble formation has been reached. Additional measurements using a plain tube with much smaller diameter but identical surface treatment indicate that great differences of the tube diameter influence the increase of the heat transfer coefficient with heat flux significantly, the relative pressure dependence and the absolute values of the heat transfer coefficient at intermediate heat fluxes, however, are concerned on a smaller scale. (orig.).

  11. Evaluación de Intercambiadores de Calor Compactos de Tubos Aletados Evaluation of Compact Finned-Tube Heat Exchangers

    Directory of Open Access Journals (Sweden)

    M.T. Martínez

    2004-01-01

    Full Text Available En este trabajo, se presenta el análisis térmico teórico de un intercambiador de calor compacto, con y sin condensación de agua en el lado del aire. El fenómeno de la condensación del vapor de agua en la corriente de aire entrante produce una película de agua en la superficie cubriéndola en forma parcial o completa. El análisis considera varias configuraciones geométricas con respecto a: la superficie de las aletas y a la forma de los tubos considerando la forma circular tradicional y también un caso para tubos planos. Los resultados obtenidos reflejan la eficiencia de la aleta en ambos casos: una aleta totalmente seca (sin condensación y a una totalmente húmeda es decir, totalmente cubierta por la película de condensado. Se concluye que la metodología propuesta es una buena alternativa de análisis y caracterización de un intercambiador, ya que los resultados obtenidos coinciden con los reportados en la literaturaThis study presents a theoretical thermal analysis of a compact heat exchanger, with and without water condensation on the air side. The phenomenon of condensation of water vapor in the entering air current produces a film of water on the surface, partially or completely covering the surface. The analysis considers various geometric configurations with respect to the surfaces of the fins and the form of the tubes, including the traditional round form as well as flattened tubes. The results obtained reflect the efficiency of the fins in both cases , including a completely dry fin (no condensation and a completely wet fin, that is completely covered with a film of condensate. It is concluded that the methodology proposed is a good alternative for the analysis and characterization of a heat exchanger since the results agree with those reported in the literature

  12. Investigating the performance of SiGe embedded dual source p-FinFET architecture

    Science.gov (United States)

    Sinha, Kunal; Gupta, Partha Sarathi; Chattopadhyay, Sanatan; Rahaman, Hafizur

    2016-10-01

    In this work, a modified Fin shaped Field Effect Transistor (FinFET) structure has been proposed with dual SiGe embedded extended source regions. Comparative simulation studies with SiGe embedded source/drain conventional single Fin channel and dual Fin channel FinFET structure having similar device footprint area shows almost 3× and 1.5× improvement of drive current respectively and lower threshold voltage in the proposed architecture. The dual extended SiGe source regions and presence of Si drain in the vertical direction of the channel generate bi-axial channel stress which improves the channel charge density, which results in improvement in drive current significantly. Also it has been observed from various simulation studies that the separated gate regions increase the inversion current density in the channel which also leads to improvement of the device performance.

  13. Two-Phase condensation Heat Transfer Coefficients Heat Transfer Coefficients and Pressure drops of R-404A for different Condensing Temperatures in a smooth and Micro-Fin Tube

    Directory of Open Access Journals (Sweden)

    DR. S.N. Sapali

    2009-11-01

    Full Text Available Two phase heat transfer coefficients and pressure drops of R-404A in a smooth (8.56 mm ID and micro-fin tube (8.96 mm ID are experimentally investigated. Different from previous studies, the present experiments are performed for different condensing temperatures, with superheating and sub cooling and using hermetically sealed compressor. The test runs are done at average saturated condensing temperatures ranging from 35oC to 60oC. The mass fluxes are between 90 and 800 kg m-2s-1 . The experimental results from both smooth and micro-fin tubes show that the average heat transfer coefficient and pressure drop increases with mass flux but decreases with increasing condensing temperature. The average heat transfer coefficient is 30-210% higher for micro-fin tube than that of smooth tube, with moderate increase in pressure drop ranging from 10-55%. New correlations based on the data gathered during the experimentation for predicting condensation heat transfer coefficients are proposed for wide range of practical applications.

  14. Effect of an Artificial Caudal Fin on the Performance of a Biomimetic Fish Robot Propelled by Piezoelectric Actuators

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    This paper addresses the design of a biomimetic fish robot actuated by piezoceramic actuators and the effect of artificial caudal fins on the fish robot's performance. The limited bending displacement produced by a lightweight piezocomposite actuator was amplified and transformed into a large tail beat motion by means of a linkage system. Caudal fins that mimic the shape of a mackerel fin were fabricated for the purpose of examining the effect of caudal fin characteristics on thrust production at an operating frequency range. The thickness distribution of a real mackerel's fin was measured and used to design artificial caudal fins. The thrust performance of the biomimetic fish robot propelled by fins of various thicknesses was examined in terms of the Strouhal number, the Froude number, the Reynolds number, and the power consumption. For the same fin area and aspect ratio, an artificial caudal fin with a distributed thickness shows the best forward speed and the least power consumption.

  15. Performance assessment of nanoscale double- and triple-gate FinFETs

    Science.gov (United States)

    Kranti, Abhinav; Armstrong, G. Alastair

    2006-04-01

    Based on 3D simulations, we report a performance assessment of triple- and double-gate FinFETs for high performance (HP), low operating power (LOP) and low standby power (LSTP) logic technologies according to ITRS 65 nm node specifications. The impact of spacer width, lateral source/drain doping gradient, aspect ratio, fin thickness and height along with gate work function on the device performance has been analysed in detail and guidelines are presented to meet the ITRS projections. The design guidelines proposed for a 65 nm node are also examined for a 45 nm node for triple- and double-gate FinFETs. Results show that lateral source/drain doping gradient along with spacer width can not only effectively control short channel effects, thus presenting low off-current, but can also be optimized to achieve low values of intrinsic delay. FinFETs should be designed with a higher aspect ratio (~4) along with lower values of fin thickness to achieve ITRS targets for off-current and intrinsic delay. Triple-gate FinFETs show greater design flexibility in selecting important technological and device parameters as compared to double-gate devices. A design window is presented to achieve ITRS targets for the three logic technology requirements with triple- and double-gate FinFETs.

  16. 针翅管传热与压降特性研究%Research on Heat Transfer and Pressure Drop Characteristics of Integral Pin-Fin Tube

    Institute of Scientific and Technical Information of China (English)

    石帅; 阎昌琪; 牛广林; 陈哲雨

    2012-01-01

    以润滑油为换热介质,对整体针翅管传热与阻力特性进行了理论分析与试验研究,研究结果可为针翅管的优化设计提供参考.在换热介质纵向冲刷换热管的条件下,对不同针翅长度的3种整体针翅管与光管进行了传热与阻力试验.结果表明:整体针翅管对润滑油换热具有很好的强化能力,在本试验范围内,整体针翅管对油流体扰动强烈,换热强度是同条件下光管的2~6倍;针翅长度是影响针翅管压降的主要因素,在雷诺数达300时,压降曲线出现转折.%Taking lubricating oil as the heat transfer medium, heat transfer and pressure drop characteristics of integral pin-fin tubes were researched both in terms of theoretical and experiments. The results can provide a reference for pin-fin tube optimization. Under the condition of heat transfer medium longitudinally flushing the heat exchanger tube surface, the heat transfer and resistance experiments of plain tube and integral pin-fin tubes (in three different length) were carried out in the present work. The results show that the integral pin-fin tubes can improve the heat transfer ability of lubricating oil. The oil flow fluctuation caused by integral pin-fin tubes is intense and the heat transfer intension of integral pin-fin tubes is 2-6 times of plain tube at the same experiment condition. The length of fin makes main influence on pressure drop, and the pressure drop curve turns around when the values of Reynolds number reaches to 300.

  17. Validity of intra-particle models of mass transfer kinetics in the analysis of a fin-tube type adsorption bed

    Energy Technology Data Exchange (ETDEWEB)

    Hong, Sang Woo; Ahn, Sang Hyeok; Chung, Jae Dong [Sejong University, Seoul (Korea, Republic of); Kwon, Oh Kyung [Korea Institute of Industrial Technology, Chonan (Korea, Republic of)

    2014-05-15

    This study presents a numerical investigation of the heat and mass transfer kinetics of a fin-tube type adsorption bed using a two dimensional numerical model with silica-gel/water as the adsorbent and refrigerant pair. The performance is strongly affected by the heat and mass transfer in the adsorption bed, but the details of the mass transfer kinetics remain unclear. The validity of intra-particle models used to simulate mass transfer kinetics such as the equilibrium, LDF, and solid-diffusion models are examined, and the valid ranges of the diffusion ratio for each model are proposed. An intra-particle diffusion model should be carefully implemented; otherwise, seriously distorted results may be produced, i.e., over-estimation for the equilibrium model and under estimation for the LDF model.

  18. Air Coolers and Fin Tubes for Heat Transfer Enhancement%空气冷却器及其强化传热翅片管型

    Institute of Scientific and Technical Information of China (English)

    曲燕; 仇性启; 王丽飞

    2012-01-01

    对干式、湿式以及干湿联合式空气冷却器的换热特点、常用的翅片管结构、三维翅片等强化传热翅型以及空气冷却器翅片管的加工工艺、选材等方面进行了综述研究.采用套片式加工工艺的条缝型错置带状三维翅片和采用无屑加工方法成形的锯齿翅片,在较低空气流速下具有较高的传热因子和摩擦因子比,是提高空气冷却器空气侧换热的高效翅片管型,为石化行业空气冷却器翅片管的改造提供参考.%The heat transfer characteristics of dry-type, wet-type and combined type air coolers, and the commonly-used fin-tube structures, the 3D enhanced heat transfer fins and the fin-tube processing as well as the material selection of air coolers were studied, the results show that the slotted 3D fin-tube which boasting of continuous integral technology and the serrated fin-tube which boasting of chipless machining method can enhance the air-side heat transfer efficiency because of their higher heat transfer factor and friction factor at lower air velocity. This provides the reference for upgrading of air cooler' s fin-tube in petrochemical industry.

  19. Research on natural condensation heat transfer characteristics on horizontal finned tube%水平肋片管外自然凝结传热特性研究

    Institute of Scientific and Technical Information of China (English)

    李慧君; 董楠; 王炯

    2015-01-01

    基于 Nusselt凝结传热理论,沿肋片管圆周方向划分有限个微元角,建立了每个微元角内肋侧壁、肋间基管及肋顶三个区域的凝结传热模型,通过求解非淹没区和淹没区总传热量,推导管外平均传热系数计算式。计算不同肋片高度、肋密度时,R134a饱和蒸汽的管外平均凝结传热系数。结果表明:随肋密度的增加,平均传热系数先增大后减小,肋密度为25 fpi时传热最佳;高肋片管的平均凝结传热系数大于低肋片管的,肋片高度达到一定值时,平均传热系数几乎不随肋高增加而增加。当 R134a 饱和蒸汽为20℃时,两种不同翅片密度的管外平均凝结传热系数随温差的增大而减小,并通过所建模型得到的计算值与 Beatty-Kate 模型进行了比较,平均误差分别为约16.1%和8.3%,故所建模型基本反映肋片管外蒸汽凝结传热机理。%Presents an analytical model to calculate the condensation heat transfer coefficient on horizontal finned tube based on the Nusselt condensation heat transfer theory.The employs an elemental calculation by dividing the tube wall into finite elements to establish the condensate heat transfer model of the fin flank,the channel between fins and the fin tip in the small annular element. The model can predict the mean condensation heat transfer coefficient outside finned tubes by calculating the total heat transfer.The average condensation heat transfer coefficient of the saturated steam R134a outside the pipe versus fin heights ,fin densities were then calculated.The results show that the average heat transfer coefficient first increases and then decreases with the increase of fin density.The optimum fin density is 25 fpi an the average condensation heat transfer coefficient of the higher finned tube is greater than that of lower finned tube.The average heat transfer coefficient hardly increased with the increase of fin height until it reaches a certain value

  20. Experimental study of heat transfer and thermal performance with longitudinal fins of solar air heater

    Science.gov (United States)

    Chabane, Foued; Moummi, Noureddine; Benramache, Said

    2013-01-01

    The thermal performance of a single pass solar air heater with five fins attached was investigated experimentally. Longitudinal fins were used inferior the absorber plate to increase the heat exchange and render the flow fluid in the channel uniform. The effect of mass flow rate of air on the outlet temperature, the heat transfer in the thickness of the solar collector, and the thermal efficiency were studied. Experiments were performed for two air mass flow rates of 0.012 and 0.016 kg s−1. Moreover, the maximum efficiency values obtained for the 0.012 and 0.016 kg s−1 with and without fins were 40.02%, 51.50% and 34.92%, 43.94%, respectively. A comparison of the results of the mass flow rates by solar collector with and without fins shows a substantial enhancement in the thermal efficiency. PMID:25685486

  1. Experimental study of heat transfer and thermal performance with longitudinal fins of solar air heater

    Directory of Open Access Journals (Sweden)

    Foued Chabane

    2014-03-01

    Full Text Available The thermal performance of a single pass solar air heater with five fins attached was investigated experimentally. Longitudinal fins were used inferior the absorber plate to increase the heat exchange and render the flow fluid in the channel uniform. The effect of mass flow rate of air on the outlet temperature, the heat transfer in the thickness of the solar collector, and the thermal efficiency were studied. Experiments were performed for two air mass flow rates of 0.012 and 0.016 kg s−1. Moreover, the maximum efficiency values obtained for the 0.012 and 0.016 kg s−1 with and without fins were 40.02%, 51.50% and 34.92%, 43.94%, respectively. A comparison of the results of the mass flow rates by solar collector with and without fins shows a substantial enhancement in the thermal efficiency.

  2. Experimental study of heat transfer and thermal performance with longitudinal fins of solar air heater.

    Science.gov (United States)

    Chabane, Foued; Moummi, Noureddine; Benramache, Said

    2014-03-01

    The thermal performance of a single pass solar air heater with five fins attached was investigated experimentally. Longitudinal fins were used inferior the absorber plate to increase the heat exchange and render the flow fluid in the channel uniform. The effect of mass flow rate of air on the outlet temperature, the heat transfer in the thickness of the solar collector, and the thermal efficiency were studied. Experiments were performed for two air mass flow rates of 0.012 and 0.016 kg s(-1). Moreover, the maximum efficiency values obtained for the 0.012 and 0.016 kg s(-1) with and without fins were 40.02%, 51.50% and 34.92%, 43.94%, respectively. A comparison of the results of the mass flow rates by solar collector with and without fins shows a substantial enhancement in the thermal efficiency.

  3. Numerical analysis of the flow and heat transfer characteristics for forced convection-radiation in entrance region of an internally finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Park, Hi Yong; Choi, Moon Suk [Hanyang Univ., Seoul (Korea, Republic of); Park, Kyoung Woo [LGIS Co., Ltd., Incheon (Korea, Republic of)

    1998-04-01

    The flow and heat transfer characteristics of combined forced convection and radiation in the entrance region of internally finned tubes are investigated numerically in this paper. The uniform flow is considered for an inlet flow condition. A three dimensional parabolic problem is solved by a marching-type procedure envolving a series of two dimensional elliptic problems in the cross-stream plane. The SIMPLER-algorithm and Raithby's pressure-velocity coupling method are employed to analyze the flow and heat transfer characteristics. For the calculation of radiative heat transfer, the P{sub 1}-approximation and the Weighted Sum of Gray Gases Method (WSGGM) are used. The effects of fin height, number of fins, optical thickness, reference temperature, and Planck number on the flow and heat transfer characteristics are examined. It was found that the effect of fin-height on the heat transfer characteristic is more dominant than that of number of fins. The present results show that the optimal non-dimensional fin height and number of fins are 0.4 and 16, respectively.

  4. The Influence of Wall Conductivity of Film Condensation with Integral Fin Tubes

    Science.gov (United States)

    1993-09-23

    Sieder , E. N., and Tate, C. E., "Heat Transfer and Pressure Drop of Liquids in Tubes", Industrial Engineering Chemistry, Vol. 28, p. 1429, 1936. 37...BEEP 1603 INPUT "ENTER Ci IF DIFFERENT FROM STORED VALUE’,Ci 1604 END IF 1605 PRINTER IS 701 1606 IF IhimO THEN PRINT USING "ISX,""Modified Sieder ...THEN Jp-l 7336 END IF 7339 IF Jp-l THEN 6874 7342 Ci-(Ci+Cic)#.S 7345 PRINT 7346 IF Ihi=- THEN 7348 PRINT USING "l6X,""Ci (based on Sieder -Tate) o

  5. Comparative Study for Improving the Thermal and Fluid Flow Performance of Micro Channel Fin Geometries Using Numerical Simulation

    Directory of Open Access Journals (Sweden)

    S.Subramanian

    2015-07-01

    Full Text Available There is a continuous quest for improving the performance of micro channels for handling the increased dissipation of heat from electronics circuits. The Oblique fin micro channels are attractive as they perform better than plate fin & pin fin configurations. There are scopes for further improvements in oblique fin micro channels. Hence this work is about the investigation for the performance enhancement by modifying the oblique fin geometry. Seven variants of micro channel geometries have been explored using three dimensional numerical simulations. The variants are plate fin, in-line pin fin, staggered pin fin, oblique fin, oblique fin with two slit angles, oblique with nozzle type slit and improved oblique fin. The simulation results are validated using the published data. To ensure a common reference for comparison, hydraulic diameter, inlet flow conditions, heat loads and the boundary conditions are kept identical across all the geometries. The results of simulation are compared for the thermal & fluid flow performances. Heat transfer correlations have been developed using the simulation data. The proposed modification is found to enhance the performance significantly

  6. Performance measurement of plate fin heat exchanger by exploration: ANN, ANFIS, GA, and SA

    Directory of Open Access Journals (Sweden)

    A.K. Gupta

    2017-01-01

    Full Text Available An experimental work is conducted on counter flow plate fin compact heat exchanger using offset strip fin under different mass flow rates. The training, testing, and validation set of data has been collected by conducting experiments. Next, artificial neural network merged with Genetic Algorithm (GA utilized to measure the performance of plate-fin compact heat exchanger. The main aim of present research is to measure the performance of plate-fin compact heat exchanger and to provide full explanations. An artificial neural network predicted simulated data, which verified with experimental data under 10–20% error. Then, the authors examined two well-known global search techniques, simulated annealing and the genetic algorithm. The proposed genetic algorithm and Simulated Annealing (SA results have been summarized. The parameters are impartially important for good results. With the emergence of a new data-driven modeling technique, Neuro-fuzzy based systems are established in academic and practical applications. The neuro-fuzzy interference system (ANFIS has also been examined to undertake the problem related to plate-fin heat exchanger performance measurement under various parameters. Moreover, Parallel with ANFIS model and Artificial Neural Network (ANN model has been created with emphasizing the accuracy of the different techniques. A wide range of statistical indicators used to assess the performance of the models. Based on the comparison, it was revealed that technical ANFIS improve the accuracy of estimates in the small pool and tropical ANN.

  7. 3D-CFD simulation and neural network model for the j and f factors of the wavy fin-and-flat tube heat exchangers

    Directory of Open Access Journals (Sweden)

    M Khoshvaght Aliabadi

    2011-09-01

    Full Text Available A three dimensional (3D computational fluid dynamics (CFD simulation and a neural network model are presented to estimate the behaviors of the Colburn factor (j and the Fanning friction factor (f for wavy fin - and - flat tube (WFFT heat exchangers. Effects of the five geometrical factors of fin pitch, fin height, fin length, fin thickness, and wavy amplitude are investigated over a wide range of Reynolds number (600fins have significant effects on the j and f factors as a function of Reynolds number. The computational results have an adequate accuracy when compared to experimental data. The accuracy of the calculations of the j and f factors are evaluated by the values of the absolute average relative deviation (AARD, being respectively 3.8% and 8.2% for the CFD simulation and 1.3% and 1% for the neural network model. Finally, new correlations are proposed to estimate the values of the j and f factors with 3.22% and 3.68% AARD respectively.

  8. Performance enhancement of AlGaN/GaN nanochannel omega-FinFET

    Science.gov (United States)

    Im, Ki-Sik; Seo, Jae Hwa; Vodapally, Sindhuri; Kang, In Man; Lee, Jae-Hoon; Cristoloveanu, Sorin; Lee, Jung-Hee

    2017-03-01

    Novel AlGaN/GaN omega-shaped nanochannel FinFETs with fin width of 50 nm were successfully fabricated using TMAH lateral wet etching with ALD HfO2 sidewall spacer. This fin structure apparently exhibited the current spreading in the access region, which results in the suppression of the drain lag effect at high drain voltage and sharp switching performance with subthreshold swing of 57-65 mV/decade. Excellent on- and off-state state performances for the fabricated device prove that the omega-shaped gate structure not only exhibits excellent gate controllability, but also decouples the active nano-channel region from the underlying thick buffer. The proposed device is very promising candidate for high-performance device applications.

  9. 十二排圆形翅片管换热器的传热与流动特性研究%Flow Behavior and Heat Transfer Characteristics of Circular Finned Tube Heat Exchangers with Twelve-row

    Institute of Scientific and Technical Information of China (English)

    詹伟民; 简弃非

    2014-01-01

    The airside flow performance of circular finned-tube with twelve-row heat exchangers is numerical investigated in this study. The velocity field, temperature field and streamlines are obtained and the result of the simulation study is compared with the experimental result and the experimental correlation. The research findings show that the heat transfer coefficient of the fin surface and the tube surface of the first row with fin spacing of 9.6mm are 1.67 and 0.97 times with the fin spacing of 2.4mm. And the heat transfer coefficients of the single fin surface and tube surface before the sixth row are strongly fluctuating, and when the number of the in-depth bundles is greater than six, the heat transfer coefficients of single fin surface and tube surface are almost consistent with going deeper into the bundles.%采用数值计算方法研究12排大管圆形翅片表面空气侧流体的流动特性,获得不同雷诺数下圆形翅片的速度分布云图、温度分布云图和流线分布图,并将模拟的结果与实验和实验关联式分别进行验证。研究结果表明:翅片间距为9.6mm第一排管壁侧和翅片表面的传热系数分别是翅片间距为2.4mm的1.67和0.97倍;前面六排翅片表面和管壁表面的传热系数具有很强的波动,而在第六排后翅片表面和管壁表面的传热系数趋向于稳定。

  10. Performance of pressure tubes in CANDU reactors

    Energy Technology Data Exchange (ETDEWEB)

    Rodgers, D.; Griffiths, M.; Bickel, G.; Buyers, A.; Coleman, C.; Nordin, H.; St Lawrence, S. [Canadian Nuclear Laboratories, Chalk River, Ontario (Canada)

    2016-06-15

    The pressure tubes in CANDU reactors typically operate for times up to about 30 years prior to refurbishment. The in-reactor performance of Zr-2.5Nb pressure tubes has been evaluated by sampling and periodic inspection. This paper describes the behavior and discusses the factors controlling the behaviour of these components. The Zr–2.5Nb pressure tubes are nominally extruded at 815{sup o}C, cold worked nominally 27%, and stress relieved at 400 {sup o}C for 24 hours, resulting in a structure consisting of elongated grains of hexagonal close-packed alpha-Zr, partially surrounded by a thin network of filaments of body-centred-cubic beta-Zr. These beta-Zr filaments are meta-stable and contain about 20% Nb after extrusion. The stress-relief treatment results in partial decomposition of the beta-Zr filaments with the formation of hexagonal close-packed alpha-phase particles that are low in Nb, surrounded by a Nb-enriched beta-Zr matrix. The material properties of pressure tubes are determined by variations in alpha-phase texture, alpha-phase grain structure, network dislocation density, beta-phase decomposition, and impurity concentration that are a function of manufacturing variables. The pressure tubes operate at temperatures between 250 {sup o}C and 310 {sup o}C with coolant pressures up to about 11 MPa in fast neutron fluxes up to 4 x 10{sup 17} n·m{sup -2}·s{sup -1} (E > 1 MeV) and the properties are modified by these conditions. The properties of the pressure tubes in an operating reactor are therefore a function of both manufacturing and operating condition variables. The ultimate tensile strength, fracture toughness, and delayed hydride-cracking properties (velocity (V) and threshold stress intensity factor (K{sub IH})) change with irradiation, but all reach a nearly limiting value at a fluence of less than 10{sup 25} n·m{sup -2} (E > 1 MeV). At this point the ultimate tensile strength is raised about 200 MPa, toughness is reduced by about 50%, V increases

  11. CFD simulation of propeller and rudder performance when using additional thrust fins

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    To analyse a possible way to improve the propulsion performance of ships, the unstructured grid and the Reynolds Average Navier-Stokes equations were used to calculate the performance of a propeller and rudder fitted with additional thrust fins in the viscous flow field.The computational fluid dynamics software FLUENT was used to simulate the thrust and torque coefficient as a function of the advance coefficient of propeller and the thrust efficiency of additional thrust fins.The pressure and velocity flow behind the propeller was calculated.The geometrical nodes of the propeller were constituted by FORTRAN program and the NUMBS method was used to create a configuration of the propeller, which was then used by GAMMBIT to generate the calculation model.The thrust efficiency of fins was calculated as a function of the number of additional fins and the attack angles.The results of the calculations agree fairly well with experimental data, which shows that the viscous flow solution we present is useful in simulating the performance of propellers and rudders with additional fins.

  12. 3D analysis of thermal exchange in finned batteries. A comparison between round and elliptical tubes; Analisi tridimensionale dello scambio termico nelle batterie alettate. Confronto fra tubi tondi e tubi ellittici

    Energy Technology Data Exchange (ETDEWEB)

    Valdiserri, P. [Bologna Univ., Bologna (Italy). Facolta' di Ingegneria, Dipartimento di Ingegneria Energetica, Nucleare e del Controllo Ambientale

    2001-05-01

    In this paper a numerical 3D analysis of the thermal exchange in air-cooled finned batteries has been carried out. Speed and temperature values in each hub of the numerical simulation domain have been reckoned both at different air flows and with different shapes of the tubes. The thermal power exchanged between tubes and air is obtained by the simulation of a numerical model of a finned battery with round section tubes and is compared to the values obtained for three batteries with elliptical section tubes. The comparison has been performed for different values of the air input speed. [Italian] In questo lavoro e' stata condotta un'analisi numerica tridimensionale dei fenomeni di scambio termico in batterie alettate raffreddate ad aria. I valori di velocita' e temperatura nei singoli nodi del dominio di simulazione numerica sono stati calcolati sia al variare della portata dell'aria sia della forma dei tubi. La potenza termica scambiata tra tubi ed aria, ottenuta dalle simulazioni in un modello numerico di batteria alettata composta da tubi di sezione circolare, e' stata confrontata con i valori ottenuti per tre batterie formate da tubi di sezione elittica. Il confronto e' stato eseguito per diversi valori della velocita' d'ingresso dell'aria.

  13. Feasibility Study of the Ø5 Tube-and-fin Heat Exchanger in Automotive Heat Pump System%车用热泵用小管径管片式换热器性能研究

    Institute of Scientific and Technical Information of China (English)

    韦伟; 赵宇; 陈江平; 宋吉; 高屹峰

    2013-01-01

      目前车用空调冷凝器均为平行流冷凝器,作为热泵蒸发器时易结霜,且化霜时排水不畅.而圆管翅片换热器换热性能较差,难以满足结构布置要求.开发了Ø5管径的小管径换热器,与平行流换热器进行了性能对比测试.结果表明:采用小管径管片式换热器时,制冷模式下COP提高了17.4%~23.7%,热泵模式下COP提高12.6%~35.8%,且在热泵模式下可降低压缩机排气温度15~28℃.小管径管片式换热器在电动汽车热泵系统应用前景广阔.%The parallel flow microchannel (PFM) heat exchanger is widely used in automotive air conditioning system, but it has the disadvantage of easy-frost and difficult in water-drain in defrost . The traditional tube and fin heat exchanger can overcome the frost and defrost problem but has low efficiency. In this paper a Ø5 tube and fin heat exchanger is developed for the automotive heat pump. Performances of small diameter tube-and-fin heat exchanger and PFM heat exchanger are compared based on benchmark test. Results show that the system with small diameter tube-and-fin heat exchanger has 17.4%~23.7% higher COP in air conditioning mode, 12.6%~35.8% higher COP and 15~28℃ lower compressor discharge temperature in heat pump mode, which indicates that small diameter tube-and-fin heat exchanger is a promising solution to the automotive heat pump system of electric vehicle.

  14. Research and Development of Heat Exchanger with Efficient Perforated Straight (Corrugated) and Internal Finned-tubes%开孔平直(波纹)高效内翅管热交换器的研究开发

    Institute of Scientific and Technical Information of China (English)

    冯苗根; 何建龙

    2012-01-01

    对几种不同结构内翅管的传热和阻力特性进行了实验分析,通过工程实际计算应用比较,揭示了高效内翅管的优越性,提出了采用开孔平直(波纹)内翅管替代原光管作为新一代列管式热交换器的发展方向.%Through analysis by both heat transfer & resistance characteristic experiments of several internal finned-tubes with different structures and comparison between the calculations applied in real projects, this paper discloses the superiority of efficient internal finned-tube and proposes the development of new generation of shell and tube heat exchanger equipped with perforated, straight (corrugated) and internal finned-tubes instead of previous tubes without fins.

  15. Performance of an adjustable, threaded inertance tube

    Science.gov (United States)

    Zhou, W. J.; Pfotenhauer, J. M.; Nellis, G. F.; Liu, S. Y.

    2015-12-01

    The performance of the Stirling type pulse tube cryocooler depends strongly on the design of the inertance tube. The phase angle produced by the inertance tube is very sensitive to its diameter and length. Recent developments are reported here regarding an adjustable inertance device that can be adjusted in real time. The inertance passage is formed by the root of a concentric cylindrical threaded device. The depth of the threads installed on the outer screw varies. In this device, the outer screw can be rotated four and half turns. At the zero turn position the length of the passage is 1.74 m and the hydraulic diameter is 7 mm. By rotating the outer screw, the inner threaded rod engages with additional, larger depth threads. Therefore, at its upper limit of rotation, the inertance passage includes both the original 1.74 m length with 7mm hydraulic diameter plus an additional 1.86 m length with a 10 mm hydraulic diameter. A phase shift change of 24° has been experimentally measured by changing the position of outer screw while operating the device at a frequency of 60 Hz. This phase angle shift is less than the theoretically predicted value due to the presence of a relatively large leak through the thread clearance. Therefore, the distributed component model of the inertance tube was modified to account for the leak path causing the data to agree with the model. Further, the application of vacuum grease to the threads causes the performance of the device to improve substantially.

  16. Performance comparison of pin fin in-duct flow arrays with various pin cross-sections

    Energy Technology Data Exchange (ETDEWEB)

    Sahiti, N. [LSTM-Erlangen, Institute of Fluid Mechanics, Friedrich-Alexander-University, Erlangen-Nuremberg, Cauerstr. 4, D-91058 Erlangen (Germany)]. E-mail: sahiti@lstm.uni-erlangen.de; Lemouedda, A. [Department of Process Engineering, Georg-Simon-Ohm University of Applied Sciences, Wassertorstr. 10, D-90489 Nuremberg (Germany); Stojkovic, D. [LSTM-Erlangen, Institute of Fluid Mechanics, Friedrich-Alexander-University, Erlangen-Nuremberg, Cauerstr. 4, D-91058 Erlangen (Germany); Durst, F. [LSTM-Erlangen, Institute of Fluid Mechanics, Friedrich-Alexander-University, Erlangen-Nuremberg, Cauerstr. 4, D-91058 Erlangen (Germany); Franz, E. [Department of Process Engineering, Georg-Simon-Ohm University of Applied Sciences, Wassertorstr. 10, D-90489 Nuremberg (Germany)

    2006-08-15

    Pin fin arrays are frequently used for cooling of high thermal loaded electronic components. Whereas the pin fin accomplishment regarding heat transfer is always higher than that of other fin configurations, the high pressure drop accompanying pins seriously reduces their overall performance. In order to check how the form of pin cross-section influences the pressure drop and heat transfer capabilities, six forms of pin cross-section were numerically investigated. By employing the conjugate heat transfer boundary conditions, numerical simulations close to realistic working conditions were performed. Two geometric comparison criteria were applied so that the conclusions derived from numerical computations were valid for various possible geometric parameters and working conditions. Both staggered and inline pin arrangements were investigated as these are common in practical applications. The heat transfer and pressure drop characteristics are presented in terms of appropriate dimensionless variables. The final judgment of the performance of the pin fin cross-section was performed based on the heat exchanger performance plot. Such a plot allows the assessment of the pin performance including their heat transfer and the pressure drop.

  17. Influence of the Water-Cooled Heat Exchanger on the Performance of a Pulse Tube Refrigerator

    Directory of Open Access Journals (Sweden)

    Wei Wang

    2017-02-01

    Full Text Available The water-cooled heat exchanger is one of the key components in a pulse tube refrigerator. Its heat exchange effectiveness directly influences the cooling performance of the refrigerator. However, effective heat exchange does not always result in a good performance, because excessively reinforced heat exchange can lead to additional flow loss. In this paper, seven different water-cooled heat exchangers were designed to explore the best configuration for a large-capacity pulse tube refrigerator. Results indicated that the heat exchanger invented by Hu always offered a better performance than that of finned and traditional shell-tube types. For a refrigerator with a working frequency of 50 Hz, the best hydraulic diameter is less than 1 mm.

  18. Novel high-gain, improved-bandwidth, finned-ladder V-band Traveling-Wave Tube slow-wave circuit design

    Science.gov (United States)

    Kory, Carol L.; Wilson, Jeffrey D.

    1994-01-01

    The V-band frequency range of 59-64 GHz is a region of the millimeter-wave spectrum that has been designated for inter-satellite communications. As a first effort to develop a high-efficiency V-band Traveling-Wave Tube (TWT), variations on a ring-plane slow-wave circuit were computationally investigated to develop an alternative to the more conventional ferruled coupled-cavity circuit. The ring-plane circuit was chosen because of its high interaction impedance, large beam aperture, and excellent thermal dissipation properties. Despite these advantages, however, low bandwidth and high voltage requirements have, until now, prevented its acceptance outside the laboratory. In this paper, the three-dimensional electrodynamic simulation code MAFIA (solution of MAxwell's Equation by the Finite-Integration-Algorithm) is used to investigate methods of increasing the bandwidth and lowering the operating voltage of the ring-plane circuit. Calculations of frequency-phase dispersion, beam on-axis interaction impedance, attenuation and small-signal gain per wavelength were performed for various geometric variations and loading distributions of the ring-plane TWT slow-wave circuit. Based on the results of the variations, a circuit termed the finned-ladder TWT slow-wave circuit was designed and is compared here to the scaled prototype ring-plane and a conventional ferruled coupled-cavity TWT circuit over the V-band frequency range. The simulation results indicate that this circuit has a much higher gain, significantly wider bandwidth, and a much lower voltage requirement than the scaled ring-plane prototype circuit, while retaining its excellent thermal dissipation properties. The finned-ladder circuit has a much larger small-signal gain per wavelength than the ferruled coupled-cavity circuit, but with a moderate sacrifice in bandwidth.

  19. 管翅式热泵相变储能器的数值模拟%Numerical Simulation of Fin-tube Heat Pump with Phase Change Thermal Storage

    Institute of Scientific and Technical Information of China (English)

    朱冬生; 徐婷; 杨硕; 叶为标; 汪南; 巨小平

    2011-01-01

    In order to study the aluminum finned tube heat transfer properties of PCM, through the model and the numerical simulation method to have fins and no finned heat transfer performance of the storage unit. Study the influence of fin spacing(w)、thickness (2v)and thermal conductivity of PCM (kpcm) on total exothermic time. Comparing with a wingless energy storage unit,the solidification time reduced to 10%. The fin spacing and the total exothermic has a linear relation. The results show that aluminum fin greatly enhance the heat transfer of the phase transition process, especially the heat transfer coefficient of the PCM lower than 0.5 W/(m· K).%为了研究铝翅片管对相变储能材料(PCM)传热性质的影响,通过建立模型数值模拟的方法对有翅片和无翅片的储能单元的传热性能进行了对比.研究了翅片间距(w)、铝片厚度(2v)、相变材料导热系数(kpcm)等参数对总放热时间的影响.在有翅片的情况下,储热单元凝固的时间比无翅片时减少了90%,而翅片间距和总放热时间近似呈线性关系.得出铝翅片可以大大加强相变过程传热、特别是对导热系数小于0.5W/(m·K)的PCM强化效果非常明显.

  20. Comparison of fin ray sampling methods on white sturgeon Acipenser transmontanus growth and swimming performance.

    Science.gov (United States)

    Nguyen, P L; Jackson, Z J; Peterson, D L

    2016-02-01

    Effects of two fin-ray sampling methods on swimming performance, growth and survival were evaluated for hatchery-reared sub-adult white sturgeon Acipenser transmontanus. Fish were subjected to either a notch removal treatment in which a small section was removed from an anterior marginal pectoral-fin ray, or a full removal treatment in which an entire marginal pectoral-fin ray was removed. Control fish did not have fin rays removed, but they were subjected to a sham operation. A modified 3230 l Brett-type swim tunnel was used to evaluate 10 min critical station-holding speeds (SCSH ) of A. transmontanus, immediately after the fin ray biopsies were obtained with each method. Survival and growth were evaluated over a 6 month period for a separate group of fish subjected to the same biopsy methods. Mean ± S.E. 10 min SCSH were 108·0 ± 2·3, 110·0 ± 2·6 and 115·0 ± 3·5 cm s(-1) for the notch removal group, full removal group and control group, respectively, and were not significantly different among treatments. Behavioural characteristics including tail-beat frequency and time spent hunkering were also not significantly different among treatment groups swimming at the same speeds. There were no mortalities and relative growth was similar among treatment groups. Average biopsy time for the notch removal method was lower and the wounds appeared to heal more quickly compared with the full removal method.

  1. Hydrodynamic Performance of an Undulatory Robot: Functional Roles of the Body and Caudal Fin Locomotion

    Directory of Open Access Journals (Sweden)

    Li Wen

    2013-01-01

    Full Text Available Both body undulation and caudal fin flapping play essential locomotive roles while a fish is swimming, but how these two affect the swimming performance and hydrodynamics of fish individually is yet to be known. We implemented a biomimetic robotic fish that travel along a servo towing system, which can be regarded as “treadmill” of the model. Hydrodynamics was studied as a function of the principal kinetic parameters of the undulatory body and caudal fin of the model in a self‐propelled condition, under which the time‐averaged measured axial net force becomes zero. Thrust efficiency was estimated from two‐dimensional digital particle image velocimetry (DPIV measurements in the horizontal and mid‐caudal fin plane. The Single‐Row Reverse Karman wake (2S is commonly observed in many previous studies of live fish swimming. However, we show that a Double‐Row Two‐Paired vortices (2P wake was generated by the robotic model for most kinetic parameter combinations. Interestingly, the 2S wake emerged within the results of a narrow range of robotic caudal fin pitch angles (0≤θ≤10°, occurring concurrently with enhanced thrust efficiency. We also show that, compared with the effect of body wavelength (λ, the wake structure behind the robotic swimmer is more sensitive to the Strouhal number (St and caudal fin pitch angle (θ.

  2. Experimental study on condensation of refrigerant-oil mixtures. Part 3; R-12 and R-22 on the external surface of single and multiple horizontal finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Wang, J.C.Y.; Lin, S.; Fazio, P.; Jiang, Z. (Concordia Univ., Montreal, Quebec (CA))

    1989-01-01

    Presented are the test results of R-12 and R-22 on the external surface of horizontal finned tubes. The oil used in this study is alkylbenzene-based. Both pure refrigerant vapor tests and vapor-oil mixture tests were conducted at two different condensing temperatures-32.2{degrees} and 40.5{degrees}C (90{degrees} and 105{degrees}F), respectively. It was found that the presence of oil in R-12 and R-22 vapor with any mass radio lowers the condensing coefficient. However, the reduction of the condensing coefficient is not proportional to the percent of oil in the refrigerant vapors for the finned tubes. As for the pressure drop across the condenser, the effect of oil in the refrigerant vapors is not noticeable.

  3. Analysis of flow maldistribution in fin-and-tube evaporators for residential air-conditioning systems

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl

    validated and showed that a slip flow model need be used. A test case 8.8 kW residential air-conditioning system with R410A as refrigerant is chosen as baseline for the numerical investigations, and the simulations are performed at standard rating conditions from ANSI/AHRI Standard 210/240 (2008...... superheat by distributing individual channel mass flow rate continuously (perfect control). The compensation method is compared to the use of a larger evaporator in order to study their trade-off in augmenting system performance (cooling capacity and COP). The studies are performed by numerical modeling...... in the object-oriented programming language Modelicar and by using the commercial modeling environment Dymola 7.4 (2010). The evaporator model needs to be capable of predicting the flow distribution and circuitry effects, and for these reasons the dynamic distributed one-dimensional mixture two-phase flow model...

  4. Numerical study of thermal performance of perforated circular pin fin heat sinks in forced convection

    Science.gov (United States)

    Wen, Mao-Yu; Yeh, Cheng-Hsiung

    2016-12-01

    This paper presents a numerical simulation of the heat transfer performance under forced convection for two different types of circular pin fin heat sinks with (Type A) and without (Type B) a hollow in the heated base. COMSOL Multiphysics, which is used for the thermal hydraulic analyses, has proven to be a powerful finite-element-based simulation tool for solving multiple physics-based systems of partial and ordinary differential equations. The standard κ- ɛ two-equations turbulence model is employed to describe the turbulent structure and behavior. The numerical results are validated with the experimental results, and are shown to be in good agreement. The effects of the Reynolds number, height of the fin, finning factor and the perforated base plate on the heat-transfer coefficient are investigated and evaluated. The present study strongly recommends the use of a small hollow ( (Dh /Db ) sink.

  5. Numerical Simulation of the Flow Field Characteristics of Perforated Fin-in-tube Heat Exchanger%整体式穿孔翅片流场特性的数值研究

    Institute of Scientific and Technical Information of China (English)

    詹伟民; 简弃非

    2014-01-01

    The airside flow performance of perforated and fin-in-tube heat exchangers is numerical investigated in this study. The pressure field, velocity field and streamlines are obtained. The research findings show that perforating fins can to strengthen heat transfer. Compare with plate fins, perforating fins enhance the heat transfer coefficient about 2.46%~6.92%.%采用数值计算方法研究穿孔翅片表面空气侧流体的流动特性,获得不同雷诺数下穿孔翅片的速度分布云图、压力分布云图和流线分布图,并与平翅片进行对比分析。研究结果表明:在翅片上合适位置进行穿孔有利于强化传热,与平翅片相比,穿孔翅片的传热系数最大提高6.92%,最小提高2.46%。

  6. 双金属复合翅片管振动特性的研究%Vibration characteristics of bimetallic finned tubes

    Institute of Scientific and Technical Information of China (English)

    郭建英; 马腾飞; 刘生宝; 白艳艳

    2016-01-01

    Bimetallic finned tubes are highly efficient heat transfer components,and they are easy to have flow-induced vibration damages.Their modal analysis has an important engineering significance.A bimetallic finned tube was simplified as a system with series and parallel stiffnesses according to its structural characteristics.The bending,torsion and axial vibration modes of the bimetallic finned tube were analyzed theoretically by using the methods of equivalent cross-sectional bending stiffness,equivalent torsion stiffness and equivalent tension-compression stiffness combined with the equivalent mass and equivalent moment of inertia.The tests and finite element analysis for vibration modes of bimetallic finned tubes were conducted in order to verify the correctness of the theoretical methods.The effects of fin geometry on the natural frequencies of a steel-aluminum bimetal finned tube with rectangular fins were investigated.The results showed that its bending,torsional and axial vibration natural frequencies decrease with increase in fin height and fin thickness,and increase with increase in fin pitch.%双金属复合翅片管是一种高效传热元件,容易发生流体诱导振动破坏,对其进行振动模态理论分析具有重要的工程指导意义。针对双金属复合翅片管的结构特征,将其简化为串、并联刚度系统,采用组合截面等效弯曲刚度、等效扭转刚度和等效抗拉压刚度,并结合等效质量和等效转动惯量的方法,对其弯曲、扭转和轴向振动模态进行理论解析。为了验证理论分析方法的准确性,对双金属复合翅片管的振动模态进行了实验测试和有限元分析。研究了翅片几何参数对双金属复合翅片管振动频率的影响规律。结果表明,对于矩形翅片形式的钢铝双金属翅片管,其弯曲、扭转和轴向振动频率均随翅片高度和翅片厚度的增大而减小,随翅片间距的增大而增大。

  7. φ7 mm管翅式换热器的翅片孔直径优化%Optimization of fin-hole diameter for φ7 mm finned-tube heat exchanger

    Institute of Scientific and Technical Information of China (English)

    钟明生; 倪雪辉; 黄起建

    2016-01-01

    通过对过盈量的分析,设计与φ7 mm内螺纹铜管配合的几种翅片孔直径的换热器,分析对比换热器的穿管阻力、U形管报废率、穿管效率以及换热能力,发现在翅片孔直径为7.27 mm时,以上4项参数能够达到最佳配合。并对胀后铜管受力变形、铜管外径、齿形变化及翅片间距分布进行分析。%Through the analysis on the magnitude of interference ,the heat exchangers with several different fin‐hole diameters suited to φ7 mm inner grooved copper tube are de‐signed .Through the analysis and comparison of the heat exchanger’s tube‐inserting resist‐ance ,U‐tube scrap rate ,tube‐inserting efficiency and heat transfer capability ,it’ s found that w hen the fin‐hole diameter is 7 .27 mm ,above four items can achieve the best fit .In addition ,the force deformation of the copper tube ,the diameter of the copper tube ,the change of the tooth profile and the distribution of the fin spacing for the expanded copper tube are analyzed .

  8. 侧置梯形翼翅片管换热器流动与传热特性%Flow and Heat Transfer Analysis of Fin-and-tube Heat Exchangers With Side-mounted Trapezium Winglets

    Institute of Scientific and Technical Information of China (English)

    苏石川; 李光琛; 陈明华; 张旭; 王浩东

    2012-01-01

    RNG k-ε model and SIMPLE algorithm were carried out to study the flow and heat transfer characteristics of fin-and-tube heat exchanger with side-mounted trapezoidal winglet vortex generators and flat fin-and-tube heat exchanger in the in-lined and staggered arrangement for the design and development of one high performance fin-and-tube heat exchanger. The results show that the performance factor of fin-and-tube heat exchanger with side-mounted trapezoidal winglets vortex generators in-lined arrangement is improving from 9.43% to 22.67%, while for staggered arrangement, the integrated performance factor is increasing from 4.89% to 14.87% within the Reynolds number range of 500 to 4 000. The side-mounted trapezoidal winglet vortex generators can effectively improve the interoperability of temperature field and velocity field and enhance its heat transfer capacity. The results also provide a reference for the design of high performance heat transfer device.%针对某翅片管换热器的设计开发,应用RNGκ-ε模型及SIMPLE算法,研究了侧置梯形翼纵向涡发生器的翅片管换热器和平直翅片管换热器在顺排和叉排两种排列方式下其流动与换热耦合特性.在雷诺数500~4000的范围内,采用侧置梯形翼涡流发生器,顺排布置时,翅片管换热器综合性能因子提高了9.43%~22.67%,叉排布置时,综合性能因子提高了4.89%~14.87%.研究结果表明,侧置梯形翼涡流发生器可以有效地改善温度场和速度场的协同性,提高其换热能力,为设计高性能换热装置提供了参考.

  9. Creatine supplementation improves the anaerobic performance of elite junior fin swimmers.

    Science.gov (United States)

    Juhász, Imre; Györe, I; Csende, Zs; Rácz, L; Tihanyi, J

    2009-09-01

    The objective of this study was to determine whether creatine supplementation (CrS) could improve mechanical power output, and swimming performance in highly trained junior competitive fin swimmers. Sixteen male fin swimmers (age:15.9+/-1.6 years) were randomly and evenly assigned to either a creatine (CR, 4x5 g/day creatine monohydrate for 5 days) or placebo group (P, same dose of a dextrose-ascorbic acid placebo) in a double-blind research. Before and after CrS the average power output was determined by a Bosco-test and the swimming time was measured in two maximal 100 m fin swims. After five days of CrS the average power of one minute continuous rebound jumps increased by 20.2%. The lactate concentration was significantly less after 5 minutes restitution at the second measurement in both groups. The swimming time was significantly reduced in both first (pre: 50.69+/-1.41 s; post: 48.86+/-1.34 s) and second (pre: 50.39+/-1.38 s; post: 48.53+/-1.35 s) sessions of swimming in CR group, but remained almost unchanged in the P group.The results of this study indicate that five day Cr supplementation enhances the dynamic strength and may increase anaerobic metabolism in the lower extremity muscles, and improves performance in consecutive maximal swims in highly trained adolescent fin swimmers.

  10. Design Features of the Separate Effect Test Facility for a Forced-Draft Sodium-to-Air Heat Exchanger (FHX) with Helical Finned Tubes

    Energy Technology Data Exchange (ETDEWEB)

    Kim, Hyungmo; Eoh, Jaehyuk; Ko, Yung Joo; Cho, Youngil; Kim, Jong-Man; Lee, Hyeong-Yeon; Jeong, Ji-Young [Korea Atomic Energy Research Institute, Daejeon (Korea, Republic of)

    2015-10-15

    A sodium-cooled fast reactor (SFR) is one of the most promising options to pursue these purposes, and the Korea Atomic Energy Research Institute (KAERI) is currently developing a PGSFR (Prototype Gen-IV Sodium-cooled Fast Reactor) with a pool-type reactor vessel. Among the many components in an SFR, a decay heat removal system (DHRS) is very important for a safety of nuclear power plants. The PGSFR adopted two different kinds of DHRS: an active and passive DHRS, and the decay heat from the primary sodium pool is moved to the two kinds of sodium-to-air heat exchangers as ultimate heat sinks through sodium-to-sodium decay heat exchangers (DHX). To verify the cooling performances and thermal-hydraulic characteristics of this type of heat exchanger, a separate effect sodium test facility named as SELFA (Sodium thermal-hydraulic Experiment Loop for Finned-tube sodium-to-Air heat exchanger) is being developed. The purposes of SELFA are verification and validation of the design code for FHX. For this, scales and configurations of SELFA are carefully defined as similarity with the FHX in the PGSFR. In this paper, we propose the key design features of SELFA including the model FHX (M-FHX) unit. To verify and validate a design code of the FHX in PGSFR, a separate effect test facility called as SELFA has being developed in KAERI.

  11. Numerical Simulation on Fin Efficiency of Tube-and-Fin Heat Exchanger Based on Field Synergy Principle%基于场协同理论的管翅式换热器翅片效率的数值模拟研究

    Institute of Scientific and Technical Information of China (English)

    张艳霞; 张红; 陶汉中

    2011-01-01

    In this paper,a three-dimensional numerical study was performed for analyzing the laminar fluid flow and heat transfer of tube-and-fin heat exchanger with flat fins. Under the conditions of considering and neglecting the fin efficiency,the simulation results were compared. In detail,the effects of Reynolds number on heat transfer rate,Nusselt number and intersection angle for two conditions were discussed, also the numerical results were analyzed from the viewpoint of field synergy principle. Furthermore, six different values of Reynolds number ranged from 200 to 1 700 were investigated. The results showed that when fin efficiency was not considered, the heat transfer rate increased by 3.44% ,4.76% ,7.48% , 12.68% , 16.04% and 19. 56% , respectively. With the increase of Reynolds number, the effect of fin efficiency on simulation results would be greater,that meant the fin efficiency could not be neglected under high Reynolds number conditions. In addition,the fin efficiency was calculated under different Reynolds number values according to its basic definition, hence a new idea for fin efficiency calculation was proposed.%本文对平直翅片管翅式换热器在考虑翅片效率和不考虑翅片效率2种情况下分别进行了层流状态下的流动和换热的三维数值模拟,研究了2种情况下Re数对换热量、Nu数及协同角的影响,并从场协同角度进行了分析.结果表明,Re数取200~1 700范围内的6个不同值,在不考虑翅片效率时,换热量分别增大了3.44%、4.76%、7.48%、12.68%、16.04%和19.56%.随着Re数的增大,翅片效率对模拟结果的影响也会增大,即在高Re数下不可忽视翅片效率对结果的影响.本文还从翅片效率的根本定义出发,得出了不同Re数下的翅片效率,为计算翅片效率提供了一个新的思路.

  12. Calculation Method of Finned Tube Condensing Heat Exchanger for Natural Gas Water Heater%天然气热水器翅片式冷凝换热器的计算方法

    Institute of Scientific and Technical Information of China (English)

    崔永章; 钱申贤

    2000-01-01

    分析了冷凝翅片换热器传热过程和主要参量,提出了天然气热水器冷凝翅片换热器的设计方法。%On the basis of theory analysis of heat transfer process and major parameters in finned tube condensing heat exchanger, a method is derived for calculating heat exchange of condensing finned tube heat exchanger.

  13. Performance of multi tubes in tube helically coiled as a compact heat exchanger

    Science.gov (United States)

    Nada, S. A.; El Shaer, W. G.; Huzayyin, A. S.

    2014-12-01

    Multi tubes in tube helically coiled heat exchanger is proposed as a compact heat exchanger. Effects of heat exchanger geometric parameters and fluid flow parameters; namely number of inner tubes, annulus hydraulic diameter, Reynolds numbers and input heat flux, on performance of the heat exchanger are experimentally investigated. Different coils with different numbers of inner tubes, namely 1, 3, 4 and 5 tubes, were tested. Results showed that coils with 3 inner tubes have higher values of heat transfer coefficient and compactness parameter (bar{h} Ah ). Pressure drop increases with increasing both of Reynolds number and number of inner tubes. Correlations of average Nusselt number were deduced from experimental data in terms of Reynolds number, Prandtl number, Number of inner coils tubes and coil hydraulic diameter. Correlations prediction was compared with experimental data and the comparison was fair enough.

  14. Desain Compact Heat Exchanger Tipe Fin And Tube Sebagai Alat Pendingin Motor Pada Boiler Feed Pump. Studi Kasus Pada Sebuah Perusahaan Pembangkit Tenaga Listrik

    Directory of Open Access Journals (Sweden)

    Luki Apriliasari

    2013-09-01

    Full Text Available Motor listrik penggerak boiler feed pump harus bekerja secara kontinyu, dan hanya boleh mati pada saat dilakukan maintenance, apabila tidak diberikan pendinginan maka akan terjadi overheating dan menyebabkan kerusakan pada motor. Hal ini sering terjadi di PLTU, motor listrik hanya didinginkan dengan dialiri udara bebas. System ini memiliki keterbatasan yaitu kotoran yang terkandung di udara bisa menempel di dinding motor, justru menyebabkan panas dalam motor tidak keluar dengan maksimal. Untuk mengatasi keterbatasan tersebut, maka diusulkan suatu metode pendinginan yaitu dengan mendesain heat exchanger tipe compact (fin and tube. Data – data operasi diambil dari suatu perusahaan pembangkit tenaga listrik yang dijadikan obyek study. Perhitungan desain heat exchanger dengan metode ∆TLMTD. Setelah mendapat dimensi yang sesuai dengan panas yang akan didinginkan, maka dilakukan analisa performansi yaitu nilai effectiveness terhadap perubahan beban. Hasil yang didapatkan dari penyelesaian study kasus ini adalah dimensi compact heat exchanger yang memiliki spesifikasi sesuai surface 7.75-5/8T dari Kays and London dengan panjang fin 1 meter, lebar fin 0,3 m, dan panjang tube 1 meter. Hasil analisa performansi (effectiveness terhadap variasi beban yaitu semakin tinggi pembebanan maka nilai effectiveness juga semakin tinggi.

  15. Improving the performance of photomultiplier tubes

    Energy Technology Data Exchange (ETDEWEB)

    Harmer, S W [Department of Engineering and Technology, Manchester Metropolitan University, Manchester M1 5GD (United Kingdom); Townsend, P D, E-mail: pdtownsend@googlemail.co [Science and Technology, University of Sussex, Brighton BN1 9QH (United Kingdom)

    2010-10-20

    Photomultipliers are ubiquitous detectors of low level light signals, but their performance is limited by the complexity of photocathode technology. Two contributory problems are that light is lost both by surface reflection and by transmission through the photocathode layer. Knowledge of the dielectric constants has allowed predictive modelling of the reflectivity and absorption of the light as a function of angle of incidence, cathode thickness and polarization. The predictions have stimulated designs of extremely simple and very low cost retrofit approaches to improve the overall effectiveness of photomultipliers. One simple design presented here exploits signal that is normally lost by the surface reflection. A simple external conical torch reflector is clipped over the photomultiplier end face. The reflector raised the efficiency of an S20 multialkali photocathode by between 20% and 10% across the blue to red spectral range. An alternative semi-cylindrical glass coupler has improved the absorption efficiency by allowing the input signal to arrive at 60{sup 0} incidence to the photocathode surface, rather than normal incidence as in the standard head-on geometry. Enhancements are from 30% to 500% across the spectral range. The greater gains are at long wavelengths, and so are particularly valuable as this is the region of lowest quantum efficiency. The latter high-incidence angle approach, when applied to a low-efficiency C grade tube, has raised the performance to greater than the best of the A grade tubes, as used in the normal head-on operation. Both methods are equally applicable to other cathode compositions.

  16. Thermal and Fluid Dynamic Performance of Pin Fin Heat Transfer Surfaces

    OpenAIRE

    Sahiti, Naser

    2006-01-01

    This thesis is organized into nine Chapters. Chapter 2 gives an overview of some highly effec-tive heat transfer surfaces used basically for the enhancement of single-phase convective heat transfer in the air conditioning, refrigeration, unit air heater and automobile industries. It follows the analysis of basic parameters that influence the performance of the fins and at the end a rela-tively simple analytical method for the assessment of the order of the magnitude of heat transfer enhanceme...

  17. The performance of a new gas to gas heat exchanger with strip fin

    NARCIS (Netherlands)

    Wang, J.; Hirs, G.G.; Rollmann, P.

    1999-01-01

    A compact gas to gas heat exchanger needs large heat transfer areas on both fluid sides. This can be realised by adding secondary surfaces. The secondary surfaces are plate fin, strip fin, and louvered fin, etc. The fins extend the heat transfer surfaces and promote turbulence. This paper presents

  18. A novel 1D/2D model for simulating conjugate heat transfer applied to flow boiling in tubes with external fins

    Science.gov (United States)

    Ocłoń, Paweł; Łopata, Stanisław; Nowak, Marzena

    2015-04-01

    This study presents a novel, simplified model for the time-efficient simulation of transient conjugate heat transfer in round tubes. The flow domain and the tube wall are modeled in 1D and 2D, respectively and empirical correlations are used to model the flow domain in 1D. The model is particularly useful when dealing with complex physics, such as flow boiling, which is the main focus of this study. The tube wall is assumed to have external fins. The flow is vertical upwards. Note that straightforward computational fluid dynamics (CFD) analysis of conjugate heat transfer in a system of tubes, leads to 3D modeling of fluid and solid domains. Because correlation is used and dimensionality reduced, the model is numerically more stable and computationally more time-efficient compared to the CFD approach. The benefit of the proposed approach is that it can be applied to large systems of tubes as encountered in many practical applications. The modeled equations are discretized in space using the finite volume method, with central differencing for the heat conduction equation in the solid domain, and upwind differencing of the convective term of the enthalpy transport equation in the flow domain. An explicit time discretization with forward differencing was applied to the enthalpy transport equation in the fluid domain. The conduction equation in the solid domain was time discretized using the Crank-Nicholson scheme. The model is applied in different boundary conditions and the predicted boiling patterns and temperature fields are discussed.

  19. 三种三角翼纵向涡翅片管换热器流动传热特性对比研究%Comparative study of fluid flow and heat transfer characteristics on the three kinds of fin-tube heat exchanger with delta winglets longitudinal vortex

    Institute of Scientific and Technical Information of China (English)

    刘丹丹; 吴学红; 张林; 孟浩; 吕彦力; 李芳星

    2015-01-01

    对三角翼圆形翅片管换热器、三角翼等径长椭圆形翅片管换热器和三角翼等周长椭圆形翅片管换热器的流动传热性能分别进行了数值研究.结果表明:三角翼等周长椭圆形翅片管换热器温度场和速度场分布最为均匀,换热效果最好;三角翼等周长椭圆形翅片管换热器奴塞尔数(Nu)最大,比三角翼圆形翅片管换热器增大2.2%~6.1%,比三角翼等径长椭圆形翅片管换热器增大6.5%~8.3%,比平翅片管换热器增大29.1%~ 33.5%;从综合传热性能分析,三角翼纵向涡椭圆形翅片管换热器适合于中等及较大雷诺数(Re)工况.%In the present study,the heat transfer and fluid flow characteristics of fin-tube heat exchangers of circular-tube,equal-diameter elliptic-tube and equal-perimeter elliptic-tube with delta winglets longitu-dinal vortex was presented based on the numerical simulation. The result showed that the temperature and velocity field of equal-perimeter elliptic-tube fin heat exchanger more uniform,and its heat transfer per-formance was the best,and the Nu number of equal-diameter elliptic-tube fin heat exchanger was the lar-gest,which was 2. 2% ~ 6. 1% higher than that of circular-tube heat exchanger with delta winglets, 6. 5% ~ 8. 3% higher than that of equal-radius elliptic-tube heat exchanger and with delta winglets and 29. 1% ~ 33. 5% higher than that of flat fin-tube heat exchanger. Considering from the overall perform-ance,the delta winglets longitudinal vortex oval fin-tube heat exchanger fit for moderate and high Reynolds numbers.

  20. Heat transfer and pressure drop of surfactant solutions at crossflown finned helical tubes. Waermeuebergang und Druckverlust waessriger Tensidloesungen an einer querangestroemten berippten Rohrwendel

    Energy Technology Data Exchange (ETDEWEB)

    Weber, M. (Huels AG, Marl (Germany)); Kleuker, H.H.; Steiff, A.; Weinspach, P.M. (Dortmund Univ. (Germany). Lehrstuhl fuer Thermische Verfahrenstechnik)

    1992-09-01

    The addition of suitable drag reducers to water in district heating networks either reduces the pressure drop significantly or the electrical power consumption of the conveying pump can be reduced at the same flow rate. New surfactant additive systems accomplish the requirements on the thermal and mechanical capacitance of district heating systems. One of the important aspects for the application of surfactant solutions is the influence on the heat transfer in the installed heat exchangers in district heating networks. In earlier publications heat transfer and pressure drop of surfactant solutions in straight pipes and in helical tubes have been discussed. Developing from the scientific findings heat transfer and pressure drop at crossflown finned helical tubes were investigated in this work. The main purpose is the presentation of the occurred effects of drag reducing solutions. Due to the complex flow conditions a prediction could not be developed as yet. (orig.).

  1. Numerical Simulation of Heat Transfer Coefficient on the Fin Side Surface in Circular Tube Bank Fin Heat Exchanger%圆管管翅式换热器肋侧换热系数的数值求解方法

    Institute of Scientific and Technical Information of China (English)

    苏梅; 林志敏; 王良璧

    2012-01-01

    本文以空气和水为流动介质,在空气进口流速um=1—6m/s的范围内,在适体坐标系下,采用耦合数值计算的方法,对圆管管翅式换热器肋侧换热系数进行数值求解,并与实验值相比较。结果表明本文提出的采用换热器总传热系数K1求解得到的肋侧换热系数与实验值最为接近,从而验证了本文提出的数值方法的准确性和可靠性。%The heat transfer coefficient on the fin side surface in circular tube bank fin heat exchanger was studied by using the conjugated simulation method in body-fitted coordinate system with the inlet air flow rate ranging from 1 m/s to 6 m/s in this paper. The numerical results were compared with the experimental results, and the discrepancies were presented in this paper. The results reveal that heat transfer coefficient on the fin side surface obtained by using the overall heat transfer coefficient K1 agrees well with the experimental results, so the accuracy and reliability of this numerical method proposed in this paper can be verified.

  2. Performance of a tapered pulse tube

    Energy Technology Data Exchange (ETDEWEB)

    Swift, G.; Allen, M.; Woolan, J.J. [Cryenco Inc., Denver, CO (United States)

    1998-02-01

    In a well instrumented pulse tube refrigerator having 1,500 W of cooling power at 125 K, the authors have measured the figure of merit of a tapered pulse tube at several operating points. At operating points near the operating point for which the taper was designed, the figure of merit is 0.96. This is close to the theoretical optimum figure of merit 0.97 calculated for this pulse tube considering only two loss mechanisms: heat conduction in the metal pulse tube wall and ordinary thermoacoustic heat transport in the gas within a few thermal penetration depths of the wall. At operating points farther from the design operating point, the measured figure of merit is much lower, as streaming driven convection adds a third loss mechanism.

  3. Steam condensation on finned tubes, in the presence of non-condensable gases and aerosols: Influence of impaction, diffusiophoresis and settling on aerosol deposition

    Energy Technology Data Exchange (ETDEWEB)

    Munoz-Cobo, J.L. [Polytechnic University of Valencia, Department of Chemical and Nuclear Engineering, Camino de Vera 14, 46022 Valencia (Spain) and Institute for Energy Engineering, Polytechnic University of Valencia, Camino de Vera 14, 46022 Valencia (Spain)]. E-mail: jlcobos@iqn.upv.es; Pena, J. [Polytechnic University of Valencia, Department of Applied Mathematics, Camino de Vera 14, 46022 Valencia (Spain); Herranz, L.E. [CIEMAT, Department of Nuclear Fission, Avenida Complutense 22, Madrid 28040 (Spain); Perez-Navarro, A. [Institute for Energy Engineering, Polytechnic University of Valencia, Camino de Vera 14, 46022 Valencia (Spain)

    2005-05-01

    This paper presents a mechanistic model to predict the steam condensation on containment finned tube heat exchangers in the presence of non-condensable gases (NC) and aerosols. The total thermal resistance from the bulk gas to the coolant is formulated as a parallel combination of the convective and condensation gas resistances coupled in series to those of condensate layer, the aerosol fouling layer, the wall, and the coolant. The condensate layer thermal resistance is calculated by means of an Adamek-based condensation model. The aerosol fouling layer is computed based on diffusiophoresis, settling and impaction mechanisms. The gas mixture (steam plus NC) thermal resistance is formulated based on a diffusion layer modeling. Finally, this paper presents a Montecarlo method implemented in the FORTRAN code TAEROSOL that is able to compute the amount of aerosol mass that is deposited by impaction on the top of the finned tubes. The model results are compared with the available experimental data of the CONGA European project.

  4. Thermal performance of plate-fin heat exchanger using passive techniques: vortex-generator and nanofluid

    Science.gov (United States)

    Khoshvaght-Aliabadi, Morteza

    2016-04-01

    This experimental study investigates the effects of vortex-generator (VG) and Cu/water nanofluid flow on performance of plate-fin heat exchangers. The Cu/water nanofluids are produced by using a one-step method, namely electro-exploded wire technique, with four nanoparticles weight fractions (i.e. 0.1, 0.2, 0.3, and 0.4 %). Required properties of nanofluids are systematically measured, and empirical correlations are developed. A highly precise test loop is fabricated to obtain accurate results of the heat transfer and pressure drop characteristics. Experiments are conducted for nanofluids flow inside the plain and VG channels. Based on the experimental results, utilizing the VG channel instead of the plain channel enhances the heat transfer rate, remarkably. Also, the results show that the VG channel is more effective than the nanofluid on the performance of plate-fin heat exchangers. It is observed that the combination of the two heat transfer enhancement techniques has a noticeably high thermal-hydraulic performance, about 1.67. Finally, correlations are developed to predict Nusselt number and friction factor of nanofluids flow inside the VG channel.

  5. Evacuated-tube solar collector--performance evaluation

    Science.gov (United States)

    1980-01-01

    Report gives thermal performance test procedures and results for commercially produced, water-filled, 8-tube collectors. Tests include efficiency, time constant for temperature drop after solar flux is cut, change in efficiency as function of sun angle, and test to see if tubes break when filled with hot water.

  6. Condensation of downward-flowing zeotropic mixture HCFC-123/HFC-134a on a staggered bundle of horizontal low-finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Honda, H.; Takamatsu, H.; Takata, N. [Kyushu Univ., Kasuga, Fukuoka (Japan). Inst. of Advanced Material Study

    1999-05-01

    Experiments were conducted to obtain row-by-row heat transfer data during condensation of downward-flowing zeotropic refrigerant mixture HCFC-123/HFC-134a on a 3 x 15 (columns x rows) staggered bundle of horizontal low-finned tubes. The vapor temperature and the HFC-134a mass fraction at the tube bundle inlet were maintained at about 50 C and 9%, respectively. The refrigerant mass velocity ranged from 9 to 34 kg/m{sup 2} s, and the condensation temperature difference from 3 to 12 K. The measured distribution of the vapor mass fraction in the tube bundle agreed fairly well with that of the equilibrium vapor mass fraction. The vapor phase mass transfer coefficient was obtained from the heat transfer data by subtracting the thermal resistance of the condensate film. The heat transfer coefficient and the mass transfer coefficient decreased significantly with decreasing mass velocity. These values first increased with the row number up to the third (or second) row, then decreased monotonically with further increasing row number, and then increased again at the last row. The mass transfer coefficient increased with condensation temperature difference, which was due to the effect of suction associated with condensation. On the basis of the analogy between heat and mass transfer, a dimensionless correlation of the mass transfer coefficient for the 4th to 14th rows was developed.

  7. Experimental Study of Heat Transfer and Pressure Drop Characteristics on Shell-side of Pin-fin Tube Oil Cooler%针翅管滑油冷却器壳侧传热与阻力性能实验研究

    Institute of Scientific and Technical Information of China (English)

    石帅; 阎昌琪; 丁铭

    2013-01-01

    The comparative experimental study for one smooth tube oil cooler and three pin-fin tube oil coolers was performed by using lubricating oil as heat transfer medium . The experimental results indicate that in the range of experimental study ,total heat transfer coefficient of pin-fin tube oil coolers is about 1.4-2 times higher than that of the smooth tube oil cooler .The heat transfer and pressure drop characteristics are greatly different for different structures of pin-fin tube oil coolers .T he effects of the structure of pin-fin tube and shell-side flow path number are dominant to influence heat transfer and pressure drop characteristics of oil coolers . In the range of experimental study , large pin-fin height is conducive to the oil flow disturbance ,but not conducive to the heat transfer on the tube-base heat transfer surface of pin-fin tube;single-pass pin-fin tube oil cooler offers high total heat transfer coefficient and volumetric heat transfer capacity ,the global heat transfer performance and the friction characteristics are better than that of two-pass pin-fin tube oil cooler .%以润滑油为换热介质,对1个光管滑油冷却器和3个采用了针翅管的滑油冷却器实验体进行了对比实验研究。结果表明:在本实验范围内,针翅管滑油冷却器的总传热系数较高,是相同条件下光管滑油冷却器总传热系数的1.4~2倍;不同结构针翅管滑油冷却器的传热与阻力性能差别较大,针翅管结构参数和壳侧流程数目是影响滑油冷却器壳程传热与阻力性能的主要因素。实验范围内,较大的针翅高度有利于油流体的扰动,但不利于针翅管一次传热面处的换热;单流程结构的针翅管滑油冷却器具有较高的传热系数和单位体积换热量,其总体换热性能与阻力性能优于双流程结构的针翅管滑油冷却器。

  8. Analysis of decrease of heat exchange efficiency of inner fin tube heat exchanger%内翅片管换热器换热效率降低分析

    Institute of Scientific and Technical Information of China (English)

    张庆生

    2012-01-01

    After use for a period of inner fin tube heat exchanger, the heat exchange efficiency decreases, which is mainly attributed to followings: blocking of tube due to improper positioning between the corrugated fin and inner tube; short circuit and change of heat exchange coefficient resulted from middle pores due to thin head of the closure at one end of the inner tube; and poor soldering quality and even blocking of the passage resulted from peeling off soldered location of inner fin heat exchange tube due to incomplete cleaning of inner (outer) tube and fins. Here, the methods used in machining of inner fin heat exchange tube for eliminating the above-mentioned problems are detailed.%内翅片管换热器使用一段时间后,换热效率会降低。主要原因是:波纹型翅片与内管定位不好,引起管内堵塞;内管一端封头的头部很薄,使用一段时间后出现中孔现象,使流体短路,换热系数发生变化;内(外)管和翅片清洗不彻底,使内翅片换热管钎焊部位脱落,影响钎焊质量甚至堵塞通道。详细介绍在内翅片换热管加工过程中对上述三种问题的解决方法。

  9. NUMERICAL SIMULATION OF THE HYDRODYNAMIC PERFORMANCE OF AN UNSYMMETRICAL FLAPPING CAUDAL FIN

    Institute of Scientific and Technical Information of China (English)

    ZHANG Xi; SU Yu-min; WANG Zhao-li

    2012-01-01

    A comprehensive numerical simulation of the hydrodynamic performance of a caudal fin with unsymmetric flapping motion is carried out.The unsymmetrical motion is induced by adding a pitch bias or a heave bias.A numerical simulation program based on the unsteady panel method is developed to simulate the hydrodynamics of an unsymmetrical flapping caudal fin.A CFD code based on Navier-Stokes equations is used to analyze the flow field.Computational results of both the panel method and the CFD method indicate that the hydrodynamics are greatly affected by the pitch bias and the heave bias.The mean lateral force coefficient is not zero as in contrast with the symmetrical flapping motion.By increasing the pitch bias angle,the mean thrust force coefficient is reduced rapidly.By adding a heave bias,the hydrodynamic coefficients are separated as two parts:in one part,the amplitude is the heave amplitude plus the bias and in the other part,it is the heave amplitude minus the bias.Analysis of the flow field shows that the vortex distribution is not symmetrical,which generates the non-zero mean lateral force coefficient.

  10. 三角形纵向涡在管翅式换热器的应用及优化%Application and Optimization of Triangular Longitudinal Vortex in Fin and Tube Heat Exchangers

    Institute of Scientific and Technical Information of China (English)

    王成刚; 高兴; 刘俊; 刘慧

    2014-01-01

    The longitudinal vortex can increase heat transfer coefficient of the fin and tube heat exchanger, and the flow resistance increases slightly. In this paper, numerical simulation on the fin and tube heat exchanger with 4 kinds of different structure fins (plain fin,H3/6,H4/6 and H5/6) was carried out. The results show that the heat transfer coefficient of the fin and tube heat exchanger with the longitudinal vortex generator is obviously increased, and the highest increase reaches 49%, at the same time resistance coefficient J also has obvious increase. The resistance factor of the fin and tube heat exchanger with the longitudinal vortex H5/6 fin has minimal increase;it is almost the same with that with plain fin. Finally, it’s pointed out that the fin and tube heat exchanger with H5/6 type longitudinal vortex fin has the best comprehensive effect.%纵向涡能够在增加管翅式换热器换热系数,同时较小幅度地增加其流动阻力。本文通过对4种结构的翅片(未进行任何处理的平翅片,结构为高为H3/6、H4/6、H5/6且攻角为30°长高比为2)进行数值模拟。结果显示安装纵向涡发生器的翅片的传热系数明显增强,且最高增加49%。在换热系数增加的同时阻力系数j也有明显的增加。其中安装纵向涡H5/6型翅片的阻力因子增加最小与平翅片几乎相同。最后本文通过对综合评价因子j/f的比较得知安装H5/6型纵向涡翅片具有最好的综合效果。

  11. Heat transfer when melting in the horizontal concentric annular gap and on finned tubes. Die Waermeuebertragung beim Schmelzen im horizontalen konzentrischen Ringspalt und am Rippenrohr

    Energy Technology Data Exchange (ETDEWEB)

    Betzel, T.

    1986-01-01

    Heat transfer in melting processes has aroused a great deal of interest recently because of the possibilities of using latent heat stores. Starting from explanations of the areas of use for latent heat stores, the possible storage media and types of store construction for active heating systems, there is an introductory phenomenological description of the melting process on resting and moving bodies and a survey of the literature. The melting and solidification processes due to purely thermal conduction (on plane walls, on cylindrical surfaces, in the concentric annular gap) and the differential equations decisive for the convection melting process are then explained. The melting process in the concentric annular gap with a falling solid body and the melting process around a horizontal tube with and without axial fins were also examined (density of heat flow, rate of melting, superimposition of boundary layer, phase boundaries). (HWJ).

  12. Mathematical treatment of melting and solidification of phase change materials between circumferentially finned tubes. Analytische Behandlung des Schmelzens und Erstarrens von Latentwaermespeichermaterialien in Rippenrohrgeometrien

    Energy Technology Data Exchange (ETDEWEB)

    Heinisch, M.

    1987-01-01

    The following study deals with the theoretical investigation of heat transfer in a latent heat store. The object of the investigation is a heat exchanger element with a circumferentially finned tube, in which the space between the fins is filled with storage material. An analytical method, employing Green's function, was developed for this arrangement in order to solve the two dimensional (r,z-coordinates) transient heat conduction in inhomogenous materials with simultaneous phase change. When compared with other well-known analytical methods, the most important advantages are that the Fourier heat conduction equation and the boundary conditions at the phase front are simultaneously fulfilled by the final solution, as well as the fact that the initial temperature is independent of a given phase change temperature. A fundamental advantage can also be seen in the very small number of time steps for calculating the transient charging/discharging processes and hence shorter calculation times. Two special extreme cases were designed where the results agree well with literature data. In comparison with the numerically calculated melting and solidification behaviour only small variations were observed.

  13. Two-Phase Flow and Energy Transfer of a Non-Azeotropic Mixture, R-407c, in a Micro-Fin Tube

    Science.gov (United States)

    Liu, Xin

    1996-11-01

    This study is to determine experimentally the two-phase flow and energy transfer characteristics of a non-azeotropic refrigerant mixture, R-407c (nominal composition: 23% R-32, 25% R-125, and 52% R-134a). R-407c is a fluid with zero ozone depletion potential and one of several alternatives to currently widely used pure refrigerant HCFC-22. As a non-azeotrope, R-407c has distinctly different characteristics from pure fluids. The phase change of a non-azeotrope under constant pressure does not proceed at a constant temperature but rather over a range of temperature. In addition, the momentum, energy transfer, and mass transfer processes are closely linked. The vapor-liquid interfacial mass transfer rate limits the evaporation or condensation rate, and in turns limits the energy transfer rate. The experiments are conducted in a test apparatus with a fluid sampling port to monitor the composition change of the mixture. The test section consists of six horizontal identical passes, constructed as double tube heat exchangers. Each pass is about 2.2 m long and are connected in order by 7.6 cm radius U-bends. The heated or cooled section of each pass is shorter than the pass length and is 1.8 meter long. The inner (mixture) tube of the test section is a nominal 3/8" inch (9.5 mm) copper tube of 0.348 mm wall thickness with 72 axial fins of 0.185 mm height on its inner surface. The apex angle of the fins is 15 deg. and the helix angle is 0. The annulus-side water, serving as heat source (evaporating mode) or heat sink (condensing mode), flows through the annular space between inner and outer tubes. The tests are conducted at 100 deg F dew point temperature and mass flux from 192,000 to 818,000 lb/hr-ft^2 for condensing, and 50 deg F dew point and mass flux from 70,000 to 394,000 lb/hr-ft^2 for evaporating. The experimental results show that, compared to R-22, two-phase flow frictional pressure gradients of R-407c are about 10% less than R-22. Due to the mass transfer

  14. Numeric Simulation on the Performance of an Undulating Fin in the Wake of a Periodic Oscillating Plate

    Directory of Open Access Journals (Sweden)

    Zhang Yong-Hua

    2013-10-01

    Full Text Available A two-dimensional unsteady computational fluid dynamics (CFD method using an unstructured, grid-based and unsteady Navier-Stokes solver with automatic adaptive re-meshing to compute the unsteady flow was adopted to study the hydrodynamic interaction between a periodic oscillating plate and a rigid undulating fin in tandem arrangement. The user-defined function (UDF program was compiled to define the undulating and oscillating motion. First, the influence of the distance between the anterior oscillating plate and the posterior undulating fin on the non-dimensional drag coefficient of the fin was investigated. Ten different distances, D=0.2L, 0.4L, 0.6L, 0.8L, 1.0L, 1.2L, 1.4L, 1.6L, 1.8L and 2.0L, were considered. The performance of the fin for different distances (D is different. Second, the plate oscillating angle (5.7o, 10 o, 20 o, 30 o, 40 o, 45 o, 50 o and frequency (0.5 Hz, 1.0 Hz, 1.5 Hz, 2.0 Hz, 2.5 Hz, 3.0 Hz, 3.5 Hz, 4.0 Hz effects on the non-dimensional drag coefficient of the fin were also implemented. The pressure distribution on the fin was computed and integrated to provide fin forces, which were decomposed into lift and thrust. Meanwhile, the flow field was demonstrated and analysed. Based on the flow structures, the reasons for different undulating performances were discussed. It shows that the results largely depend on the distance between the two objects. The plate oscillating angle and frequency also make a certain contribution to the performance of the posterior undulating fin. The results are similar to the interaction between two undulating objects in tandem arrangement and they may provide a physical insight into the understanding of fin interaction in fishes or bio-robotic underwater propulsors that are propelled by multi fins.

  15. Comparative study on thermal performance of natural draft cooling towers with finned shells

    Energy Technology Data Exchange (ETDEWEB)

    Goodarzi, Mohsen [Bu-Ali Sina Univ., Hamedan (Iran, Islamic Republic of). Dept. of Mechanical Engineering

    2016-10-15

    The cooling efficiency of natural draft cooling towers under crosswind condition should be improved. In the present research work three different externally finned shells were considered for a typical natural draft cooling tower to investigate the cooling improvement. They were numerically simulated under normal and crosswind conditions. Numerical results show that twisting four fin plates over the tower shell along the 45 peripheral angle, could improve the cooling efficiency up to 6.5 %. Because of the periodic shape of the fin plates, the cooling efficiency of the cooling tower with finned shell is less sensitive to the change of wind.

  16. 变频空调中翅片管蒸发器换热与压降特性%Heat transfer and pressure drop characteristics of fin - and - tube evaporators in variable frequency air- condition system

    Institute of Scientific and Technical Information of China (English)

    刘金平; 祁元龙; 邹永胜

    2011-01-01

    通过试验研究了变频空调系统中翅片管蒸发器管内外侧换热与压降特性,分析了压缩机频率对波纹翅片和百叶窗翅片管蒸发器管内沸腾换热系数、空气侧换热因子和摩擦因子的影响.结果表明:随着压缩机频率的增加,两种翅片的管内沸腾换热系数hi均增加;摩擦因子f都减小,百叶窗翅片的摩擦因子f是波纹翅片的2倍多;换热因子j随着压缩机频率增加而减小,波纹翅片的j因子随Re数变化明显,百叶窗翅片的则变化不大.%The heat transfer and pressure drop characteristics of outside and inside of the fin - and - tube evaporators in variable frequency air - condition system were studied. The effects of compressor frequency on inside boiling heat transfer coefficient, airside heat transfer factor and friction factor of wavy fin and louver fin were investigated. The results indicated that with the increase of compressor frequency, the boiling heat transfer coefficients in two - phase region of two fins increased. The friction factors f of both fins decreased, and the factor f of louver fin almost was two times higher than that of wavy fin. The factors j of the two fins also decreased and the factor j of wavy fin changed obviously than louver fin with the variety of Re number.

  17. Numerical analysis of flow and heat transfer behavior in fin-tube flat-plate solar collector

    Institute of Scientific and Technical Information of China (English)

    Namory Camara; LU Hui-lin

    2007-01-01

    Temperature distribution over the absorber plate of a parallel flow flat-plate solar collector is numerically analyzed. The governing differential equations with boundary conditions are solved numerically using fluent software. Effects of the inlet mass flux, inlet temperature and tube spacing on velocity and temperature distributions are discussed. Numerical results show that the distributions of velocity and temperature of fluid is unsymmetrical inside pipe.

  18. In-reactor performance of pressure tubes in CANDU reactors

    Science.gov (United States)

    Rodgers, D. K.; Coleman, C. E.; Griffiths, M.; Bickel, G. A.; Theaker, J. R.; Muir, I.; Bahurmuz, A. A.; Lawrence, S. St.; Resta Levi, M.

    2008-12-01

    The pressure tubes in CANDU reactors have been operating for times up to about 25 years. The in-reactor performance of Zr-2.5Nb pressure tubes has been evaluated by sampling and periodic inspection. This paper describes the behaviour and discusses the factors controlling the behaviour of these components in currently operating CANDU reactors. The mechanical properties (such as ultimate tensile strength, UTS, and fracture toughness), and delayed-hydride-cracking properties (crack growth rate Vc, and threshold stress intensity factor, KIH) change with irradiation; the former reach a limiting value at a fluence of Pressure tubes exhibit elongation and diametral expansion. The deformation behaviour is a function of operating conditions and material properties that vary from tube-to-tube and as a function of axial location. Semi-empirical predictive models have been developed to describe the deformation response of average tubes as a function of operating conditions. For corrosion and, more importantly deuterium pickup, semi-empirical predictive models have also been developed to represent the behaviour of an average tube. The effect of material variability on corrosion behaviour is less well defined compared with other properties. Improvements in manufacturing have increased fracture resistance by minimising trace elements, especially H and Cl, and reduced variability by tightening controls on forming parameters, especially hot-working temperatures.

  19. 直接空冷凝汽器间断波纹翅片式扁平管的数值研究%NUMERICAL STUDY OF DISCONTINUOUSLY CORRUGATED-FIN FLAT TUBES FOR DIRECT AIR COOLED CONDENSERS

    Institute of Scientific and Technical Information of China (English)

    张树国; 赵兴楼; 张艳娟

    2009-01-01

    蛇形扁平管在空冷机组的应用上取得了较好的效果,为进一步提高机组空冷凝汽器的冷凝效率,优化翅片式扁平管的结构,建立了间断波纹翅片式扁平管通道的三维物理数学模型.通过对对流换热系数、气侧换热量、流动损失的对比分析表明,间断波纹翅片式扁平管在空气侧换热量和流动损失方面比蛇形翅片式扁平管有一定的优势.%Better effectiveness had been obtained in applying snake-shaped finned flat tubes onto air-cooled units. In order to further enhance the condensing efficiency of air-cooled condensers for the said units,and optimize the structure of finned flat tubes, a three-dimenssional physico-mathematical model of a channel formulated by discontinuously corrugated fin flat tubes has been established.Through comparison and analysis of the convection heat transfer coefficient, heat amount transferred to the air side,and the flow loss etc. ,it shows that the discontinuously corrogated fin flat tubes boast cer-tain superiority in aspects of the heat amount transferred to air side and the flow loss as compared withthat of the snake-shaped finned flat tubes.

  20. On the heat transfer in the pool boiling at tightly finned steel tubes; Zum Waermeuebergang beim Behaeltersieden an eng berippten Stahlrohren

    Energy Technology Data Exchange (ETDEWEB)

    Bujok, Patrick; Wang, Yabai; Luke, Andrea [Kassel Univ. (Germany). Lehrstuhl fuer Technische Thermodynamik

    2012-07-01

    from the laboratory scale (single tube, mini-bundle) to the technical scales. On this occasion, the authors investigate the impact of tightly finned steel tubes with trapezoidal cross-sectional ribs on the heat transfer during the boiling in case of free convection over a wide range of pressures from the beginning up to the fully developed nucleate boiling. Hydrocarbons such as n-pentane and i-octane as a natural refrigerant in the process industry are used as a boiling fluid. The results of the investigations at an electrically heated and horizontally placed test tube consisting of structural steel are compared with correlations from the literature. First results from a mixture of both hydrocarbons show that the heat transfer deteriorates if only a little amount of the heavier boiling component is added.

  1. Heat transfer performance characteristics of hybrid nanofluids as coolant in louvered fin automotive radiator

    Science.gov (United States)

    Sahoo, Rashmi R.; Sarkar, Jahar

    2016-12-01

    Present study deals with the enhancement of convective heat transfer performance of EG brine based various hybrid nanofluids i.e. Ag, Cu, SiC, CuO and TiO2 in 0-1% volume fraction of Al2O3 nanofluid, as coolants for louvered fin automobile radiator. The effects of nanoparticles combination and operating parameters on thermo physical properties, heat transfer, effectiveness, pumping power and performance index of hybrid nanofluids have been evaluated. Comparison of studied hybrid nanofluids based on radiator size and pumping power has been made as well. Among all studied hybrid nanofluids, 1% Ag hybrid nanofluid (0.5% Ag and 0.5% Al2O3) yields highest effectiveness and heat transfer rate as well as pumping power. However, SiC + Al2O3 dispersed hybrid nanofluid yields maximum performance index and hence this can be recommended for best coolant. For the same radiator size and heat transfer rate, pumping power increases by using Ag hybrid nanofluids leading to increase in engine thermal efficiency and hence reduction in engine fuel consumption. For same coolant flow rate and heat transfer rate, the radiator size reduces and pumping power increases by using Ag hybrid nanofluids leading to reduction in radiator size, weight and cost.

  2. Numerical investigation for finding the appropriate design parameters of a fin-and-tube heat exchanger with delta-winglet vortex generators

    Science.gov (United States)

    Behfard, M.; Sohankar, A.

    2016-01-01

    A numerical simulation is performed to investigate the heat transfer and pressure drop characteristics of three-row inline tube bundles as a part of a heat exchanger (Re = 1000, Pr = 4.29). To enhance heat transfer, two pairs of delta winglet-type vortex generators (VGs) installed beside the first row and between the first and second rows of the tube bundles. The diameter of the second row of the tubes is chosen smaller than those of the first and third. A comprehensive study on the effects of various geometrical parameters such as transverse and longitudinal positions of VGs, length and height of VGs and angle of attack of the delta winglets is performed to augment heat transfer. Based on this study the best values of these design parameters are determined. The results showed that the best model increases the convective heat transfer ratio and thermal performance factor about 59 and 43 %, respectively, in compare with the geometry without VG.

  3. Performance of AlGaN/GaN Nanowire Omega-Shaped-Gate Fin-Shaped Field-Effect Transistor.

    Science.gov (United States)

    Lee, Dong-Gi; Sindhuri, V; Jo, Young-Woo; Son, Dong-Hyeok; Kang, Hee-Sung; Lee, Jae-Hong; Lee, Jae-Hoon; Cristoloveanu, Sorin; Im, Ki-Sik; Lee, Jung-Hee

    2016-05-01

    The AlGaN/GaN nanowire omega-shaped-gate FinFET have been successfully fabricated demonstrating much improved performance compared to conventional AlGaN/GaN MISHFET. The AlGaN/GaN omega-shaped-gate FinFET exhibited the remarkable on-state performances, such as maximum drain current of 1.1 A/mm, low on-resistance, and low current collapse compared to that of the conventional device structure. In addition, the excellent off-state performances were measured: low off-state leakage current as low as -10(-10) mA, the theoretical SS value of -62 mV/dec, and high I(ON)/I(OFF) ratio (-10(9)). Improved dc performances were obtained for omega-shaped-gate structure due to the fully depletion of the active fin body and perfectly separation of the depleted fin from the underlying thick GaN buffer layer. Furthermore, the additional reason for the enhanced device performance of the proposed device is the improved gate controllability compared to the conventional MISHFET. The proposed nano-structure device is very promising candidate for the steep switching device applications.

  4. Compact exhaust gas boilers. Investigation of heat transfer and pressure drop for serrated finned tubes. (Abbreviated edition); Kompakte avgasskjeler. Undersoekelse av varmeovergang og trykktap for serraterte finnede roer. (Forkortet utgave.)

    Energy Technology Data Exchange (ETDEWEB)

    Midtbust, H.O.; Naess, E.

    1995-07-03

    This report discusses investigations of pressure drops and heat transfer in cross-current flow of gases (air) on bundles of serrated finned tubes. For the various geometries the tube spacing and tube diameter varied while the geometry of the fins remained unchanged. Pressure drop and heat transfer were measured at six different air flows for each geometry, and the results compared with available correlations from the literature. The measurements are at variance with the correlations and indicate that the pressure loss coefficient for all the tested geometries are less influenced by the flow conditions (air speed) than predicted by the correlations. Compared with the correlation recommended by the tube supplier (Weierman`s correlation) the measured results are mostly somewhat higher than predicted for the larger air flows. The maximum observed deviation is 70%. The deviation between the published pressure loss correlations is also considerable. The heat transfer measurements agree qualitatively with the published correlations with respect to the flow conditions. Comparison with the heat transfer correlation recommended by the tube supplier indicates that the correlation over-predicts the heat transfer quite considerably. The deviation increases systematically with reduced tube diameter and with increased angle of the tube arrangement. 16 figs., 7 tabs.

  5. 双面犁法加工整体翅片管的成形数学模型%Mathematical Model of Forming Integral-fin Tubes by Double-ploughing Method

    Institute of Scientific and Technical Information of China (English)

    吴斌; 夏伟; 汤勇

    2001-01-01

    The mathematical model of forming integral-fin tubes by the double-ploughing method is established. The relationship between the geometric variables that characterize integral-fin tubes and the cutting data, tool geometry parameters is revealed theoretically. Based on this model, the optimal fin parameters for enhanced the heat transfer can be obtained. The theoretical analysis and the experiment results indicate that for a certain tool, the fin height and mean fin thickness increase with the increase of extrusion depth and feed.%建立了双面犁法加工整体翅片管的成形数学模型,推导了翅片结构参数与加工用量及刀具几何参数之间的关系,为优选翅片结构参数以达到最佳传热效果提供了理论依据。理论分析和试验结果均表明,对于某一刀具,翅片高度和平均翅厚均随挤压深度和进给量的增加而增大。

  6. Numerical Study on Flow and Heat Transfer Characteristics of Finned Tube Bundles for Air-cooled Heat Exchangers of Indirect Dry Cooling Systems in Power Plants%电站间冷系统空冷散热器翅片管束流动传热性能的数值研究

    Institute of Scientific and Technical Information of China (English)

    杨立军; 贾思宁; 卜永东; 杜小泽; 杨勇平

    2012-01-01

    空冷散热器为电站间接空冷系统的主要设备,研究空冷散热器翅片管束的流动传热特性,对于电站间冷系统的优化设计与高效运行具有重要意义.对间接空冷系统空冷散热器常用翅片管束流动传热性能进行了数值模拟研究,通过计算获得了空冷散热器冷却空气流动阻力和平均对流换热系数随迎面风速的变化规律,拟合得到了摩擦因子与努赛尔特数随雷诺数的变化关系.利用对流换热的综合性能评价标准(performance evaluation criteria,PEC),即Nu/f1/3,对6种翅片管束的流动传热性能进行了比较.结果表明,随迎面风速增加,空气对流换热增强,压降增加,翅片管的对流换热系数随之升高,摩擦因子降低,但是换热系数的增加幅度小于压降的增加幅度.Forgo型翅片管束综合流动传热性能优于椭圆型管束.本文研究结果为电站间冷系统空冷散热器的选型和优化设计提供了一定的理论依据.%Air-cooled heat exchanger is one of the main components of the indirect dry cooling system in a power plant. It is of benefit to the optimal design and operation of indirect dry cooling system to clarify the flow and heat transfer characteristics of air-cooled finned tube heat exchangers. The thermo-flow performances of the commonly used finned tube bundles in air-cooled heat exchangers were investigated by a numerical simulation. The variations of the flow resistance and average convection heat transfer coefficient of cooling air through the finned tube heat exchanger with the windward velocity were presented. The correlating equations of the friction factor versus Reynolds number, and the Nusselt number versus Reynolds number were fitted. On the basis of the performance evaluation criteria for convection heat transfer, the expression of Nu/f1/3 was applied to the thermo-flow performances prediction for six finned tube bundles. The results show that as the windward velocity increases

  7. Characteristics of the Initial Stage of CaCO3 Crystallization Fouling on Two Kinds of Oblique Fin Tube%两种斜翅管表面碳酸钙垢初始阶段结垢特性

    Institute of Scientific and Technical Information of China (English)

    盛健; 张华; 赵萍

    2014-01-01

    To investigate the effect of CaCO3 concentration and velocity on CaCO3 scaling fouling process on plain,straight oblique and saw-tooth oblique fin tubes,experiments were done at different CaCO3 concentration,velocity and surface parameter of the three kinds of tubes.The results show that the homogeneous nucleation rate and the growing rate both increase when CaCO3 concentration increases.This makes the scaling particle concentration and fouling ion concentration increase,the former leads to more scaling on tubes and the later enlarges the heterogeneous nucleation rate and growing rate.Higher velocity decreases the nucleation of scaling,scaling crystal and fouling resistance,but it can prolong the induction period.Higher velocity increases nucleation rates on straight oblique fin tube and saw-tooth oblique fin tube,but the induction period extends and the mass of scaling and fouling resistance decrease.Straight oblique fin tube and saw-tooth oblique fin tube have bigger heat transfer coefficient than plain tube under both clean and fouling conditions in despite of smaller fouling resistance and a little more scaling.Under the same condition,saw-tooth oblique fin tubes have bigger heat transfer coefficient and fouling mass than straight oblique fin tubes,but the total heat transfer coefficient is bigger than that of straight oblique fin tubes.%进行了3种强化管在不同碳酸钙溶液浓度和流速下的动态结垢实验,得到碳酸钙浓度、流速和不同管型对碳酸钙析晶垢结垢过程的影响。结果表明,碳酸钙浓度增大,使溶液中均相成核速率和所形成晶核的生长速率增大,使溶液换热表面界面的污垢晶粒浓度和成垢离子浓度均增大,前者使更多的污垢附着换热面,而后者使表面异相成核速率和生长速率增大。流速增大,使光管表面形成的晶核、污垢晶体和污垢热阻均减少,而诱导期延长;使平直和锯齿斜翅管初始成核增多,但诱

  8. A Comparative Study of Conventional and Tip-Fin Propeller Performance

    DEFF Research Database (Denmark)

    Andersen, Poul

    1997-01-01

    During more than a decade several attempts have been made to obtain higher propeller efficiencies by radically modifying the geometry in the tip region of the blade. In the tip-fin propeller a tip fin or winglet is attached to the blade tip and integrated into the blade in such a way that the blade...... tip is softly curved towards the suction side.Whereas the developments previously have been concentrated mainly on increasing the efficiency of the propeller, the emphasis of current efforts has been on both high efficiency as well as good cavitation properties. This has resulted in a design...... with a combination of skew and tip fin. To evaluate the design, open-water, self-propulsion and cavitation model tests have been carried out. The tests are done for the conventional propeller originally designed for the ship and for a tip-fin propeller designed for the same ship under the same operation conditions...

  9. Global Analysis and Structural Performance of the Tubed Mega Frame

    OpenAIRE

    Zhang, Han

    2014-01-01

    The Tubed Mega Frame is a new structure concept for high-rise buildings which is developed by Tyréns. In order to study the structural performance as well as the efficiency of this new concept, a global analysis of the Tubed Mega Frame structure is performed using finite element analysis software ETABS. Besides, the lateral loads that should be applied on the structure according to different codes are also studied. From the design code study for wind loads and seismic design response spectrum...

  10. Performance of double -pass solar collector with CPC and fins for heat transfer enhancement

    Science.gov (United States)

    Alfegi, Ebrahim M. A.; Abosbaia, Alhadi A. S.; Mezughi, Khaled M. A.; Sopian, Kamaruzzaman

    2013-06-01

    The temperature of photovoltaic modules increases when it absorbs solar radiation, causing a decrease in efficiency. This undesirable effect can be partially avoided by applying a heat recovery unit with fluid circulation (air or water) with the photovoltaic module. Such unit is called photovoltaic / thermal collector (pv/t) or hybrid (pv/t). In this unit, photovoltaic cells were pasted directly on the flat plate absorber. An experimental study of a solar air heater with photovoltaic cell located at the absorber with fins and compound parabolic collector for heat transfer enhancement and increasing the number of reflection on the cells have been conducted. The performance of the photovoltaic, thermal, and combined pv/t collector over range of operating conditions and the results was discussed. Results at solar irradiance of 500 W/m2 show that the combined pv/t efficiency is increasing from 37.28 % to 81.41 % at mass flow rates various from 0.029 to 0.436 kg/s.

  11. 圆弧形三角翼翅片管换热器流动与传热特性的数值模拟%Flow and Heat-transfer Characteristics of Finned Tube Heat Exchanger with Arc Delta Winglets

    Institute of Scientific and Technical Information of China (English)

    苏石川; 李光琛; 陈明华; 张旭; 王浩东

    2013-01-01

    3D numerical simulations were performed to investigate the flow and heat transfer coupling characteristics of finned tube heat exchangers with arc or straight delta-winglet vortex generators. Results show that when the Re is in 500-5 000, both the arc and straight delta winglets can enhance the heat transfer of heat exchanger. The enhancement effect of arc delta winglet is slightly weaker than the straight one, but its flow resistance is obviously smaller. In comparison with straight delta-winglet exchanger, the comprehensive performance of arc delta-winglet exchanger is 7. 3%-H. 5% and 8. 2%-9. 5% higher respectively in the case of aligned and staggered arrangement of heat-exchanger tube. The vortex generator can enable fluid to generate a velocity component perpendicular to the fin direction and improve the cooperativity between velocity filed and temperature field, and therefore the heat-transfer performance is enhanced.%采用三维数值模拟方法对加装圆弧形三角翼和直三角翼涡流发生器的翅片管换热器的流动与传热耦合特性进行了研究.结果表明:Re在500~5 000时,圆弧形三角翼和直三角翼均可以提高换热器的传热能力,圆弧形三角翼强化传热的效果略低于直三角翼,但其流动阻力明显小于直三角翼;换热管顺排布置时,圆弧形三角翼换热器的综合性能比直三角翼提高了7.3%~11.5%;换热管叉排布置时,圆弧形三角翼换热器的综合性能比直三角翼提高了8.2%~9.5%;涡流发生器可以使流体产生垂直于翅片方向的速度分量,改善流场中速度场和温度场的协同性,从而增强传热能力.

  12. Heat exchanger performance calculations for enhanced-tube condenser applications

    Energy Technology Data Exchange (ETDEWEB)

    Rabas, T.J.

    1992-07-01

    The lack of a prediction method is sometimes used for the rejection of enhanced tubes for some condenser applications even though there is ample data from single-tube condensing experiments. Three methods are discussed that can be used to rate and/or size these multitube units based on the single-tube experimental results. The Kern vertical-number correction appears to be quite adequate for most operating conditions, the exceptions being large sizes and/or deep vacuum operation. The bundle-factor method is preferred for these applications; however, field test results are required to obtain this factor. If performance data are not available, pointwise or numerical methods are required but special care must be taken to insure that the adverse effects of noncondensable gas pockets and the saturation-temperature depression are properly addressed.

  13. Heat exchanger performance calculations for enhanced-tube condenser applications

    Energy Technology Data Exchange (ETDEWEB)

    Rabas, T.J.

    1992-01-01

    The lack of a prediction method is sometimes used for the rejection of enhanced tubes for some condenser applications even though there is ample data from single-tube condensing experiments. Three methods are discussed that can be used to rate and/or size these multitube units based on the single-tube experimental results. The Kern vertical-number correction appears to be quite adequate for most operating conditions, the exceptions being large sizes and/or deep vacuum operation. The bundle-factor method is preferred for these applications; however, field test results are required to obtain this factor. If performance data are not available, pointwise or numerical methods are required but special care must be taken to insure that the adverse effects of noncondensable gas pockets and the saturation-temperature depression are properly addressed.

  14. 螺旋管圈水冷壁鳍片焊缝专用超声检测技术%The Special Ultrasonic Testing Technology for Fins Weld of Spiral Water Cooled Wall Tube

    Institute of Scientific and Technical Information of China (English)

    严祯荣; 陈学东; 罗晓明

    2015-01-01

    针对螺旋管圈水冷壁鳍片焊缝裂纹的产生特性,开发了专用微型超声波检测探头和超声波检测仪器。在刻有近似鳍片裂纹和平底孔的螺旋管圈水冷壁试件上进行了验证性检测试验。在鳍片宽度仅5 mm 的狭长检测空间,通过鳍片单一面耦合,实现了双面鳍片焊缝缺陷检测,能够方便、有效地应用到超超临界锅炉螺旋管圈水冷壁检修环节。%For features of fins crack initiation of spiral water cooled wall tube,a special miniature ultrasonic probe and ultrasonic testing instrument were developed.The confirmatory tests were carried out on specimen of spiral water cooled wall tube,which were engraved with the approximate fins weld crack and flat bottom holes.The confirmatory tests have realized detection of the double fins weld defect in the long and narrow space detection of the only 5 mm fin width,through the fins of the single surface coupling,which can be conveniently and effectively applied to the overhaul of spiral water cooled wall tube of ultra supercritical boiler.

  15. 管翅式全铝换热器在家用空调上的应用研究%Application Research on Fin Tube Aluminum Exchanger Used for Room Air Conditioners

    Institute of Scientific and Technical Information of China (English)

    2012-01-01

    In this article, fin tube aluminum exchanger used for room air conditioners are studied and ana-lyzed in different aspects, including material option, experiment analysis and welding technology. Moreover, the feasibility which fin tube aluminum exchanger may be used for room air conditioners is raised.%  本文对家用空调器换热器采用管翅式全铝换热器的材料选择、试验分析、焊接工艺等进行了研究和分析,提出了管翅式全铝换热器在家用空调器上的应用可行性。

  16. Predicting optimum vortex tube performance using a simplified CFD model

    Energy Technology Data Exchange (ETDEWEB)

    Karimi-Esfahani, M; Fartaj, A.; Rankin, G.W. [Univ. of Windsor, Dept. of Mechanical, Automotive and Materials Engineering, Windsor, Ontario (Canada)]. E-mail: mki_60@hotmail.com

    2004-07-01

    The Ranque-Hilsch tube is a particular type of vortex tube device. The flow enters the device tangentially near one end and exits from the open ends of the tube. The inlet air is of a uniform temperature throughout while the outputs are of different temperatures. One outlet is hotter and the other is colder than the inlet air. This device has no moving parts and does not require any additional power for its operation other than that supplied to the device to compress the inlet air. It has, however, not been widely used, mainly because of its low efficiency. In this paper, a simplified 2-dimensional computational fluid dynamics model for the flow in the vortex tube is developed using FLUENT. This model makes use of the assumption of axial symmetry throughout the entire flow domain. Compared to a three-dimensional computational solution, the simplified model requires significantly less computational time. This is important because the model is to be used for an optimization study. A user-defined function is generated to implement a modified version of the k-epsilon model to account for turbulence. This model is validated by comparing a particular solution with available experimental data. The variation of cold temperature drop and efficiency of the device with orifice diameter, inlet pressure and cold mass flow ratio qualitatively agree with experimental results. Variation of these performance indices with tube length did not agree with the experiments for small values of tube length. However, it did agree qualitatively for large values. (author)

  17. PLC在钉头管埋弧螺柱焊中的应用%The Application of Programmable Logical Controller (PLC) in Submerged Arc Stud Welding for Pin Finned Tube

    Institute of Scientific and Technical Information of China (English)

    周拨云; 梅强

    2011-01-01

    In order to accurately control pin finned tube welding procedure, the PLC was applied into the control of pin finned tube submerged arc stud welding. This article introduced SSAW for pin finned tube composition and control requirements of welding control system, this system selected Emerson EC10-2416BTA programmable logical controller, adopted Emerson Control Start software to workout control procedure, and realized automatic welding for pin finned tube submerged arc stud welding. This system is with high efficiency energy saving, it overcomes some disadvantages of manual welding,such as great labour intensity,bad quality of welding joints and low welding efficiency,at the same time, this system can identify failure, alarm and timely deal with, so it can ensure stable welding quality.%为了对钉头管焊接过程进行精确控制,将PLC应用于钉头管埋弧螺柱焊焊接控制.介绍了钉头管埋弧螺柱焊焊接控制系统的组成及控制要求,选用了艾默生EC10-2416BTA型可编程控制器,采用艾默生编程软件Control Start编制控制程序,实现了钉头管埋弧螺柱焊的自动化焊接.该系统高效节能,并克服了手工焊劳动强度大、接头质量差、焊接效率低等缺点,具有故障诊断和报警功能,并作出相应的处理,保证稳定焊接质量.

  18. Modeling the discontinuous individual channel injection into fin-and-tube evaporators for residential air-conditioning

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Elmegaard, Brian

    2012-01-01

    secondary flow increases performance. Moreover, the paper reports on the applicability of Modelica developed models to analyze and optimize the working principle and design of expansion devices such that Modelica may be used in future development of novel discontinuous expansion devices....

  19. Friction characteristics for water-ethylene glycol mixture flow in horizontal tubes with new type of helically fins%乙二醇溶液水平新型多头内螺纹管内流阻特性

    Institute of Scientific and Technical Information of China (English)

    张吉礼; 王永辉; 马志先; 陈敬东

    2016-01-01

    建立了水平管内绝热流动阻力特性试验系统,试验研究了乙二醇溶液在两种新型多头内螺纹管内的流动特性.试验中,乙二醇体积分数为15%,两种试验管公称内径为22 mm与16 mm、螺纹头数为60头与38头、螺旋升角为45°与60°、相对粗糙高为0.022与0.053,测试段长度分别为2643 mm与2945 mm,Pr范围13.9~23.2,Re范围4000~33000.结果表明:多头内螺纹管阻力系数达到极大值之前的变化趋势与均匀粗糙管显著不同,而且无法通过既有多头内螺纹管经验模型准确描述;多头内螺纹管内达到阻力系数极大值的分界点Re为内肋结构参数的函数;入口效应对内螺纹管阻力系数的影响随Re增加而增大,传统的判别入口段可忽略的判据(l/di>60)并不适用于多头内螺纹管,尤其是在Re>20000的工况;既有多头内螺纹管经验模型适用工况条件有待进一步拓宽,多头内螺纹结构流动阻力的作用机制、阻力系数出现极大值的分界点的变化规律有待进一步试验探索.%An experiment setup was built for investigating single-phase adiabatic flow characteristics of internal helical-rib roughness. The friction characteristics for 15% (by volume) water-ethylene glycol mixture flow in three internal finned tubes (two types of new developed internal helical-fins) and a smooth tube were obtained. The parameters of test tubes are nominal inside diameters (22 mm and 16 mm), numbers of fins (60 and 38), helix angles (45° and 60°) and fin height to inside diameter ratios (0.022 and 0.053). The lengths of the internal helical-rib tubes in test section were 2643 mm and 2945 mm, respectively. The Prandtl number varied from 13.9 to 23.2 and the Reynolds number ranged from 4000 to 33000. The smooth-tube results were compared to the Filonenko equation with satisfactory agreement. The experimental results of different length and same type multi-start internal helically-finned tubes also showed that the

  20. Performance of the CMS Drift Tube Chambers with Cosmic Rays

    CERN Document Server

    Chatrchyan, S; Sirunyan, A M; Adam, W; Arnold, B; Bergauer, H; Bergauer, T; Dragicevic, M; Eichberger, M; Erö, J; Friedl, M; Frühwirth, R; Ghete, V M; Hammer, J; Hänsel, S; Hoch, M; Hörmann, N; Hrubec, J; Jeitler, M; Kasieczka, G; Kastner, K; Krammer, M; Liko, D; Magrans de Abril, I; Mikulec, I; Mittermayr, F; Neuherz, B; Oberegger, M; Padrta, M; Pernicka, M; Rohringer, H; Schmid, S; Schöfbeck, R; Schreiner, T; Stark, R; Steininger, H; Strauss, J; Taurok, A; Teischinger, F; Themel, T; Uhl, D; Wagner, P; Waltenberger, W; Walzel, G; Widl, E; Wulz, C E; Chekhovsky, V; Dvornikov, O; Emeliantchik, I; Litomin, A; Makarenko, V; Marfin, I; Mossolov, V; Shumeiko, N; Solin, A; Stefanovitch, R; Suarez Gonzalez, J; Tikhonov, A; Fedorov, A; Karneyeu, A; Korzhik, M; Panov, V; Zuyeuski, R; Kuchinsky, P; Beaumont, W; Benucci, L; Cardaci, M; De Wolf, E A; Delmeire, E; Druzhkin, D; Hashemi, M; Janssen, X; Maes, T; Mucibello, L; Ochesanu, S; Rougny, R; Selvaggi, M; Van Haevermaet, H; Van Mechelen, P; Van Remortel, N; Adler, V; Beauceron, S; Blyweert, S; D'Hondt, J; De Weirdt, S; Devroede, O; Heyninck, J; Kalogeropoulos, A; Maes, J; Maes, M; Mozer, M U; Tavernier, S; Van Doninck, W; Van Mulders, P; Villella, I; Bouhali, O; Chabert, E C; Charaf, O; Clerbaux, B; De Lentdecker, G; Dero, V; Elgammal, S; Gay, A P R; Hammad, G H; Marage, P E; Rugovac, S; Vander Velde, C; Vanlaer, P; Wickens, J; Grunewald, M; Klein, B; Marinov, A; Ryckbosch, D; Thyssen, F; Tytgat, M; Vanelderen, L; Verwilligen, P; Basegmez, S; Bruno, G; Caudron, J; Delaere, C; Demin, P; Favart, D; Giammanco, A; Grégoire, G; Lemaitre, V; Militaru, O; Ovyn, S; Piotrzkowski, K; Quertenmont, L; Schul, N; Beliy, N; Daubie, E; Alves, G A; Pol, M E; Souza, M H G; Carvalho, W; De Jesus Damiao, D; De Oliveira Martins, C; Fonseca De Souza, S; Mundim, L; Oguri, V; Santoro, A; Silva Do Amaral, S M; Sznajder, A; Fernandez Perez Tomei, T R; Ferreira Dias, M A; Gregores, E M; Novaes, S F; Abadjiev, K; Anguelov, T; Damgov, J; Darmenov, N; 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Wigmans, R; Yazgan, E; Engh, D; Florez, C; Johns, W; Pathak, S; Sheldon, P; Andelin, D; Arenton, M W; Balazs, M; Boutle, S; Buehler, M; Conetti, S; Cox, B; Hirosky, R; Ledovskoy, A; Neu, C; Phillips II, D; Ronquest, M; Yohay, R; Gollapinni, S; Gunthoti, K; Harr, R; Karchin, P E; Mattson, M; Sakharov, A; Anderson, M; Bachtis, M; Bellinger, J N; Carlsmith, D; Crotty, I; Dasu, S; Dutta, S; Efron, J; Feyzi, F; Flood, K; Gray, L; Grogg, K S; Grothe, M; Hall-Wilton, R; Jaworski, M; Klabbers, P; Klukas, J; Lanaro, A; Lazaridis, C; Leonard, J; Loveless, R; Magrans de Abril, M; Mohapatra, A; Ott, G; Polese, G; Reeder, D; Savin, A; Smith, W H; Sourkov, A; Swanson, J; Weinberg, M; Wenman, D; Wensveen, M; White, A

    2010-01-01

    Studies of the performance of the CMS drift tube barrel muon system are described, with results based on data collected during the CMS Cosmic Run at Four Tesla. For most of these data, the solenoidal magnet was operated with a central field of 3.8 T. The analysis of data from 246 out of a total of 250 chambers indicates a very good muon reconstruction capability, with a coordinate resolution for a single hit of about 260 microns, and a nearly 100% efficiency for the drift tube cells. The resolution of the track direction measured in the bending plane is about 1.8 mrad, and the efficiency to reconstruct a segment in a single chamber is higher than 99%. The CMS simulation of cosmic rays reproduces well the performance of the barrel muon detector.

  1. Thermal-hydraulic performance of oval tubes in a cross-flow of air

    Science.gov (United States)

    Hasan, Ala

    2005-06-01

    The thermal-hydraulic performance of five oval tubes is experimentally investigated and compared with that for a circular tube in a cross-flow of air. The range of Reynolds numbers ReD is approximately between 1,000 and 11,000. The nominal axis ratios R (major axis/minor axis) for three of the investigated oval tubes are 2, 3, and 4. Two other configurations of oval tubes are also tested, an oval tube R=3 with two wires soldered on its upper and lower top positions, and a cut-oval tube. The performance of the tubes is corrected for the effects of area blockage and turbulence intensity. The measurement results show that the mean Nusselt numbers NuD for the oval tubes are close to that for the circular tube for ReDthermal-hydraulic performance is indicated by the ratio NuD/Cd, which shows a better combined performance for the oval tubes.

  2. Performance evaluation of a natural-convection solar air-heater with a rectangular-finned absorber plate

    Energy Technology Data Exchange (ETDEWEB)

    Fakoor Pakdaman, M.; Lashkari, A.; Basirat Tabrizi, H.; Hosseini, R. [Department of Mechanical Engineering, Amirkabir University of Technology, Tehran (Iran, Islamic Republic of)

    2011-02-15

    This paper deals with an experimental investigation to evaluate different thermal characteristics of a natural-convection flat-plate solar air-heater with longitudinal rectangular fins array. Having determined the thermal performance of the system a Nusselt number correlation is presented for such finned duct devices. In the presented empirical model which may have industrial applications, solar radiation and ambient temperature have been considered as independent parameters. Other characteristics of the system such as different dimensionless variables, plates and outflow temperatures, efficiency, and mass flow rate have been empirically modeled based on these variables. The particular difference in this study in comparison with the other similar studies is the presentation of an empirical model for rectangular-finned solar air-heaters. This model proposes design concepts and rules of thumb, and demonstrates the calculations of the design parameters. Based on the order of magnitude analysis, solar radiation has been found to be the main parameter which characterizes the thermal behavior of the system. Besides, exergy analysis has been carried out, and optimum conditions in which the system has the highest performance have been determined. (author)

  3. Approximate formulas of number of transfer unit of U shaped fin-tube heat exchangers%U型翅片管换热器传热单元数计算式

    Institute of Scientific and Technical Information of China (English)

    吴小舟; 赵加宁

    2012-01-01

    To obtain the formulas of number of transfer unit (NTU) of U shaped fin-tube heat exchangers, a U shaped fin-tube heat exchanger is taked as research object. Approximate NTU formulas of number of transfer unit are derived by establishing heat transfer model of U shaped fin-tube when the trend of two flows in fin-tube heat exchanger is counter and parallel, respectively. Subsequently, the heat transfer coefficients of fin-tube are com- pared and analyzed by effectiveness-number of transfer unit method (e-NTU method) and logarithm mean tem- perature difference method ( LMTD method) when inlet water temperature is from 45 ℃ to 60℃ and water flow rate is from 30 kg/h to 110 kg/h. The results show that, the differenbe of the heat transfer coefficients respectively calculated by 6-NTU method and LMTD method is so small that these NTU formulas are valid.%为了得到U型翅片管换热器传热单元数计算式,以U型翅片管换热器为研究对象,通过建立翅片管换热模型,推导出了逆流和顺流2种流体流动趋势的传热单元数计算式(NTU计算式).分别采用推导出的传热单元数计算式(F—NTU法)和前人推导出的平均温差关系式(LMTD法)计算U型翅片管传热系数,并进行对比分析.结果表明,当进水温度为45~60℃,热水流量为30~110kg/h时,由ε-NTU法和LMTD法计算出来的翅片管传热系数相差很小.所推导出来的U型翅片管换热器传热单元数计算式是合理的.

  4. Application of The fin tube with the dentation spiral in HRSG of the F class gas-steam Combined Cycle%开齿螺旋鳍片管在F级燃气一蒸汽联合循环佘热锅炉中的应用

    Institute of Scientific and Technical Information of China (English)

    朱晨曦; 莫耀伟

    2005-01-01

    This text will discuss elements of take shape and characteristic of heat transfer of the fin tube of the dentation spiralattheheating surface in the gas-steam Combined Cycle Unit(390 MW)of HRSG,also analyses and investigates material of tube with performance of machine,chemistry andjointing,them arcusefor reference experiencein order to application for the fin tube of the dentation spiral in the F class gas—steam Combined Cycle of HRSG.%论述了燃气一蒸汽联合循环发电机组(350 Mw)余热锅炉受热面开齿螺旋鳍片管的成形原理和传热特性,分析和研究了管材的机械、化学、焊接性能,为开齿螺旋鳍片管在F级燃气一蒸汽联合循环余热锅炉中的应用提供借鉴经验。

  5. 基于曲线拟合优化设计肋片管换热器%Using Curve Fitting to Optimize of Fin and Tube Heat Exchanger

    Institute of Scientific and Technical Information of China (English)

    杨恒; 朱梅; 远高

    2013-01-01

      主要对等厚环肋传热过程进行数值分析,利用曲线拟合的方法计算不同肋片尺寸下的散热量和肋效率的精确解,并在金属消耗一定和散热量一定情况下,优化等厚环肋的结构。%  This thesis discusses numerical analysis the process of heat transfer by uniform annular fin, using the curve fitting method to calculate the exact solution of heat transfer and fin sufficiency under the different fin sizes, and optimize of the structure of the uniform annular fin based on the same metal consumption and the same heat transfer of a single fin.

  6. T型翅片管重沸器传热性能研究与工业应用%STUDY ON HEAT TRANSFER CHARACTERISTICS OF T-TYPE FINNED TUBE REBOILER AND ITS COMMERCIAL APPLICATION

    Institute of Scientific and Technical Information of China (English)

    梁龙虎

    2001-01-01

    Test results of heat transfer characteristics of the T-type finned tube reboiler were introduced together with its commercial application.Compared to conventional smooth tube reboiler,the heat transfer coefficient enhanced by 30%~50%.It is characterized by little occupation area,low cost and steady operation.Satisfactory results were also obtained by using the T-type finned tube to replace the smooth tube in evaporator.%介绍了T型翅片管重沸器的传热性能试验结果及其工业应用情况。T型翅片管重沸器与普通光管重沸器相比,其传热系数可提高30%~50%,而且还具有占地面积小、投资省、操作平稳等优点。T型翅片管代替光管用于蒸汽发生器,也取得了较好的效果。

  7. Performance of a lead radiator, gas tube calorimeter

    Energy Technology Data Exchange (ETDEWEB)

    Spiegel, L.; Arenton, M.; Chen, T.Y.; Conetti, S.; Cox, B.; Delchamps, S.W.; Etemadi, B.; Fortney, L.; Guffey, K.; Haire, M.

    1989-03-13

    Design and performance of a 4.2 radiation length lead-sandwich, gas tube hodoscope are discussed. The device, measuring 1 /times/ 2 m/sup 2/ in area and 12 cm in depth, was employed in Fermi National Accelerator Laboratory experiment 705. Multiple samplings of anode wires situated within three-walled aluminum tubes were used to generate an X coordinate; similarly, capacitively coupled copper-clad strips were ganged together to yield a Y coordinate. The results reviewed are based on an analysis of electron calibration data taken during a recent six-month running period. In particular, position resolution (in millimeters) is seen to be 0.8 + 3.3/..sqrt..E + 31/E for the 9.92 mm spaced wires and 0.6 + 3.2/..sqrt..E + 32/E for the 12.5 mm strips, where E represents the electron beam energy in GeV. 5 refs., 6 figs.

  8. Enhancement of acoustical performance of hollow tube sound absorber

    Science.gov (United States)

    Putra, Azma; Khair, Fazlin Abd; Nor, Mohd Jailani Mohd

    2016-03-01

    This paper presents acoustical performance of hollow structures utilizing the recycled lollipop sticks as acoustic absorbers. The hollow cross section of the structures is arranged facing the sound incidence. The effects of different length of the sticks and air gap on the acoustical performance are studied. The absorption coefficient was measured using impedance tube method. Here it is found that improvement on the sound absorption performance is achieved by introducing natural kapok fiber inserted into the void between the hollow structures. Results reveal that by inserting the kapok fibers, both the absorption bandwidth and the absorption coefficient increase. For test sample backed by a rigid surface, best performance of sound absorption is obtained for fibers inserted at the front and back sides of the absorber. And for the case of test sample with air gap, this is achieved for fibers introduced only at the back side of the absorber.

  9. Performance enhancement in uniaxially tensile stressed GeSn n-channel fin tunneling field-effect transistor: Impact of stress direction

    Science.gov (United States)

    Wang, Hongjuan; Han, Genquan; Jiang, Xiangwei; Liu, Yan; Zhang, Chunfu; Zhang, Jincheng; Hao, Yue

    2017-04-01

    In this work, the boosting effect on the performance of GeSn n-channel fin tunneling FET (nFinTFET) enabled by uniaxial tensile stress is investigated theoretically. As the fin rotates within the (001) plane, the uniaxial tensile stress is always along its direction. The electrical characteristics of tensile-stressed GeSn nFinTFETs with point and line tunneling modes are computed utilizing the technology computer aided design (TCAD) simulator in which the dynamic nonlocal band-to-band tunneling (BTBT) algorithm is employed. In comparison with the relaxed devices, tensile-stressed GeSn nFinTFETs achieve a substantial enhancement in band-to-band tunneling generation rate (G BTBT) and on-state current I ON owing to the reduced bandgap E G induced by the tensile stress. Performance improvement of GeSn nFinTFETs induced by tensile stress demonstrates a strong dependence on channel direction and tunneling modes. Under the same magnitude of stress, line-nFinTFETs obtain a more pronounced I ON enhancement over the transistors with point tunneling mode.

  10. Thermal Performance of Convective-Radiative Heat Transfer in Porous Fins

    Directory of Open Access Journals (Sweden)

    Majid SHAHBABAEI

    2014-01-01

    Full Text Available Forced and natural convection in porous fins with convective coefficient at the tips under radiation and convection effects are investigated in this paper. Aluminum and copper as fin materials are investigated. In forced and natural convection, air and water are applied as working fluids, respectively. In order to solve this nonlinear equation, Homotopy Perturbation Method (HPM and Variational Iteration Method (VIM are used. To verify the accuracy of the methods, a comparison is made to the exact solution (BVP. In this work, the effects of porosity parameter (, Radiation parameter (α and Temperature-Ratio parameter (µ on non-dimensional temperature distribution for both of the flows are shown. The results show that the effects of (α and (µ on temperature distribution in natural convection are based on porosity and in forced convection are uniform, approximately. Also, it is shown that both VIM and HPM are capable of being used to solve this nonlinear heat transfer equation.doi:10.14456/WJST.2014.64

  11. Numerical Research on High Temperature Stress Characteristic of Internally Finned Bayonet Tube%插管式内翅片管高温应力特性的数值研究

    Institute of Scientific and Technical Information of China (English)

    马挺; 吉彦鹏; 曾敏; 王秋旺

    2011-01-01

    In the present paper, the high temperature stress characteristic of internally finned bayonet tube is numerically studied. The results indicate that high temperature is the main factor to cause large stress and deformation. The large stress happens in the joint of inner fins and inner tubes, so the welding quality of the joint must be ensured. Due to the significant potential of reducing thermal stress, the bayonet structure is superior to the traditional tube for use in the high temperature heat exchanger. Furthermore, it is more suitable for use in the high pressure environment than primary surface recuperator.%本文采用ANSYS软件对插管式内翅片管的高温应力特性进行了数值研究,数值模拟结果表明,高温是产生大应力和大应变的主要原因,在内翅片与内管焊接的部位存在较大的应力区,在焊接过程中要保证此处的焊接质量,插管式内翅片管相对于传统内翅片管具有大幅降低热应力的优点,同时在承受高压方面也比原表面回热器具有更大的优势。

  12. 斜波纹翅片管换热器空气侧特性的数值模拟研究%Numeric Simulation of Heat Transfer Enhancement Characteristics at Air-cooling-side of Declinational Wave Fin-and-tube Heat Exchanger

    Institute of Scientific and Technical Information of China (English)

    2013-01-01

      利用 FLUENT 软件,对平直翅片、均匀斜波纹翅片和倾角渐增斜波纹翅片空气侧的流体流动和换热过程进行了数值模拟.结果表明:在雷诺数为176.5~1777.4的范围内,倾角渐增斜波纹翅片比平直翅片的努赛尔数提高了10.14%~46.57%,阻力系数增加了36.15%~160.67%.三种翅片中,倾角渐增斜波纹翅片的努赛尔数最大,强化传热效果最好.%The fluid flow and heat transfer process of plain fin,declinational-wave fin and increase-angle declinational-wave fin-and-tube are numerically simulated based on the software FLUENT. The simulation results show that the characteristics of the declinational wave fin-and-tube are much better than that of the plain fin-and-tube when the Reynolds number ranger of 176.5~1777.4. Similarly Nusselt number of the increase-angle declinational-wave fin-and-tube has 10.14%~46.57% higher than plain fin. The resistance coefficient is 36.15%~160.67% higher than plain fin. Through comparative analysis,the Nusselt numer of the increase-angle declinational-wave fin-and-tube is the highest and the effect of heat exchange is the best.

  13. Effects of intraspecific variation in reproductive traits, pectoral fin use and burst swimming on metabolic rates and swimming performance in the Trinidadian guppy (Poecilia reticulata).

    Science.gov (United States)

    Svendsen, Jon C; Banet, Amanda I; Christensen, Rune H B; Steffensen, John F; Aarestrup, Kim

    2013-09-15

    There is considerable intraspecific variation in metabolic rates and locomotor performance in aquatic ectothermic vertebrates; however, the mechanistic basis remains poorly understood. Using pregnant Trinidadian guppies (Poecilia reticulata), a live-bearing teleost, we examined the effects of reproductive traits, pectoral fin use and burst-assisted swimming on swimming metabolic rate, standard metabolic rate (O2std) and prolonged swimming performance (Ucrit). Reproductive traits included reproductive allocation and pregnancy stage, the former defined as the mass of the reproductive tissues divided by the total body mass. Results showed that the metabolic rate increased curvilinearly with swimming speed. The slope of the relationship was used as an index of swimming cost. There was no evidence that reproductive traits correlated with swimming cost, O2std or Ucrit. In contrast, data revealed strong effects of pectoral fin use on swimming cost and Ucrit. Poecilia reticulata employed body-caudal fin (BCF) swimming at all tested swimming speeds; however, fish with a high simultaneous use of the pectoral fins exhibited increased swimming cost and decreased Ucrit. These data indicated that combining BCF swimming and pectoral fin movement over a wide speed range, presumably to support swimming stability and control, is an inefficient swimming behaviour. Finally, transition to burst-assisted swimming was associated with an increase in aerobic metabolic rate. Our study highlights factors other than swimming speed that affect swimming cost and suggests that intraspecific diversity in biomechanical performance, such as pectoral fin use, is an important source of variation in both locomotor cost and maximal performance.

  14. Influence of tube's diameter on boiling heat transfer performance in small diameter tubes

    Science.gov (United States)

    Gan, Chengjun; Wang, Weicheng; Zhang, Lining

    1998-03-01

    This paper reports the experiments of evaporation study in 6 mm inner copper diameter tubes using HFC-134a, HCFC-22 and CFC-12 as working fluid. The results show that the evaporation heat transfer coefficient increases with the decreasing of inner diameter of tubes. A new concept of non-dimensional tube diameter U is proposed in this paper for correction of the influence of the tube diameter on the evaporation heat transfer coefficient. And further, a convenient empirical correction method is presented.

  15. Thermal performance of evacuated tube heat pipe solar collector

    Science.gov (United States)

    Putra, Nandy; Kristian, M. R.; David, R.; Haliansyah, K.; Ariantara, Bambang

    2016-06-01

    The high fossil energy consumption not only causes the scarcity of energy but also raises problems of global warming. Increasing needs of fossil fuel could be reduced through the utilization of solar energy by using solar collectors. Indonesia has the abundant potential for solar energy, but non-renewable energy sources still dominate energy consumption. With heat pipe as passive heat transfer device, evacuated tube solar collector is expected to heat up water for industrial and home usage without external power supply needed to circulate water inside the solar collector. This research was conducted to determine the performance of heat pipe-based evacuated tube solar collector as solar water heater experimentally. The experiments were carried out using stainless steel screen mesh as a wick material, and water and Al2O3-water 0.1% nanofluid as working fluid, and applying inclination angles of 0°, 15°, 30°, and 45°. To analyze the heat absorbed and transferred by the prototype, water at 30°C was circulated through the condenser. A 150 Watt halogen lamp was used as sun simulator, and the prototype was covered by an insulation box to obtain a steady state condition with a minimum affection of ambient changes. Experimental results show that the usage of Al2O3-water 0.1% nanofluid at 30° inclination angle provides the highest thermal performance, which gives efficiency as high as 0.196 and thermal resistance as low as 5.32 °C/W. The use of nanofluid as working fluid enhances thermal performance due to high thermal conductivity of the working fluid. The increase of the inclination angle plays a role in the drainage of the condensate to the evaporator that leads to higher thermal performance until the optimal inclination angle is reached.

  16. Effects of intraspecific variation in reproductive traits, pectoral fin use and burst swimming on metabolic rates and swimming performance in the Trinidadian guppy (Poecilia reticulata)

    DEFF Research Database (Denmark)

    Svendsen, Jon Christian; Banet, Amanda I.; Christensen, Rune Haubo Bojesen

    2013-01-01

    of reproductive traits, pectoral fin use and burse-assisted swimming on swimming metabolic rate, standard metabolic rate (MO2std) and prolonged swimming performance (Ucrit). Reproductive traits included reproductive allocation and pregnancy stage, the former defined as the mass of the reproductive tissues divided...... by the total body mass. Results showed that the metabolic rate increased curvilinearly with swimming speed. The slope of the relationship was used as an index of swimming cost. There was no evidence that reproductive traits correlated with swimming cost, MO2std or Ucrit. In contrast, data revealed strong...... effects of pectoral fin use on swimming cost and Ucrit. Poecilia reticulata employed body-caudal fin (BCF) swimming at all tested swimming speeds; however, fish with a high simultaneous use of the pectoral fins exhibited increased swimming cost and decreased Ucrit. These data indicated that combining BCF...

  17. Performance of polypropylene and steel tubes in solar water heaters with natural circulation

    Energy Technology Data Exchange (ETDEWEB)

    Riazi, M.R. [Kuwait Univ., Safat (Kuwait). Chemical Engineering Dept.; Razavi, J. [Sharif Univ. of Technology, Tehran (Iran, Islamic Republic of). Chemical Engineering Dept.

    1997-02-01

    Performance of solar water heaters in thermosyphonic flow with polypropylene and steel tubes was studied experimentally. An experimental apparatus consisting of 36 south-facing parallel tubes was designed and built especially for this study. Experiments were performed at Sharif University of Technology in Tehran during July--August 1994 from 0900 to 1700, when the ambient temperature varied from 29 to 36 C. Overall, 30 experiments were conducted for both types of tubes. At first, it was found that the best collector slope for both types of tubes was 36{degree} and it is independent of tube type. Generally, it was found that polypropylene tubes under similar conditions can increase water temperature by 10 C more than steel tubes. Based on the results shown in this study, use of polypropylene tubes in solar water heating systems is recommended.

  18. Numerical Study of Air Flow and Heat Transfer Characteristics on the Outside of Combined Plane-wavy Fin-and-oval Tube%平直-波纹翅片椭圆管外空气流动与传热特性的数值研究

    Institute of Scientific and Technical Information of China (English)

    2015-01-01

    A 3‐D steady and turbulent numerical simulation was employed to investigate the flow and heat transfer characteristics of air ,having constant properties ,in fin‐and‐oval tube heat exchangers with wavy fin or wavy‐plain combined fin .The investigation reveals the effect of air inlet velocity or Reynolds number (Re) ,wavy fin proportion and location in the combined fin on the average Nusselt number (Nu) of the whole fin surface ,the pressure loss(Δp) and the coeffi‐cient of performance (j/f ) .It is found that ,within the studied Re range ,the wavy location in conbined fin has a significant influence on the Nu ,but has little effect on the Δp ;however ,the wavy fin proportion is a key factor for the Δp .The change of average Nusselt number in the width direction(Nu(x)) along flow direction occurs mainly at the fin leading edge ,and the Nu(x) has a smaller difference at the fin rear section for different fin configurations .So it is more suit‐able to locate plain fin to the rear section rather than wavy fin ,which can further reduce the pres‐sure loss penalty w hile maintains the enhanced heat transfer .For all studied objects ,the optimum j/f can be achieved .The finned oval tube heat exchanger with a combination of 6 wavelength wavy fin and 8 wavelength plain fin arranged along flow direction has maximum j/f value .%利用三维稳态湍流数值模拟方法,研究了物性参数为常数的空气在波纹翅片椭圆管和4种不同结构参数的平直‐波纹复合翅片椭圆管换热器翅片间的换热与流阻特性,揭示了空气进口流速(或雷诺数 R e)、平直‐波纹复合翅片中波纹段占有比例以及所处位置对翅片表面平均努塞尔数 Nu、压差损失Δp和翅片管综合换热性能因子 j/f 影响的规律。结果表明,复合翅片中波纹段所处的位置对换热强度的影响显著,但对流动压降(Δp)的影响甚微;复合翅片中波纹翅片所占比例的多少是影响

  19. Design and Performance Analysis of 1-Bit FinFET Full Adder Cells for Subthreshold Region at 16 nm Process Technology

    Directory of Open Access Journals (Sweden)

    ‘Aqilah binti Abdul Tahrim

    2015-01-01

    Full Text Available The scaling process of the conventional 2D-planar metal-oxide semiconductor field-effect transistor (MOSFET is now approaching its limit as technology has reached below 20 nm process technology. A new nonplanar device architecture called FinFET was invented to overcome the problem by allowing transistors to be scaled down into sub-20 nm region. In this work, the FinFET structure is implemented in 1-bit full adder transistors to investigate its performance and energy efficiency in the subthreshold region for cell designs of Complementary MOS (CMOS, Complementary Pass-Transistor Logic (CPL, Transmission Gate (TG, and Hybrid CMOS (HCMOS. The performance of 1-bit FinFET-based full adder in 16-nm technology is benchmarked against conventional MOSFET-based full adder. The Predictive Technology Model (PTM and Berkeley Shortchannel IGFET Model-Common Multi-Gate (BSIM-CMG 16 nm low power libraries are used. Propagation delay, average power dissipation, power-delay-product (PDP, and energy-delay-product (EDP are analysed based on all four types of full adder cell designs of both FETs. The 1-bit FinFET-based full adder shows a great reduction in all four metric performances. A reduction in propagation delay, PDP, and EDP is evident in the 1-bit FinFET-based full adder of CPL, giving the best overall performance due to its high-speed performance and good current driving capabilities.

  20. Entropy Minimum Generation Analysis Of Circular Fin for Air Cooler%空冷器环肋的熵最小化原理分析

    Institute of Scientific and Technical Information of China (English)

    詹福才; 王立新; 荣丁石; 张志荣

    2011-01-01

    Circular fin parameters for regular triangle arrangement tubes of air cooler are analyzed by EMG (entropy minimum generation) principle. The impact of face velocity,bundle width,tube length, tube rows, fin height, fin thickness, fin density and horizontal tube pitch on heat exchange performance and motor power are studied. The results show that lower face velocity,higher and thinner fin, higher fin density, more tube rows and smaller tube pitch can lead to less irreversible loss. The presentations of this paper is applicable for other type of fins optimization design.%运用熵最小化原理对空冷器正三角形排列换热管的环肋进行了优化,分析了迎面风速、管束宽度、换热管长度、管排数、翅片高度、翅片厚度、翅片密度以及管间距对其换热性能和电机功率消耗的影响.结果表明,低迎面风速、高薄翅片、高翅片密度、多管排数和较小的管间距造成的不可逆损失较小.这一分析结果也适用于其它类型翅片的优化设计.

  1. 全尺寸单排翅管耦合换热的异步CFD模拟%Asynchronous CFD Simulation for Conjugate Heat Exchange of Full-size Single Row Finned Tube

    Institute of Scientific and Technical Information of China (English)

    白焰; 邓慧; 李欣欣; 张东明

    2016-01-01

    The single-row flat wave finned tube is widely applied as the unit tube by the direct air cooled condenser in power plants. Caused by the complicated body geometry in fin side, the vapour condensation involving phase transition, and the heat transfer from vapour zone to air zone conjugating on several interfaces, using computational fluid dynamics (CFD) method to simulate the heat transfer in both the vapour channel and the cooling air channel simultaneously, many challenges are encountered. A mathematical model to simulate the condensation of water vapour was developed counting the interfacial shear stress, the heat balance conditions on the interfacial boundaries of the conjugate heat were presented as well as the method to calculate the conjugate heat. The numerical simulation for the full-size finned tube was carefully separated to 282 CFD modules which share same boundaries each other. Based on the 282 CFD modules, the asynchronous strategy to calculate the conjugate heat of the finned tube in overall scale was successfully carried out. The results from the CFD simulations agree very well with the experimental results, which validates the proposed condensation model, also show the great potential of the asynchronous CFD approach as an effective tool for the full-size finned tube to predict the heat transfer in both sides. Based on the CFD results, the characteristics of flow field was also investigated in terms of both the cooling air and the vapour.%火电厂空冷凝汽器普遍使用单排蛇形翅管作为换热器基管.由于蛇形翅管翅侧几何特征复杂,管内凝结有相变相随,蒸汽到空气的传热经过多个耦合面,用计算流体动力学(computational fluid dynamics,CFD)同步模拟翅管双侧换热,存在很多困难.提出液膜表面剪切力条件下的管内冷凝模型,分析蒸汽至空气的耦合换热过程和换热面平衡条件,给出耦合换热量的计算方法.将全尺寸翅管换热的数值模拟分解成282个

  2. DKV joint project: reduction of CFC-emissions in air conditioning and refrigeration. Subproject 6. Pool boiling of new refrigerants and their mixtures at single plain and finned tubes. Final report; DKV-Verbundvorhaben: Minderung von FCKW-Emissionen in der Klima- und Kaeltetechnik. Teilvorhaben 6; Waermeuebergang bei der Verdampfung neuer Kaeltemittel an einzelnen Glatt- und Rippenrohren. Abschlussbericht

    Energy Technology Data Exchange (ETDEWEB)

    Gorenflo, D.; Rott, W.; Sokol, P.; Caplanis, S; Kuenstler, W.

    1993-03-01

    Heat transfer at pool boiling from three novel finned tubes with different fin geometry to the new refrigerants R134a (CH{sub 2}F.CF{sub 3}), R152a (CH{sub 3}.CHF{sub 2}), R227 (CF{sub 3}.CHF.CF{sub 3}) and to a nearly equimolar mixture of R134a and R152a has been investigated within extended ranges of heat flux and saturation pressure. The main new features of the tubes are: K-shaped fins with very narrow fin distances/T-shaped fins with additional grooves between the fins/Y-shaped fins with additional grooves between the fins. The results show that especially the tubes with T-shaped and Y-shaped fins are significantly superior to plain tubes at pool boiling of the new refrigerants at saturation pressures up to approximately 10 bar. The biggest enhancement has been achieved using the tube with Y-shaped fins, thus energy consumption can be reduced by smaller temperature differences on the pool side, if these tubes will be applied, and the amount of refrigerants as well as construction material for the evaporators can be reduced by more compact design, being possible, because the heat flow rate transferred per unit of tube length may be chosen higher. (orig.). 11 refs., 1 tab., 12 figs. [Deutsch] Durch Waermeuebergangsmessungen bei der Verdampfung von neuen, teilfluorierten Kaeltemitteln an neuentwickelten Hochleistungs-Verdampferrohren sollten verlaessliche Auslegungsgrundlagen fuer optimierte Rohrbuendelverdampfer bereitgestellt werden, die mit geringerem Energiebedarf und durch kompakte Bauweise mit reduziertem Material- und Kaeltemittelaufwand auskommen und dadurch einerseits kein Ozongefaehrdungspotential und andererseits einen geringeren Beitrag zum Treibhauseffket liefern als die z.Zt. noch verwendete Technik. Zu Beginn des Vorhabens existierten entsprechende Unterlagen in der Literatur nicht. Als Versuchsstoffe dienten die neuen Kaeltemittel R134a(CH{sub 2}F.CF{sub 3}), R152a(CH{sub 3}.CHF{sub 2}), R227(CF{sub 3}.CHF.CF{sub 3}) sowie ein etwa aequimolares

  3. Real gas features on the performance of pulse tube cryocoolers

    Science.gov (United States)

    Ju, Y. L.

    2002-05-01

    The working helium gas in a pulse tube cryocooler operating at temperatures down to 80 K is mainly assumed to be an ideal gas. Therefore, the time-variations of the temperature profiles and the position of the gas element traveling with pressure oscillations inside the pulse tube can be readily determined by the law of Poisson function. However, this is certainly invalid for the pulse tube cryocooler operating at temperature range of liquid helium, in which the thermal properties of the helium gas change drastically. The temperature profiles in the regenerator and the pulse tube are strongly affected by the real thermal properties of the helium gas. We derive in this paper, the respective expressions to follow the tracks of the gas elements as they move in the pulse tube, and to reveal the time dependence of the temperature profiles and the position of gas elements traveling with the pressure oscillations inside the pulse tube. The approach is based on the thermodynamic equations for the real gas. We will show that contrary to the ideal gas case there is another term which determines the dynamic behaviors of the temperature distributions and the position of the gas elements. A typical calculation is presented for visualizing the time dependence of the cooling-down processes of the temperature profiles in the pulse tube of a 4K two-stage pulse tube cryocooler from room temperature down to low temperature.

  4. Condensation of Refrigerant-11 on the outside of horizontal and inclined enhanced tubes

    Energy Technology Data Exchange (ETDEWEB)

    Domingo, N.

    1982-12-01

    Heat transfer condensation tests with Refrigerant-11 were performed on the outside of a smooth tube and a variety of enhanced tubes oriented horizontally and at various tube inclinations. One smooth tube and seven enhanced (externally fluted, roped, spiraled, and externally finned) tubes of 2.54-cm (1-in.) nominal outside diameter and 1.17-m (4-ft) length were tested. Several of the tested tubes featured internal enhanced geometries, which were caused by the heat transfer enhancing geometry on the tube's external surface. Condensing heat transfer coefficients are reported as composite coefficients, which combine the resistance of the condensing film and the tube wall, and are based on total tube outside surface area. Results show that in the horizontal condensing mode, the rank order (best to worst) of the tube geometries tested was spiral-shaped tubes, rope-shaped tubes, smooth tube, externally finned tube, and externally fluted tube. For a spiral-shaped tube, horizontal composite coefficients were up to 2.0 times the corresponding horizontal smooth tube values. For tilt angles greater than or equal to 60/sup 0/ from the horizontal, the condensing performance of the externally fluted tube was best of all the tubes tested.

  5. 扁管翅片换热器肋侧换热系数定义用特征温度%The Characteristic Temperature in the Definition of the Heat Transfer Coefficient on the Fin Side Surface of a Flat Tube Bank Fin Heat Exchanger

    Institute of Scientific and Technical Information of China (English)

    姚玉换; 王良璧

    2012-01-01

    为了获得换热器肋侧换热系数定义用比较普适的特征温度,采用分区求解、边界耦合方法与非耦合方法对扁管翅片式换热器三雏模型的流动与传热性能进行了数值模拟,得到了换热器在不同肋片材料和不同雷诺数下用不同特征温度定义肋侧换热系数的区别,并将数值结果与实验结果进行比较.结果表明:当特征温度不同时,肋侧换热系数数值结果不同;当Re小于1000和用非耦合计算时,与实验值吻合最好的是以流动进出口平均温度为特征温度的数值结果;而Re大于1000后,耦合计算时以流动进出口平均温度为特征温度数值结果与实验值更靠近.%To obtain an appropriate characteristic temperature in the definition of the fin side surface heat transfer coefficient, flow and heat transfer characteristics of a flat tube bank fin heat exchanger are simulated by coupled and non-coupled numerical methods. Heat transfer coefficient of the fin side surface under different materials and Reynolds numbers is obtained. The numerical results obtained by two algorithms are compared with experimental data. It shows that the fin side surface heat transfer coefficient is different if the characteristic temperature is selected differently. The numerical result using the average temperature of the fin side fluid as the characteristic temperature agrees well with the experimental results when Re is less than 1 000 and the non-coupled method is adopted. The results are the same when Re is larger than 1 000 and the coupled method is used.

  6. A comprehensive study of modified Wilson plot technique to determine the heat transfer coefficient during condensation of steam and R-134a over single horizontal plain and finned tubes

    Energy Technology Data Exchange (ETDEWEB)

    Kumar, Ravi; Varma, H.K.; Agrawal, K.N.; Mohanty, Bikash

    2001-03-01

    In the present investigation a comprehensive study of the modified Wilson plot technique has been made and a stepwise methodology has been evolved. This technique can be used to determine the condensing-side heat transfer coefficient during condensation of vapor over a horizontal tube. The necessary experimental data have been acquired by conducting experiments for the condensation of steam and R-134a over a plain tube and different finned tubes (CIFTs and SIFTs). The experimental heat transfer coefficient, based on the test-section wall temperature measurement (wall temperature was measured with thermocouples), h{sub o}, has been compared with that predicted by the modified Wilson plot technique, h{sub mw}. The modified Wilson plot technique underpredicted the condensing-side heat transfer coefficient for the condensation of steam in a range of 7.5-15%. The heat transfer coefficient for the condensation of R-134a is also underpredicted in a range of 13-25% by this technique. (Author)

  7. Heat Transfer and Friction Characteristics of Wavy Fin with Hydrophilic Coating under Dehumidifying Conditions

    Institute of Scientific and Technical Information of China (English)

    ZHANG Yuan-ming; DING Guo-liang; MA Xiao-kui

    2007-01-01

    An experimental study on the airside heat transfer and friction characteristics of seven hydrophilic-coated wavy finned tube heat exchangers is performed under dehumidifying conditions. The effects of fin pitch, number of tube rows and inlet air relative humidity on the airside characteristics are investigated. The airside heat transfer and friction characteristics are presented in the form of Colburn factor and friction factor, respectively. The test results indicate that the Colburn factor and friction factor increase with decreasing fin pitch. The Colburn factor of 2tube row heat exchanger is higher than that of 3 row heat exchanger, while their friction factors are nearly equal. As the inlet relative humidity increases, the Colburn factor increases and the friction factor is almost unchanged. The airside heat transfer and friction correlations are proposed for the hydrophilic-coated wavy fin with mean deviations of 6.5% and 9.1%, respectively. They can be used to design or evaluate hydrophilic-coated wavy fin-and-tube heat exchangers.

  8. Effect of the conical-shape on the performance of vortex tube

    Science.gov (United States)

    Guen, M.; Natkaniec, C.; Kammeyer, J.; Seume, J. R.; Adjlout, L.; Imine, O.

    2013-04-01

    The present study focuses on the effect of conical shape in the cold side of the Ranque-Hilsch vortex tube which is shown to have a considerable influence on the system performance. A vortex tube is a simple circular tube with no moving parts which is capable to divide a high pressure flow into two relatively lower pressure flows with temperatures higher and lower than the incoming flow. A three-dimensional computational fluid dynamic model is used to analyse the mechanisms of flow inside a vortex tube. The SST turbulence model is used to predict the turbulent flow behaviour inside the vortex tube. The geometry of a vortex tube with circumferential inlet slots as well as axial cold and hot outlet is considered. Performance curves temperature separation versus cold outlet mass fraction are calculated for a given inlet mass flow rate and varying outlet mass flow rates.

  9. 直通式太阳能真空管集热器热性能分析%Thermal Performance Analyses of the Direct Pass Vacuum Tube Solar Collector

    Institute of Scientific and Technical Information of China (English)

    葛众; 王辉涛; 王华

    2012-01-01

    通过对直通式太阳能真空管传热模型的分析,在导出单根带翅片与不带翅片的直通式太阳能真空管的总热损失系数、效率因子、热迁移因子和瞬时效率的基础上,建立了直通式太阳能真空管的性能预测模型;针对由多根并联、顺流布置的直通式太阳能真空管组成的平行流集热器,对比计算了带翅片与不带翅片两种真空管及由其组成的集热器的瞬时效率.结果表明,在工质流量,进口温度,环境温度等条件相同的情况下带翅片的直通式太阳能真空管以及由其构成的集热器的瞬时效率分别比不带翅片的太阳能真空管及集热器提高很多;并联直通式太阳能真空管间的流量分配不均匀性致使集热器的整体效率低于单根真空管的瞬时效率.%The heat transfer model of direct pass solar vacuum tube is analyzed. Based on the overall heat loss coefficient, the prediction models to calculate the performances such as thermal efficiency factor, the heat removal factor and the instantaneous efficiency of tubes with fins and without fins, are developed. As for the solar collector composed of multiple parallel downstream arrangement of direct pass vacuum tube, the instantaneous efficiency of tubes with fins and without fins are compared with each Pfher. The results show that the instantaneous efficiency of direct pass vacuum tube solar collector with fins is much higher than that without fins on condition that the refrigerant flow rate, inlet temperature, ambient temperature are kept the same. The uneven distribution of flow rate between rows of collector results in a decline in the overall efficiency compared with the single vacuum tube.

  10. Numerical optimization of louvered fin heat exchanger with variable louver angles

    Science.gov (United States)

    Ameel, B.; Degroote, J.; Huisseune, H.; De Jaeger, P.; Vierendeels, J.; De Paepe, M.

    2012-11-01

    Several studies of the louvered fin heat exchanger have already been done. Both experimental and numerical studies are available. Investigations to the optimal louver angle have been performed, many times in combination with other fin parameters such as louver pitch and fin thickness. Most studies assume a single louver angle for all the louvers in the heat exchanger. Hsieh and Jang [1] on the other hand studied the effect of a variable louver angle for 5 different cases with successively increasing or decreasing louver angles. Tube-fin interactions were not taken into account. In this study, a round tube and fin geometry with individually varying louver angles is analyzed. The thickness of the fin was neglected. Any interactions between the optimal louver angles and the fin thickness are hence not captured. A laminar and steady calculation was performed, with symmetric boundary conditions. For the Reynolds number on the hydraulic diameter (ReDh) of 535 that was studied, a Von Karman vortex street is present behind the last tube row of heat exchanger. The steady calculation is hence only an approximation of the reality, but is shown to give reasonable results. An ordinary kriging response surface model was used to explore the entire parameter space. Updates to the model were made on the basis of improving the Pareto front, visualizing the tradeoff between heat transfer and pressure drop. It is shown that the use of individually varying louver angles allows increasing the Colburn j factor by 1.3% for the same friction factor, with respect to the optimal uniform louvered fin configuration.

  11. Ultrahigh performance of Ti-based glassy alloy tube sensor for Coriolis mass flowmeter

    Institute of Scientific and Technical Information of China (English)

    MA Chao-li; A. INOUE; ZHANG Tao

    2006-01-01

    Bulk metallic glasses (BMGs) have potential applications for both structural and functional components owing to their good mechanical properties. With the aim of demonstrating great engineering value of BMGs, a direct melt-forming technique based on suction casting for the production of glassy alloy tubes was developed. The fabrication, structure, geometry, properties and sensor performance of the tubes were examined. The results show that the Coriolis mass flowmeters using the Ti-based glassy alloy sensor tube exhibit excellent measurement sensitivity, viz. 28.5 times higher than that of the conventional flowmeter manufactured using stainless steel (SUS316) tube.

  12. Thermal and friction drop characteristic of heat exchangers with elliptical tubes and smooth fins//Caracterización térmica e hidráulica de intercambiadores de calor con tubos elípticos y aletas lisas

    Directory of Open Access Journals (Sweden)

    Rubén Borrajo-Pérez

    2012-09-01

    Full Text Available Pressure drop and heat transfer are the most important parameters in compact heat exchanger. There is a lack of information in the literature about heat exchanger with elliptical tube. The objective of this work was the experimental characterization of compact heat exchangers models using elliptical tube with eccentricity of 0,5 and smooth fins. The Reynolds numbers and the spacing were varied and always inside laminar regime. The experiments were conducted in an open wind tunnel using sublimation of naphthalene and the heat and mass transfer analogy. As results, the average and local Nusselt number and friction factor for 36 models were obtained. Correlations for Colburn and friction factors were presented. This correlations were obtained for 200fins. These are the first correlations presented in the open literature covering a wider range of pitches. A baseline for future implementations of enhancement heattransfer techniques is presented.Key words: friction factor, heat transfer coefficient, elliptical tube, compact heat exchanger._______________________________________________________________________________Resumen:Caída de presión y transferencia de calor son importantes parámetros en intercambiadores de calor. Existe falta de información cuando de intercambiadores de calor y tubos elípticos se trata. El objetivo del trabajo fue caracterizar experimentalmente modelos de intercambiadores de calor con tubos elípticos yaletas lisas. El numero de Reynolds y los espaciamientos fueron variados, dentro del régimen laminar. Los experimentos fueron desarrollados en un túnel de viento de circuito abierto usando la sublimación de naftaleno y la analogía calor y masa. Los números de Nusselt medio, locales y el factor de fricción fueronobtenidos en forma de correlaciones de Factores de Fricción y Colburn. Las correlaciones, validas para 200

  13. Performance Limits of Pulse Tube Cryocoolers Using 3HE

    Science.gov (United States)

    Kittel, P.

    2008-03-01

    The enthalpy, entropy, and exergy flows resulting from the real gas effects of 3He in ideal pulse tube cryocoolers are described. The discussion follows a previous description of the real gas effects of 4He in ideal pulse tube cryocoolers and makes use of a recently developed model of the thermophysical properties of 3He. This model is used to describe how the thermodynamic flows are affected by real gas phenomena of 3He and compares these effects to similar effects for 4He. The analysis was done over the pressure range 0.3-2 MPa and temperatures down to 1 K. At 2 MPa there is almost no difference in the cooling power between 3He and 4He. At lower pressures, using 3He is advantageous. There is a 1-2 K reduction in the 3He cooling power vs. temperature curves compared to those for 4He in the 0.3-1 MPa range.

  14. Effect of YouTube Videos and Pictures on EFL Students’ Writing Performance

    Directory of Open Access Journals (Sweden)

    Erlik Widiyani Styati

    2017-01-01

    Full Text Available This research aims at investigating the effect of YouTube videos and pictures as the authentic materials on Indonesian EFL students’ writing performance. The experimental research is conducted by using quasi-experimental design. This research employed two groups; an experimental and control group. This is to see which group is effective to be used in helping the students’ writing ability. The first group was taught by using YouTube videos and the second group was given treatment by using pictures. Both YouTube and pictures are the authentic materials which help the students to have better writing performance. The subjects of this study were the second semester students of English Department, IKIP PGRI Madiun. Both of the groups were instructed to write paragraph by using YouTube videos and pictures as the authentic materials. The data were analyzed by using Independent t-test. The result of the study shows that there is significantly different between the students who write paragraph after being taught by using YouTube videos and by using pictures. The students who were taught by using YouTube videos had lower writing performance than the students who were taught by using pictures. It means that using pictures in teaching writing is better than using YouTube videos to help the students in writing performance.

  15. Evaluation of the heat transfer performance of helical coils of non-circular tubes

    Institute of Scientific and Technical Information of China (English)

    Jundika C.KURNIA; Agus P.SASMITO; Arun S.MUJUMDAR

    2011-01-01

    This study addresses heat transfer performance of various configurations of coiled non-circular tubes, e. g. , in-plane spiral ducts, helical spiral ducts, and conical spiral ducts. The laminar flow of a Newtonian fluid in helical coils made of square cross section tubes is simulated using the computational fluid dynamic approach. The effects of tube Reynolds number, fluid Prandtl number, coil diameter, etc. , are quantified and discussed. Both constant wall temperature and constant heat flux conditions are simulated. The effect of in-plane coil versus a cylindrical design of constant coil, as well as a conical coil design is discussed. Results are compared with those for a straight square tube of the same length as that used to form the coils. Advantages and limitations of using coiled tubes are discussed in light of the numerical results.

  16. Steady-state and transient heat transfer through fins of complex geometry

    Directory of Open Access Journals (Sweden)

    Taler Dawid

    2014-06-01

    Full Text Available Various methods for steady-state and transient analysis of temperature distribution and efficiency of continuous-plate fins are presented. For a constant heat transfer coefficient over the fin surface, the plate fin can be divided into imaginary rectangular or hexangular fins. At first approximate methods for determining the steady-state fin efficiency like the method of equivalent circular fin and the sector method are discussed. When the fin geometry is complex, thus transient temperature distribution and fin efficiency can be determined using numerical methods. A numerical method for transient analysis of fins with complex geometry is developed. Transient temperature distributions in continuous fins attached to oval tubes is computed using the finite volume - finite element methods. The developed method can be used in the transient analysis of compact heat exchangers to calculate correctly the heat flow rate transferred from the finned tubes to the fluid.

  17. A biorobotic model of the sunfish pectoral fin for investigations of fin sensorimotor control

    Energy Technology Data Exchange (ETDEWEB)

    Phelan, Chris; Tangorra, James [Department of Mechanical Engineering, Drexel University, Philadelphia, PA 19104 (United States); Lauder, George [Museum of Comparative Zoology, Harvard University, Cambridge, MA 02138 (United States); Hale, Melina, E-mail: tangorra@coe.drexel.ed [Department of Organismal Biology and Anatomy, University of Chicago, Chicago, IL 60637 (United States)

    2010-09-15

    A comprehensive understanding of the control of flexible fins is fundamental to engineering underwater vehicles that perform like fish, since it is the fins that produce forces which control the fish's motion. However, little is known about the fin's sensory system or about how fish use sensory information to modulate the fin and to control propulsive forces. As part of a research program that involves neuromechanical and behavioral studies of the sunfish pectoral fin, a biorobotic model of the pectoral fin and of the fin's sensorimotor system was developed and used to investigate relationships between sensory information, fin ray motions and propulsive forces. This robotic fin is able to generate the motions and forces of the biological fin during steady swimming and turn maneuvers, and is instrumented with a relatively small set of sensors that represent the biological lateral line and receptors hypothesized to exist intrinsic to the pectoral fin. Results support the idea that fin ray curvature, and the pressure in the flow along the wall that represents the fish body, capture time-varying characteristics of the magnitude and direction of the force created throughout a fin beat. However, none of the sensor modalities alone are sufficient to predict the propulsive force. Knowledge of the time-varying force vector with sufficient detail for the closed-loop control of fin ray motion will result from the integration of characteristics of many sensor modalities.

  18. Impact of pattern dependency of SiGe layers grown selectively in source/drain on the performance of 14 nm node FinFETs

    Science.gov (United States)

    Qin, Changliang; Wang, Guilei; Kolahdouz, M.; Luo, Jun; Yin, Huaxing; Yang, Ping; Li, Junfeng; Zhu, Huilong; Chao, Zhao; Ye, Tianchun; Radamson, Henry H.

    2016-10-01

    A complete mapping of 14 nm FinFETs performance over 200 mm wafers was performed and the pattern dependency of SiGe selective growth was calculated using an empirical kinetic molecule model for the reactant precursors. The transistor structures were analyzed by conventional characterization tools and their performance was simulated by considering the process related variations. The applied model presents for the first time a powerful tool for transistor community to predict the SiGe profile and strain modulating over a processed wafer, independent of wafer size.

  19. Effect of Geometric Modifications on the Performance of Vortex Tube - A Review

    Directory of Open Access Journals (Sweden)

    O. M. Kshirsagar

    2014-11-01

    Full Text Available The vortex tube is device, which produces hot and cold air streams simultaneously at its two ends from a source of compressed air without any moving part. Literature review of this paper is to understand the effect of various parameters like inlet pressure of air, number of nozzles, cold orifice diameter and hot end valve angle on the performance of vortex tube. Also by the literature review it is clear that there is no theory so perfect, which gives the satisfactory explanation of the vortex tube phenomenon. Due to this reason researcher conduct the series of experimentation to understand the effect of various parameters mentioned above on the performance of vortex tube.

  20. Numerical study on natural convection heat transfer of fin - tube air - heating vaporizer%空温式翅片管气化器自然对流换热的数值模拟

    Institute of Scientific and Technical Information of China (English)

    陈叔平; 常智新; 韩宏茵; 谢福寿; 姚淑婷

    2011-01-01

    The natural convective heat transfer model on the air side of air - heating cryogenic finned - tube vaporizer was established. The natural convection heat transfer of vaporizer side air was simulated 3D - numerically used by fluent software,SST model and SIMPLEC algorithm for differentstructure parameters and inside wall temperature of the vaporizer. Based on the result of numerical simulation, the influence of different structure sizes and wall temperatures on natural convection heat transfer was analysed, and a calculation correlation of Nusselt number for the air side natural convection heat transfer of vaporizer was fitted, providing a reference for engineering practice.%建立了深冷空温式星形翅片管气化器的空气侧自然对流换热模型.利用fluent软件,采用SST k-ω湍流模型和SIMPLEC算法,对多组不同结构参数、不同内壁面温度的气化器空气侧自然对流换热进行了三维数值模拟.由数值模拟结果分析了气化器各结构尺寸大小与壁温对翅片管自然对流换热的影响,并拟合了气化器空气侧自然对流换热的Nu数的计算关联式,为工程实际供参考.

  1. 风速对空气源热泵翅片管换热器结霜特性影响%The effects of wind speed on frosting characteristics of fin - tube heat exchanger for air source heat pump

    Institute of Scientific and Technical Information of China (English)

    尹从绪; 陈轶光

    2011-01-01

    The effect of the wind velocity on the frosting characteristics of the fin - and - tube heat exchanger was investigated experimentally. The experimental results indicated that the frost mass accumulation doesn't increase linearly with the wind velocity, the minimum frost mass accumulation are formed at the air velocity of 1. 3m/s. The frost thickness decreased as the wind velocity increase, but the maximum heating capacity increased as the face velocity increase.%针对风速对空气源热泵翅片管室外换热器结霜特性的影响进行了实验研究.实验结果表明,结霜量随风速的增加不是成线形增长,在风速为1.3m/s时结霜量最小.霜层厚度随着风速的增加反而减小,而翅片管换热器的最大换热量随着风速的增加而增加.

  2. Performance investigation of capillary tubes for machine tool coolers retrofitted with HFC-407C refrigerant

    Science.gov (United States)

    Wang, Fujen; Chang, Tongbou; Chiang, Weiming; Lee, Haochung

    2012-09-01

    The machine tool coolers are the best managers of coolant temperature in avoiding the deviation of spindle centerline for machine tools. However, the machine coolers are facing the compressed schedule to phase out the HCFC (hydro-chloro-floro-carbon) refrigerant and little attention has been paid to comparative study on sizing capillary tube for retrofitted HFC (hydro-floro-carbon) refrigerant. In this paper, the adiabatic flow in capillary tube is analyzed and modeled for retrofitting of HFC-407C refrigerant in a machine tool cooler system. A computer code including determining the length of sub-cooled flow region and the two phase region of capillary tube is developed. Comparative study of HCFC-22 and HFC-407C in a capillary tube is derived and conducted to simplify the traditional trial-and-error method of predicting the length of capillary tubes. Besides, experimental investigation is carried out by field tests to verify the simulation model and cooling performance of the machine tool cooler system. The results from the experiments reveal that the numerical model provides an effective approach to determine the performance data of capillary tube specific for retrofitting a HFC-407C machine tool cooler. The developed machine tool cooler system is not only directly compatible with new HFC-407C refrigerant, but can also perform a cost-effective temperature control specific for industrial machines.

  3. Parametric experiments and CFD analysis on condensation heat transfer performance of externally condensing tubes

    Energy Technology Data Exchange (ETDEWEB)

    Jeon, Byong Guk; Kim, Do Yun; Shin, Chang Wook; NO, Hee Cheon, E-mail: hcno@kaist.ac.kr

    2015-11-15

    Highlights: • Geometric effects of HXs on external condensation are experimentally observed. • Lower tube angle has higher heat transfer coefficients over vertical tubes by 15–30%. • 2.68 cmD tube has higher heat transfer coefficients over 4.91 cmD tube roughly by 10–20%. • CFD approach is validated against our experiments with good accuracy (error ∼7%). - Abstract: To ensure safe operation of nuclear power plants even in the case of a prolonged station blackout, advanced reactors adopt passive systems that can operate without electricity supply. In Korea, a passive auxiliary feedwater system was successfully validated, and a passive containment cooling system (PCCS) has recently attracted attention. To investigate the thermal performance of PCCSs, we perform various experiments with external heat exchangers, which condense steam externally, for PCCSs. Through experiments, we construct a database for the lower air mass fraction and perform a parametric study on the tube inclination and diameter. The operating ranges for the experiments are 0.24–0.38 MPa (pressure), 0.06–0.4 (air mass fraction), and 0–90° (tube inclination). A lower tube inclination and smaller tube diameter are found to yield higher heat-transfer coefficients, by approximately 20%. In the prediction of condensation heat-transfer coefficients, experimental correlations and the heat–mass transfer analogy have limitations in both accuracy and applicability. A computational-fluid-dynamics approach is used with the aid of user-defined functions to calculate the heat-transfer coefficients. The resulting predictions exhibit an average error of 7% when the air mass fraction is higher than 0.2.

  4. Small-bore chest tubes seem to perform better than larger tubes in treatment of spontaneous pneumothorax

    DEFF Research Database (Denmark)

    Iepsen, Ulrik Winning; Ringbæk, Thomas

    2013-01-01

    The aim of this study was to compare the efficacy and complications of surgical (large-bore) chest tube drainage with smaller and less invasive chest tubes in the treatment of non-traumatic pneumothorax (PT). ......The aim of this study was to compare the efficacy and complications of surgical (large-bore) chest tube drainage with smaller and less invasive chest tubes in the treatment of non-traumatic pneumothorax (PT). ...

  5. Performance tests of the 1MWt shell-and-tube heat exchangers for OTEC

    Energy Technology Data Exchange (ETDEWEB)

    Thomas, A.; Lorenz, J. J.; Hillis, D. L.; Yung, D. T.; Sather, N. P.

    1979-01-01

    Final test results are reported for the five 1 MWt shell-and-tube heat exchangers tested at Argonne National Laboratory. These five heat exchangers are the Union Carbide flooded-bundle evaporator, the Union Carbide sprayed-bundle evaporator, the Union Carbide enhanced-tube condenser, the Carnegie-Mellon vertical fluted-tube evaporator, and the Carnegie-Mellon vertical fluted-tube condenser. Performance parameters measured include the overall heat transfer coefficient (U/sub 0/), the water-side pressure drop, and the vapor quality. Also measured were operational characteristics of the heat exchangers such as repeatability of results and the dependence of U/sub 0/ on heat duty, ammonia flow rate, and subcooling. Individual water-side and ammonia-side coefficients were deduced using the Wilson Plot method.

  6. Optimization of counter flow Ranque-Hilsch vortex tube performance using Taguchi method

    Energy Technology Data Exchange (ETDEWEB)

    Pinar, Ahmet Murat [Celal Bayar University, Vocational High School, Department of Machinery, 45400-Turgutlu-Manisa (Turkey); Uluer, Onuralp [Gazi University, Faculty of Technical Education, Mechanical Education Department, Teknikokullar, 06503 Ankara (Turkey); Kirmaci, Volkan [Bartin University, Faculty of Engineering, Mechanical Engineering Department, 74100 Bartin (Turkey)

    2009-09-15

    This study discusses the application of Taguchi method in assessing maximum temperature gradient for the Ranque-Hilsch counter flow vortex tube performance. The experiments were planned based on Taguchi's L27 orthogonal array with each trial performed under different conditions of inlet pressure, nozzle number and fluid type. Signal-to-noise ratio (S/N) analysis, analysis of variance (ANOVA) and regression analysis were carried out in order to determine the effects of process parameters and optimal factor settings. Finally, confirmation tests verified that Taguchi method achieved optimization of counter flow Ranque-Hilsch vortex tube performance with sufficient accuracy. (author)

  7. Thermal performance enhancement in tubes using helically twisted tape with alternate axis inserts

    Science.gov (United States)

    Yongsiri, K.; Thianpong, C.; Nanan, K.; Eiamsa-ard, S.

    2016-01-01

    This article presents an investigation on heat transfer enhancement in a round tube inserted with a helically twisted tape. The effects of a helically twisted tape with alternate axis (HTT-A) on heat transfer, friction factor, and thermal performance factor behaviours are reported for the turbulent regime. HTT-A geometries are tape pitch to tube diameter, P/D = 1.0, 1.5, and 2.0; alternate length to pitch length, l/P = 1.0, 1.5, and 2.0; twisted length to tape width, y/W = 3.0; and tape width to tube diameter, w/D = 0.2. The experiment has been performed by varying the volumetric air flow rate in order to adjust Reynolds number ranging from 6 000 to 20 000. The wall of the testing tube is uniformly heated as a constant heat flux while the tests are covered with thermal insulations to reduce heat loss to surroundings. Thermal performance is evaluated by comparing the present experimental results with the results of the modified HTT-A and also those obtained from previous study (conventional helically twisted tape, HTT). The thermal performance of tested tube with HTT-A is evaluated to obtain the degree of heat transfer enhancement and friction factor induced by HTT-A with respect to the plain tube under the same test conditions. Evenly, it is interesting to observe that the tube with HTT-A consistently possesses higher heat transfer and thermal performance factor than those with the HTT around 14.1% and 1.9%, respectively. The HTT-A with the smaller pitch ratio and adjacent twist length provides higher heat transfer rate and friction factor than the one with larger pitch ratio and alternate length as a result of a larger contact surface area, stronger swirl intensity and, thus, better fluid mixing near the tube wall. In the range determined, the tubes with the largest pitch ratio ( P/D = 2.0) and smallest alternate length ( l/P = 1.0) give the highest thermal performance factor at around 1.35. In addition, the empirical correlations of the Nusselt number, friction

  8. Modeling the cooling performance of vortex tube using a genetic algorithm-based artificial neural network

    Directory of Open Access Journals (Sweden)

    Pouraria Hassan

    2016-01-01

    Full Text Available In this study, artificial neural networks (ANNs have been used to model the effects of four important parameters consist of the ratio of the length to diameter(L/D, the ratio of the cold outlet diameter to the tube diameter(d/D, inlet pressure(P, and cold mass fraction (Y on the cooling performance of counter flow vortex tube. In this approach, experimental data have been used to train and validate the neural network model with MATLAB software. Also, genetic algorithm (GA has been used to find the optimal network architecture. In this model, temperature drop at the cold outlet has been considered as the cooling performance of the vortex tube. Based on experimental data, cooling performance of the vortex tube has been predicted by four inlet parameters (L/D, d/D, P, Y. The results of this study indicate that the genetic algorithm-based artificial neural network model is capable of predicting the cooling performance of vortex tube in a wide operating range and with satisfactory precision.

  9. Optimization of thermal performance of Ranque Hilsch Vortex Tube: MADM techniques

    Science.gov (United States)

    Devade, K. D.; Pise, A. T.

    2016-08-01

    Thermal performance of vortex tube is noticeably influenced by its geometrical and operational parameters. In this study effect of various geometrical (L/D ratio: 15, 16, 17, 18; exit valve angle; 300, 450, 600, 750, 900; cold end orifice diameter: 5, 6 and 7mm, tube divergence angle: 00, 20, 30, 40) and operational parameters (inlet pressure: 2 to 6 bars) on the performance of vortex tube have been investigated experimentally. Multiple Attribute Decision Making (MADM) techniques are applied to determine the optimum combination of the vortex tube. Performance of vortex tube was analysed with optimum temperature difference on cold end, COP for cooling. The MADM (Multiple Attribute Decision Making) methods, namely WSM (Weighted Sum Method), WPM (Weighted Power Method), TOPSIS (Technique for Order Preference by Similarity to Ideal Solution) and AHP (Analytical Hierarchy Process) are applied. Experimental best performing combinations are obtained for Length to Diameter ratios 15, 16, 17 with exit valve angle as 450,750 and 900 at orifice diameter 5mm for inlet pressure of 5 and 6 bar pressure. Best COP, efficiency and cold end temperature difference are 0.245, 40.6% and 38.3K respectively for the combination of 15 L/D, 450 valve angle, 5mm orifice diameter and 2 bar pressure by MADM techniques.

  10. The Effect of the Capillary Tube Coil Number on the Refrigeration System Performance

    Directory of Open Access Journals (Sweden)

    Thamir K. Salim

    2012-06-01

    Full Text Available The capillary tube performance for (R134a is experimentally investigated. The experimental setup is a real vapor compression refrigeration system. All properties of the refrigeration system are measured for various mass flow rate from (13 – 23 kg/hr and capillary tube coil number (0-4 with fixed length (150 cm and capillary diameter(2.5mm.The results showed that the theoretical compression power increases by (65.8 % as the condenser temperature increases by (2.71%, also the theoretical compression power decreases by (10.3 % as the capillary tube coil number increases.The study shows also that the cooling capacity increases by (65.3% as the evaporator temperature increases by (8.4 %, and the cooling capacity increases by (1.6%as the capillary tube coil number increases in the range (0-4.The coefficient of performance decreases by (43.4 %, as the mass flow rateincreases by (76.9%, also the coefficient of performance increases by (13.51 % as thecapillary tube coil number increases in the range (0-4.Through this study, it was found that the best coil number in refrigeration cycle at the lowest mass flow rate (31 Kg/hr and at high mass flow rate (23 Kg/hr is (coil number = 4, this will give the highest performance, cooling capacity and lowest theoretical compression power.

  11. HEAT TRANSFER EVALUATION OF HFC-236EA WITH HIGH PERFORMANCE ENHANCED TUBES IN CONDENSATION AND EVAPORATION

    Science.gov (United States)

    The report gives results of an evaluation of the heat transfer performance of pure hydrofluorocarbon (HFC)-236ea for high performance enhanced tubes which had not been previously used in Navy shipboard chillers. Shell-side heat transfer coefficient data are presented for condensa...

  12. Performance Study of Concrete-Filled Steel Tubes

    Directory of Open Access Journals (Sweden)

    Chair A.

    2014-04-01

    This type of structure can be used in Algeria for rehabilitating old buildings, or strengthening reinforced concretecolumns to improve their structural performance. However, new regulatory measures should be considered in order tointroduce this compound element in the construction.

  13. Evaluation of a Fin and Tube Type Adsorber/Desorber Heat Exchanger using =ACF/C2H5OH Pair

    Science.gov (United States)

    Kariya, Keishi; Makimoto, Naoya; Kuwahara, Ken; Koyama, Shigeru

    This study deals with the experiment to clarify the characteristics of adsorption refrigeration system employing activated carbon fiber (ACF) and ethanol pair and to evaluate the performance of adsorber/desorber heat exchanger defined by two kind of index to the system performance. The experiments are carried out by varying system running parameters such as regeneration temperature for adsorber, ethanol temperature in the evaporator, pre-heating/cooling cycle time, adsorption/desorption cycle time. Regeneration temperature for adsorber is from 60 to 90 °C and ethanol temperature is from 0 to 20 °C and pre-heating/cooling cycle time is 60 and 120 second and adsorption/desorption cycle time is from 120 to 300 second. Results show that the system can be operated with regeneration temperature of 60 °C and the system performance improves with increase of ethanol temperature. It is also found that the system performance is affected by regeneration temperature for adsorber and the pre-heating/cooling cycle time and adsorption/desorption cycle time.

  14. Effect of Hybridized Fiber Wrapped Around the Aluminum Tubes on the Crushing Performances

    Science.gov (United States)

    Ismail, A. E.; Noranai, Z.; Mohd Nor, N. H.; Mohd Tobi, A. L.; Ahmad, M. H.

    2016-11-01

    Nowadays, synthetic fibres for an example glass fibres is frequently used to wrap the metallic tubes in order to increase their load-bearing capacity. Due to environmental considerations and non-biodegradable behaviour, natural fibres or materials are increasingly used to replace synthetic fibres. The use of synthetic fibres can be minimized by combining them with natural fibres. Based on the literature survey, combining both fibres (synthetic and natural) for crushing applications are relatively new and therefore the main work of this paper is to present the crushing performances of hybridized fibres wrapped around the aluminium tubes when subjected to quasi-static crushing forces. Glass fibres are then combined with yarn kenaf fibres according to these volume fractions: 0, 25, 50, 75 and 100%. The hybridized fibres are wrapped around the tubes twice using different orientations [0o/0o], [15°/-15°], [30o/-30o] and [45o/-45o] included empty tubes before they are immersed into polyester resin bath. The composite tubes are then quasi-statically compressed using a constant cross-head displacement of 10mm/min. The force-displacement curves for each tube conditions are recorded automatically and analysed. The relation between hybridized fibbers and fibre orientations with crashworthiness parameters are investigated and discussed associating with their crushing mechanisms.

  15. Numerical analysis of air-foil shaped fin performance in printed circuit heat exchanger in a supercritical carbon dioxide power cycle

    Energy Technology Data Exchange (ETDEWEB)

    Kim, Tae Ho [Department of Mechanical Engineering, POSTECH, Pohang 790-784 (Korea, Republic of); Kwon, Jin Gyu [Division of Advanced Nuclear Engineering, POSTECH, Pohang 790-784 (Korea, Republic of); Yoon, Sung Ho [Korea Institute of Nuclear Nonproliferation and Control, Daejeon 305-348 (Korea, Republic of); Park, Hyun Sun, E-mail: hejsunny@postech.ac.kr [Division of Advanced Nuclear Engineering, POSTECH, Pohang 790-784 (Korea, Republic of); Kim, Moo Hwan [Korea Institute of Nuclear Safety, Daejeon 305-338 (Korea, Republic of); Cha, Jae Eun [Korea Atomic Energy Research Institute, Daejeon 305-353 (Korea, Republic of)

    2015-07-15

    Highlights: • Staggered arrangement affects the pressure drop but does not significantly affect to the heat transfer. • The total pressure drop is reduced, but the amount of acceleration pressure drop increases while that of frictional pressure drop decreases as the horizontal number increases. • For the vertical number, the total pressure drop decreases more largely than the horizontal number. • The objective function shows that the fully staggered arrangement shows best performance. - Abstract: One of the key issues of the PCHE technology in the supercritical CO{sub 2} Brayton cycle is to achieve an efficient and compact designs to be able to enhance heat transfer and reduce pressure drop. The issue is challenging due to the complex configuration of micro-channels in the PCHE. In this study, an innovative micro-channel equipped with an array of airfoil fins is analyzed to evaluate its performance. In so doing, sensitivity analysis with various design parameters is performed to configure the optimal arrangement of airfoil fins by using CFD analysis for Supercritical Carbon dioxide Integral Experimental Loop (SCIEL) in Korean Atomic Energy Research Institute (KAERI). Dominant geometric parameters of the fin arrangement that affects to the thermal and hydraulic performances are the horizontal, vertical and staggered pitches. ANSYS ICEM CFD and ANSYS CFX are used for the grid generation and the computational calculation. CO{sub 2} properties are used by using REFPROF software database. The inlet temperature of the hot side is 618 K and that of the cold side is 585 K. The reference mass flow rate is set as 1.2 g/s for the vertical number of 2.0, which is the Reynolds number of about 30,000. The mass flow rate changes from 0.4 to 4.8 g/s in order to investigate the Reynolds number effect. The k-ε model is selected as the turbulence model. In conclusions, the results show that the optimal arrangement of airfoil fins can be examined in terms of an objective

  16. Identification of the heat transfer coefficient over the external area of a finned tubes heat exchanger with respect to the moisture content of the air without condensation; Identification du coefficient de transfert thermique sur la surface externe d`un echangeur de chaleur a tubes et ailettes planes en fonction de l`humidite de l`air, en l`absence de condensation

    Energy Technology Data Exchange (ETDEWEB)

    Benelmir, R.; Khalfi, M.; Feidt, M. [Nancy-1 Univ. Henri-Poincare, 54 - Vandoeuvre-les-Nancy (France). Lab. d`energetique et de mecanique theorique et appliquee

    1997-04-01

    The following, which is rather oriented towards experimentation, shows the influence of the humidity content of air on heat transfer. This first article concerns heat transfer between, the external fluid (moist air) and the internal fluid (water containing glycol, whose thermal behavior inside circular tubes is well-known) in a heat exchanger of the same type as those used in automotive air conditioning (horizontal copper tubes and plane aluminium fins), in the absence of condensation. The most difficult part of this experimental work is the measurement and control of the air humidity, since one has to make sure that the measurement in certainties are not significant compared to the precision of the calculation of the heat transfer coefficient. The conclusion is that, for this type of exchanger, the heat transfer coefficient decreases with air humidity in the absence of condensation (dry wall). Some correlations have been developed with respect to the relative air humidity. An analog experimental investigation, but this time carried out in the presence of condensation (partially or completely wetted wall), is about to be completed; the obtained results will be communicated later on. (authors) 15 refs.

  17. FIN 403 UOP Course Tutorial / fin403dotcom

    OpenAIRE

    anil10

    2015-01-01

    FIN 403 Entire Course For more course tutorials visit www.fin403.com   FIN 403 Week 1 Individual Assignment Global Finance Environment Paper FIN 403 Week 1 DQ 1 FIN 403 Week 1 DQ 2 FIN 403 Week 1 Summary FIN403 Week 2 Learning Team Assignment Investment Decision Selection Paper   FIN 403 Week 2 DQ 1 FIN 403 Week 2 DQ 2 FIN 403 Week 2 Summary FIN 403 Week 3 Learning Team Assignment Foreign Exchange and Derivatives Market Paper F...

  18. FIN 403 Uop Material-fin403dotcom

    OpenAIRE

    Sandywilliam8

    2015-01-01

    FIN 403 Entire Course For more course tutorials visit www.fin403.com   FIN 403 Week 1 Individual Assignment Global Finance Environment Paper FIN 403 Week 1 DQ 1 FIN 403 Week 1 DQ 2 FIN 403 Week 1 Summary FIN403 Week 2 Learning Team Assignment Investment Decision Selection Paper   FIN 403 Week 2 DQ 1 FIN 403 Week 2 DQ 2 FIN 403 Week 2 Summary FIN 403 Week 3 Learning Team Assignment Foreign Exchange and Derivatives Market Paper F...

  19. Theory Study on Heat Transfer and Pressure Drop of Two Different Herringbone Wavy Fin and Tube Heat Exchangers%两种流路结构波纹翅片换热器换热与阻力特性的理论研究

    Institute of Scientific and Technical Information of China (English)

    严俗

    2015-01-01

    本文模拟研究了两种换热流路结构的波纹翅片换热器的换热与阻力特性。模拟结果表明换热器A的换热量略大于换热器B换热量,而换热器A制冷剂侧阻力却远大于换热器B制冷剂侧阻力。综合来看,换热器B流路优于换热器A流路。因而流路形式对换热器的换热和阻力的影响很大。%The influence of the way of refrigerant flow path on heat transfer and pressure drop characteristics of her-ringbone wavy fin and tube heat exchangers were investigated by simulation. The results show that the capacity of heat exchanger A is larger than that of heat exchanger B, but the resistance on refirigerant side of heat exchanger A is greatly more than that of heat exchanger B. By comparing the comprehensive performance of two dirrerent flow paths heat exchangers, it can be found that the way of refrigerant flow path of heat exchanger B is better than that of heat exchanger A and the way of refrigerant flow path is more important to research heat transfer and pressure drop charac-teristics.

  20. An experimental investigation of heat transfer enhancement in minichannel: Combination of nanofluid and micro fin structure techniques

    DEFF Research Database (Denmark)

    Zhang, Ji; Diao, Yanhua; Zhao, Yaohua;

    2017-01-01

    This work experimentally studied the single-phase heat transfer and pressure drop characteristics by using two heat transfer enhancement techniques (micro fin structure and nanofluids) in multiport minichannel flat tube (MMFT). MMFT consisted of numerous parallel rectangular minichannels and is w......This work experimentally studied the single-phase heat transfer and pressure drop characteristics by using two heat transfer enhancement techniques (micro fin structure and nanofluids) in multiport minichannel flat tube (MMFT). MMFT consisted of numerous parallel rectangular minichannels...... with different micro fin numbers (N = 0, 1, 2, 3 and 4) and nanofluids with three volume concentrations (φ = 0.005%, 0.01% and 0.1%) were used as test sections and working fluids respectively. Secondly, the experiments using two combined enhancement technique were performed. By using conjunctively two...

  1. Numerical Model on Frost Height of Round Plate Fin Used for Outdoor Heat Exchanger of Mobile Electric Heat Pumps

    Directory of Open Access Journals (Sweden)

    Moo-Yeon Lee

    2012-01-01

    Full Text Available The objective of this study is to provide the numerical model for prediction of the frost growth of the round plate fin for the purpose of using it as a round plate fin-tube heat exchanger (evaporator under frosting conditions. In this study, numerical model was considering the frost density change with time, and it showed better agreement with experimental data of Sahin (1994 than that of the Kim model (2004 and the Jonse and Parker model (1975. This is because the prediction on the frost height with time was improved by using the frost thermal conductivity reflecting the void fraction and density of ice crystal with frost growth. Therefore, the developed numerical model could be used for frosting performance prediction of the round plate fin-tube heat exchanger.

  2. Effect of YouTube Videos and Pictures on EFL Students' Writing Performance

    Science.gov (United States)

    Styati, Erlik Widiyani

    2016-01-01

    This research aims at investigating the effect of YouTube videos and pictures as the authentic materials on Indonesian EFL students' writing performance. The experimental research is conducted by using quasi-experimental design. This research employed two groups: an experimental and control group. This is to see which group is effective to be used…

  3. Performance improvement of double-tube gas cooler in CO2 refrigeration system using nanofluids

    Directory of Open Access Journals (Sweden)

    Sarkar Jahar

    2015-01-01

    Full Text Available The theoretical analyses of the double-tube gas cooler in transcritical carbon dioxide refrigeration cycle have been performed to study the performance improvement of gas cooler as well as CO2 cycle using Al2O3, TiO2, CuO and Cu nanofluids as coolants. Effects of various operating parameters (nanofluid inlet temperature and mass flow rate, CO2 pressure and particle volume fraction are studied as well. Use of nanofluid as coolant in double-tube gas cooler of CO2 cycle improves the gas cooler effectiveness, cooling capacity and COP without penalty of pumping power. The CO2 cycle yields best performance using Al2O3-H2O as a coolant in double-tube gas cooler followed by TiO2-H2O, CuO-H2O and Cu-H2O. The maximum cooling COP improvement of transcritical CO2 cycle for Al2O3-H2O is 25.4%, whereas that for TiO2-H2O is 23.8%, for CuO-H2O is 20.2% and for Cu-H2O is 16.2% for the given ranges of study. Study shows that the nanofluid may effectively use as coolant in double-tube gas cooler to improve the performance of transcritical CO2 refrigeration cycle.

  4. Novel High-Performance Grid Fins for Missile Control at High Speeds: Preliminary Numerical and Experimental Investigations

    Science.gov (United States)

    2006-05-01

    wings as lifting surfaces and stabilisers for their first motorised flight attempts. At present the applications of lattice wings ([1], [2]) include...0.5 m P e r f o r m a n c e Tube B 6 -1 Vacuum Shutt e r Nozzle Telescope t o V a c u u m Pump E l e c t r i c al Co n n e c t i o n

  5. A comparison of heat transfer enhancement in a medium temperature thermal energy storage heat exchanger using fins

    Energy Technology Data Exchange (ETDEWEB)

    Agyenim, Francis; Smyth, Mervyn [Centre for Sustainable Technologies, University of Ulster, Newtownabbey BT37 0QB (United Kingdom); Eames, Philip [Electronic and Electrical Engineering, Loughborough University, Leicestershire LE11 3TU (United Kingdom)

    2009-09-15

    An experimental energy storage system has been designed using a horizontal concentric tube heat exchanger incorporating a medium temperature phase change material (PCM) Erythritol, with a melting point of 117.7 C. Three experimental configurations, a control system with no heat transfer enhancement and systems augmented with circular and longitudinal fins have been studied. The results presented compare the system heat transfer characteristics using isotherm plots and temperature-time curves. The system with longitudinal fins gave the best performance with increased thermal response during charging and reduced subcooling in the melt during discharging. The experimentally measured data for the control, circular finned and longitudinal finned systems have been shown to vindicate the assumption of axissymmetry (direction parallel to the heat transfer fluid flow) using temperature gradients in the axial, radial and angular directions in the double pipe PCM system. (author)

  6. QuantiFERON–TB Gold In-Tube test performance in Denmark

    DEFF Research Database (Denmark)

    Hermansen, Thomas; Lillebaek, Troels; Hansen, Ann-Brit E;

    2014-01-01

    BACKGROUND: Little is known about the QuantiFERON-TB Gold In-Tube Test (QFT) in extreme age groups. The test performance has been reported to be impaired in children and elderly, but reports are diverging. The aim of this study was to evaluate QFT performance in patients with and without Tubercul...... in children ≥ 1 years in low endemic regions but that the test should be used with care among the elderly.......BACKGROUND: Little is known about the QuantiFERON-TB Gold In-Tube Test (QFT) in extreme age groups. The test performance has been reported to be impaired in children and elderly, but reports are diverging. The aim of this study was to evaluate QFT performance in patients with and without...

  7. Numerical simulation on heat transfer performance of vertical U-tube with different borehole fill materials

    Institute of Scientific and Technical Information of China (English)

    2006-01-01

    Heat exchange performance of vertical U-tube heat exchanger was studiedwith two different borehole fill materials and CFD software. Borehole surfa