WorldWideScience

Sample records for dryers

  1. Hair dryer burns in children.

    Science.gov (United States)

    Prescott, P R

    1990-11-01

    Three children with burn injuries caused by home hair dryers are described. In one patient the injury was believed to be accidental, and in the other two cases the injuries were deliberately caused by a caretaker. The lack of prior experience with hair dryer burns initially led to suspicion of other causes. The characteristics of each case aided in the final determination of accidental vs nonaccidental injury. These cases prompted testing of home hair dryers to determine their heat output. At the highest heat settings, the dryers rapidly generated temperatures in excess of 110 degrees C. After the dryers were turned off, the protective grills maintained sufficient temperatures to cause full-thickness burns for up to 2 minutes. These cases and the results of testing demonstrate that hair dryers must be added to the list of known causes of accidental and nonaccidental burns in children.

  2. "Dissection" of a Hair Dryer

    Science.gov (United States)

    Eisenstein, Stan; Simpson, Jeff

    2008-01-01

    The electrical design of the common hair dryer is based almost entirely on relatively simple principles learned in introductory physics classes. Just as biology students dissect a frog to see the principles of anatomy in action, physics students can "dissect" a hair dryer to see how principles of electricity are used in a real system. They can…

  3. Clothes Dryer Automatic Termination Evaluation

    Energy Technology Data Exchange (ETDEWEB)

    TeGrotenhuis, Ward E.

    2014-10-01

    Volume 2: Improved Sensor and Control Designs Many residential clothes dryers on the market today provide automatic cycles that are intended to stop when the clothes are dry, as determined by the final remaining moisture content (RMC). However, testing of automatic termination cycles has shown that many dryers are susceptible to over-drying of loads, leading to excess energy consumption. In particular, tests performed using the DOE Test Procedure in Appendix D2 of 10 CFR 430 subpart B have shown that as much as 62% of the energy used in a cycle may be from over-drying. Volume 1 of this report shows an average of 20% excess energy from over-drying when running automatic cycles with various load compositions and dryer settings. Consequently, improving automatic termination sensors and algorithms has the potential for substantial energy savings in the U.S.

  4. ``Dissection'' of a Hair Dryer

    Science.gov (United States)

    Eisenstein, Stan; Simpson, Jeff

    2008-12-01

    The electrical design of the common hair dryer is based almost entirely on relatively simple principles learned in introductory physics classes. Just as biology students dissect a frog to see the principles of anatomy in action, physics students can "dissect" a hair dryer to see how principles of electricity are used in a real system. They can discover how engineers solve problems such as how to vary between low and high heat and fan speed by simply moving the position of a single switch. Principles of alternating versus direct current, series and parallel circuits, electrical safety, voltage dividing, ac rectification, power, and measurement of resistance and continuity all come in to play.

  5. BWR Steam Dryer Alternating Stress Assessment Procedures

    Energy Technology Data Exchange (ETDEWEB)

    Morante, R. J. [Brookhaven National Lab. (BNL), Upton, NY (United States); Hambric, S. A. [Brookhaven National Lab. (BNL), Upton, NY (United States); Ziada, S. [Brookhaven National Lab. (BNL), Upton, NY (United States)

    2016-12-01

    This report presents an overview of Boiling Water Reactor (BWR) steam dryer design; the fatigue cracking failures that occurred at the Quad Cities (QC) plants and their root causes; a history of BWR Extended Power Uprates (EPUs) in the USA; and a discussion of steam dryer modifications/replacements, alternating stress mechanisms on steam dryers, and structural integrity evaluations (static and alternating stress).

  6. High Efficiency, High Performance Clothes Dryer

    Energy Technology Data Exchange (ETDEWEB)

    Peter Pescatore; Phil Carbone

    2005-03-31

    This program covered the development of two separate products; an electric heat pump clothes dryer and a modulating gas dryer. These development efforts were independent of one another and are presented in this report in two separate volumes. Volume 1 details the Heat Pump Dryer Development while Volume 2 details the Modulating Gas Dryer Development. In both product development efforts, the intent was to develop high efficiency, high performance designs that would be attractive to US consumers. Working with Whirlpool Corporation as our commercial partner, TIAX applied this approach of satisfying consumer needs throughout the Product Development Process for both dryer designs. Heat pump clothes dryers have been in existence for years, especially in Europe, but have not been able to penetrate the market. This has been especially true in the US market where no volume production heat pump dryers are available. The issue has typically been around two key areas: cost and performance. Cost is a given in that a heat pump clothes dryer has numerous additional components associated with it. While heat pump dryers have been able to achieve significant energy savings compared to standard electric resistance dryers (over 50% in some cases), designs to date have been hampered by excessively long dry times, a major market driver in the US. The development work done on the heat pump dryer over the course of this program led to a demonstration dryer that delivered the following performance characteristics: (1) 40-50% energy savings on large loads with 35 F lower fabric temperatures and similar dry times; (2) 10-30 F reduction in fabric temperature for delicate loads with up to 50% energy savings and 30-40% time savings; (3) Improved fabric temperature uniformity; and (4) Robust performance across a range of vent restrictions. For the gas dryer development, the concept developed was one of modulating the gas flow to the dryer throughout the dry cycle. Through heat modulation in a

  7. High Efficiency, High Performance Clothes Dryer

    Energy Technology Data Exchange (ETDEWEB)

    Peter Pescatore; Phil Carbone

    2005-03-31

    This program covered the development of two separate products; an electric heat pump clothes dryer and a modulating gas dryer. These development efforts were independent of one another and are presented in this report in two separate volumes. Volume 1 details the Heat Pump Dryer Development while Volume 2 details the Modulating Gas Dryer Development. In both product development efforts, the intent was to develop high efficiency, high performance designs that would be attractive to US consumers. Working with Whirlpool Corporation as our commercial partner, TIAX applied this approach of satisfying consumer needs throughout the Product Development Process for both dryer designs. Heat pump clothes dryers have been in existence for years, especially in Europe, but have not been able to penetrate the market. This has been especially true in the US market where no volume production heat pump dryers are available. The issue has typically been around two key areas: cost and performance. Cost is a given in that a heat pump clothes dryer has numerous additional components associated with it. While heat pump dryers have been able to achieve significant energy savings compared to standard electric resistance dryers (over 50% in some cases), designs to date have been hampered by excessively long dry times, a major market driver in the US. The development work done on the heat pump dryer over the course of this program led to a demonstration dryer that delivered the following performance characteristics: (1) 40-50% energy savings on large loads with 35 F lower fabric temperatures and similar dry times; (2) 10-30 F reduction in fabric temperature for delicate loads with up to 50% energy savings and 30-40% time savings; (3) Improved fabric temperature uniformity; and (4) Robust performance across a range of vent restrictions. For the gas dryer development, the concept developed was one of modulating the gas flow to the dryer throughout the dry cycle. Through heat modulation in a

  8. The modelling of a domestic tumble dryer

    Energy Technology Data Exchange (ETDEWEB)

    Deans, J. [University of Auckland (New Zealand). Dept. of Mechanical Engineering

    2001-06-01

    The characteristics of a small domestic tumbler dryer have been investigated using performance tests and a computer model of the dryer. This model, which was partially developed using the tests results, encompasses all of the energy and mass transfer routes within the complete dryer. The tests demonstrated that the mass and energy transport mechanisms within the dryer drum are not well defined, and a key feature of the model is the simplified equations used to represent these flows. There is a strong correlation between the results from the performance tests and the results predicted by the computer model. The performance test results show that the dryer examined in this study operates at much higher efficiencies than those previously reported. The dryers in the earlier studies were slightly larger and operated with larger air flow rates and higher energy inputs. The drying process generates lint, and the model has been used to demonstrate the effects which the localised accumulation of lint in a trap has on the dryer's performance. Other operational effects investigated using the model include the influence of fabric type on the performance of the dryer, the sensitivity of the dryer performance to operating conditions and the possibility of energy recovery from the exhaust stream by recirculating part of the stream through the dryer. (author)

  9. PERFORMANCE EVALUATION OF A DRYER FOR PROCESSED ...

    African Journals Online (AJOL)

    thinkexploitsint'l

    Department of Agricultural and Biosystems Engineering.University of ... The dryer consists of drying chamber, trays, chimney, electric heater, blower with centrifugal fan and prime ... The working principle of the dryer followed the steps described below. .... Agricultural Engineering International the CIGRE journal. 6(1091).

  10. Automatic Endpoint Determination for Batch Tea Dryers

    NARCIS (Netherlands)

    Temple, S.J.; Boxtel, van A.J.B.

    2000-01-01

    Agricultural Engineering and Physics, Wageningen University, Bomenweg 4, Wageningen, 6703 HD, The Netherlands Abstract: A laboratory batch fluid-bed dryer was developed for handling small samples of tea for experimental batch manufacture, and this dryer required a means of stopping drying when the p

  11. Automatic endpoint determination for batch tea dryers

    NARCIS (Netherlands)

    Temple, S.J.; Boxtel, van A.J.B.

    2001-01-01

    A laboratory batch fluid-bed dryer was developed for handling small samples of tea for experimental batch manufacture, and this dryer required a means of stopping drying when the process was complete. A control system was devised which requires only the initial weight of the sample to be entered

  12. Survey of industrial dryers for solids

    Energy Technology Data Exchange (ETDEWEB)

    Richardson, A.S.; Jensen, W.P.

    1976-07-01

    A study was directed toward obtaining data for an estimate of the current and anticipated energy demand for industrial drying operations for solid materials. Twenty-seven dryer types, including those utilizing both direct and indirect heat sources, were identified and are described. Results of an analysis made on 17 dryer types and based on data obtained from several of the largest solids dryer manufacturers indicate that industrial dryers for solids currently consume about 1.3 x 10/sup 18/ J (1.2 quads) of energy. This represents nearly 4 percent of the total United States industrial energy use. Several examples of steps being taken by industry to reduce energy requirements for solids drying are included. Still further action to reduce energy consumption of dryers is possible; implementation will depend upon the extent to which incentives are provided by fuel scarcity, fuel costs, and the perfection of new technology by industry alone and in programs with the Federal Government.

  13. Performance of indirect solar cabinet dryer

    Energy Technology Data Exchange (ETDEWEB)

    Sreekumar, A.; Manikantan, P.E.; Vijayakumar, K.P. [Solar Thermal Energy Laboratory, Department of Physics, Cochin University of Science and Technology, Kochi 682 022 (India)

    2008-06-15

    In this paper, the development and testing of a new type of efficient solar dryer, particularly meant for drying vegetables and fruit, is described. The dryer has two compartments: one for collecting solar radiation and producing thermal energy and the other for spreading the product to be dried. This arrangement was made to absorb maximum solar radiation by the absorber plate. In this dryer, the product was loaded beneath the absorber plate, which prevented the problem of discoloration due to irradiation by direct sunlight. Two axial flow fans, provided in the air inlet, can accelerate the drying rate. The dryer had six perforated trays for loading the material. The absorber plate of the dryer attained a temperature of 97.2 C when it was studied under no load conditions. The maximum air temperature in the dryer, under this condition was 78.1 C. The dryer was loaded with 4 kg of bitter gourd having an initial moisture content of 95%, and the final desired moisture content of 5% was achieved within 6 h without losing the product colour, while it was 11 h for open sun drying. The collector glazing was inclined at a particular angle, suitable to the location, for absorption of maximum solar radiation. A detailed performance analysis was done by three methods, namely 'annualized cost method', 'present worth of annual savings' and 'present worth of cumulative savings'. The drying cost for 1 kg of bitter gourd was calculated as Rs. 17.52, and it was Rs. 41.35, in the case of an electric dryer. The life span of the solar dryer was assumed to be 20 years. The cumulative present worth of annual savings over the life of the solar dryer was calculated for bitter gourd drying, and it turned out be Rs. 31659.26, which was much higher than the capital cost of the dryer (Rs. 6500). The payback period was calculated as 3.26 years, which was also very small considering the life of the system (20 years). So, the dryer would dry products free of cost

  14. Dryer

    Energy Technology Data Exchange (ETDEWEB)

    Halley, G.D.; Thwaites, C.M.M.; Talbott, M.

    1994-06-29

    An apparatus is provided for drying materials, such as natural products including crops, cereals, vegetables, timber etc., which includes a sealed chamber into which the materials are placed which retains a volume of gas. Water-vapour exchange means are provided either in the wall of the chamber unit or in a separate unit, which comprise a selectively permeable membrane which is permeable to water-vapour but impermeable to gas. A heater heats the gas inside the chamber, which absorbs water vapour from the material. The water vapour is then selectively transported through the membrane, whilst the heated gas is retained in the chamber. The drying process is energy-efficient. (author)

  15. ENERGY STAR Certified Residential Clothes Dryers

    Data.gov (United States)

    U.S. Environmental Protection Agency — Certified models meet all ENERGY STAR requirements as listed in the Version 1.0 ENERGY STAR Program Requirements for Clothes Dryers that are effective as of January...

  16. Studies on Ultrasonic Spray Dryer (1)

    OpenAIRE

    井上, 昌夫

    1981-01-01

    Author has initiated research and development activities for a epochal ultrasonic spray dryer in order to obtain large quantities of droplets in uniform diameters, from which a practically applicable ultrasonic spray dryer would possibly be developed. Since the time Wood, Loomis et al. reported their experiments on atomization of liquids by ultrasonic power, research in this field is now widely attempted in many countries. In Japan, this field is being investigated by Ohno et al. Chiba, and M...

  17. Multirack foldable solar dryer for Mango flakes

    Directory of Open Access Journals (Sweden)

    S. H. Sengar

    2012-02-01

    Full Text Available Foldable solar dryer developed and evaluated for Mango flakes drying. Mango fruits were selected as drying material. Time required for reducing the moisture content up to 10 per cent as a safe storage for solar dryer was observed for Mango flakes. Overall collection efficiency was found to be 0.97 %, whereas where pickup efficiency was found to be 15 per cent. Evaluation parameters were collection efficiency, system drying efficiency, pick-up efficiency, moisture ratio and drying rate.

  18. Improving dryer energy efficiency and controllability simultaneously by process modification

    NARCIS (Netherlands)

    Atuonwu, J.C.; Straten, G. van; Deventer, H.C. van; Boxtel, A.J.B. van

    2013-01-01

    This work establishes a relationship between dryer energy performance and controllability using energy balances and process resiliency analysis. It is shown that using the process gain matrix, the dryer energy efficiency can be reliably calculated with conditions for simultaneous controllability

  19. Affordable Hybrid Heat Pump Clothes Dryer

    Energy Technology Data Exchange (ETDEWEB)

    TeGrotenhuis, Ward E. [Pacific Northwest National Lab. (PNNL), Richland, WA (United States); Butterfield, Andrew [Jabil, St. Petersburg, FL (United States); Caldwell, Dustin D. [Pacific Northwest National Lab. (PNNL), Richland, WA (United States); Crook, Alexander [Jabil, St. Petersburg, FL (United States)

    2016-06-30

    This project was successful in demonstrating the feasibility of a step change in residential clothes dryer energy efficiency by demonstrating heat pump technology capable of 50% energy savings over conventional standard-size electric dryers with comparable drying times. A prototype system was designed from off-the-shelf components that can meet the project’s efficiency goals and are affordable. An experimental prototype system was built based on the design that reached 50% energy savings. Improvements have been identified that will reduce drying times of over 60 minutes to reach the goal of 40 minutes. Nevertheless, the prototype represents a step change in efficiency over heat pump dryers recently introduced to the U.S. market, with 30% improvement in energy efficiency at comparable drying times.

  20. Determination of Loading Capacity of a Direct Solar Boiler Dryer

    OpenAIRE

    I.A. Ikem; D. Osim-Asu; O.E. Nyong; S.A. Takim

    2016-01-01

    Thermodynamic analysis of solar boiler natural convection dryer used for drying agricultural products was employed to dry restaurant wastes. Practical steps were taken to determine the loading capacity of the dryer. Replicas of the dryer (dimensions and materials) were selected and employed but with varying loads. This dryer is made up of glass flat-plate collector which serves as the drying chamber cover. Thermodynamic properties of the working fluid were measured at input and exit points...

  1. Experimental testing of a new solar dryer

    Energy Technology Data Exchange (ETDEWEB)

    Tiris, Cigdem; Ozbalta, Necdet (Ege Univ., Izmir (Turkey). Solar Energy Inst.); Tiris, Mustafa; Dincer, Ibrahim (TUBITAK, Kocaeli (Turkey). Marmara Research Center)

    1994-06-01

    Drying of agricultural products is an energy-intensive operation. High prices and shortages in fossil fuels increase the emphasis on using solar energy as an alternative energy source, especially in developing countries. In this respect, a new solar dryer, which consisted of a solar air heater and a drying chamber, was developed and used for drying various fruits and vegetables, i.e. sultana grapes, green beans, sweet peppers and chili peppers and was successfully tested. In order to make a comparison, the traditional sun-drying experiments were employed. Results showed that the solar dryer reduced the drying time significantly and prevented mass losses, and essentially provided better product quality. (author)

  2. 40 CFR 60.252 - Standards for thermal dryers.

    Science.gov (United States)

    2010-07-01

    ...)(i) through (iii) of this section, as applicable to the affected facility. (i) For each thermal dryer...)(i) or (b)(3)(ii) of this section, as applicable to the affected facility. (i) For each thermal dryer... limits of this section. (c) Thermal dryers receiving all of their thermal input from an affected...

  3. Investigation of the drying airflow at a newly developed dryer geometry for mixed flow grain dryers

    Directory of Open Access Journals (Sweden)

    Holger Scaar

    2016-06-01

    Full Text Available The mixed-flow dryer has been a matter of investigation many times regarding drying efficiency, dryer control, and performance enhancement over the past years. However, there is still considerable demand for optimization in terms of energy efficiency and homogeneity of drying. In order to analyze the specific energy consumption and the homogeneity of the drying process, different thermodynamic process conditions have been investigated for the conventional MFD design using numerical and experimental methods. Based on the results obtained, a novel dryer design has been developed. With this, a considerable increase of efficiency is expected. As the fluid dynamic analysis of the first design draft revealed, further development is required until scaling-up and transfer into practice will be possible. While homogeneous airflow conditions could be demonstrated in the core flow region in the center of the dryer, the configuration must be optimized in the near wall regions.

  4. Study of a control system for a layered fuel dryer

    Energy Technology Data Exchange (ETDEWEB)

    Ul' shin, V.A.; Bardamid, V.I.; Menyailenko, A.S.

    1987-02-01

    Operation of coal dryers used in coal preparation plants and methods for more efficient operation control are evaluated. Mathematical model of a coal-fired dryer was developed. Factors which influence dryer operation and efficiency are discussed. A mathematical model of a coal-fired furnace for a coal dryer was also developed. Using the mathematical model a control system for a coal-fired furnace was designed. The control system, types of measuring instruments and their performance are evaluated. Recommendations for a control system for coal-fired coal dryers are made. The system permits furnace efficiency to be increased by 5-6%. 11 refs.

  5. Thermodynamic Analysis of a Mixed-Mode Solar Dryer

    Directory of Open Access Journals (Sweden)

    I.A. Ikem

    2016-02-01

    Full Text Available Thermodynamic analysis of a mixed-mode solar dryer used for restaurant wastes is presented. This dryer is made up of up of flat-plat collector and a drying chamber. Thermodynamic properties of the working fluid were measured at input and exit points. Energy and exergy balance equations at the various segments of the dryer were formulated based on the balances in the solar grains dryer. The results show that energy and exergy efficiency are approximately in direct relation to the energy loss and exergy destruction. The dried product was tested suitable for animal consumption. These results are useful for design of solar grain dryer.

  6. Drying radioactive wastewater salts using a thin film dryer

    Energy Technology Data Exchange (ETDEWEB)

    Scully, D.E.

    1998-03-19

    This paper describes the operational experience in drying brines generated at a radioactive wastewater treatment facility. The brines are composed of aqueous ammonium sulfate/sodium sulfate and aqueous sodium nitrate/sodium sulfate, The brine feeds receive pretreatment to preclude dryer bridging and fouling. The dryer products are a distillate and a powder. The dryer is a vertical thin film type consisting of a steam heated cylinder with rotor. Maintenance on the dryer has been minimal. Although many operability problems have had to be overcome, dryer performance can now be said to be highly reliable.

  7. Design of starch coated seed cotton dryers

    Science.gov (United States)

    A model was developed for the design and analysis of a high temperature tunnel dryer, primarily used with a new cotton ginning product, EASIflo ® cottonseed (starch-coated cottonseed). This form of cottonseed has emerged as a viable, value-added product for the cotton ginning industry. Currently, li...

  8. 78 FR 49607 - Energy Conservation Program: Test Procedures for Residential Clothes Dryers

    Science.gov (United States)

    2013-08-14

    ... continuously or intermittently tumbles the clothes dryer drum after the clothes dryer indicates to the user..., ``Household Tumble Type Clothes Dryers,'' and the IEC test standard 61121, ``Tumble dryers for household use... Procedures for Residential Clothes Dryers; Final Rule #0;#0;Federal Register / Vol. 78, No. 157 /...

  9. Fabric-drying process in domestic dryers

    Energy Technology Data Exchange (ETDEWEB)

    Yadav, V.; Moon, C.G. [Department of Mechanical Engineering, The University of Auckland, Auckland 1142 (New Zealand)

    2008-02-15

    A theoretical analysis of the drying process occurring inside the household electric tumbler clothes-dryer is performed to determine various thermo-physical parameters affecting the energy consumption and for the development of a simulation model. Experiments are conducted on a test set-up, based on a compact tumble-dryer, to measure the values of the parameters necessary for evaluating the performance. Widely-accepted economy standards are considered for comparison of simulation and experimental results. The simulation results are in reasonable agreement with experimental data. An empirical correlation for the specific moisture-extraction rate (SMER) is developed to translate energy-consumption information from one standard to the other. (author)

  10. Failure behaviour of a tumble dryer

    OpenAIRE

    Droessaert, Stijn; De Waele, Wim; De Groote, W; Delorge, E

    2011-01-01

    A tumble dryer is a rotating heated vessel used to fulfil a poly-condensation process of PETgranules. This step is very crucial in the entire production process of polymer fibres. System failure, causing production loss, cannot be afforded. Unfortunately, since a couple of years, the reactors suffer from severe cracking at weld details. To find the root cause(s) of this problem a detailed study of the vessel construction, the loads induced during the production process and the cracking has be...

  11. Performance evaluation of heat pump dryer.

    Science.gov (United States)

    Pal, U S; Khan, M K

    2010-03-01

    A batch type heat pump assisted dehumidified air dryer was developed successfully with a medium range of temperatures (30-41°C) for safe drying of heat sensitive crops. Dehumidification system of the developed heat pump dryer (HPD) maintained the relative humidity (RH) of air entering the drying chamber below 40%. The inlet drying air temperature decreased during early hours of drying followed by rapid rise between the 2nd and 10th h, after which the temperature was almost stable. The RH of inlet and exhaust drying air increased initially and decreased subsequently with drying time as product became drier. The HPD was found to have a specific moisture extraction rate between 0.55 and 1.10 kg/kWh. Energy consumption for HPD for 24 h of operation was found less (4.48-5.05 kWh) than the hot air dryer (5.65-9.6 kWh) while operating under different drying conditions. Better quality dried sweet pepper (Capsicum annuum L.) was obtained in HPD owing to lower drying air temperature.

  12. The Annular Microwave Dryer Design and Study on Honeysuckle

    Directory of Open Access Journals (Sweden)

    Geng Yuefeng

    2014-03-01

    Full Text Available In order to dry fresh honeysuckle, microwave drying process were studied on fresh honeysuckle; and microwave drying apparatus on fresh honeysuckle is designed according to the drying process. The designed microwave dryer contains microwave generator, microwave dryer, dehumidifying systems, control system, transmission systems, microwave leakage inhibited mechanism and other components. The drying experiment is carried by the designed dryer, from the setting-to-work test, the design was success.

  13. Thermodynamic Analysis of a Mixed-Mode Solar Dryer

    OpenAIRE

    I.A. Ikem; I.H. Iondover; O.E. Nyong; A.J. Adie

    2016-01-01

    Thermodynamic analysis of a mixed-mode solar dryer used for restaurant wastes is presented. This dryer is made up of up of flat-plat collector and a drying chamber. Thermodynamic properties of the working fluid were measured at input and exit points. Energy and exergy balance equations at the various segments of the dryer were formulated based on the balances in the solar grains dryer. The results show that energy and exergy efficiency are approximately in direct relation to the energy loss ...

  14. Critical Point Dryer: Tousimis 916B Series C

    Data.gov (United States)

    Federal Laboratory Consortium — Description: CORAL Name: Critical Point Dryer This system utilizes CO 2to dry fragile suspended and floating structures Specifications / Capabilities: Wafer size up...

  15. A Comparison of Dryer Types used for Tea Drying

    NARCIS (Netherlands)

    Temple, S.J.; Boxtel, van A.J.B.

    2000-01-01

    The objective of this work was to determine how various types of tea dryer would perform with different levels of inputs. Three dryer types were commonly found in practice, two others are not generally used and one type is unknown in practice. Simulation models for each type were constructed from a

  16. Improving dryer energy efficiency and controllability simultaneously by process modification

    NARCIS (Netherlands)

    Atuonwu, J.C.; Straten, van G.; Deventer, van H.C.; Boxtel, van A.J.B.

    2013-01-01

    This work establishes a relationship between dryer energy performance and controllability using energy balances and process resiliency analysis. It is shown that using the process gain matrix, the dryer energy efficiency can be reliably calculated with conditions for simultaneous controllability imp

  17. Heat Pump Clothes Dryer Model Development

    Energy Technology Data Exchange (ETDEWEB)

    Shen, Bo [ORNL

    2016-01-01

    A heat pump clothes dryer (HPCD) is an innovative appliance that uses a vapor compression system to dry clothes. Air circulates in a closed loop through the drum, so no vent is required. The condenser heats air to evaporate moisture out of the clothes, and the evaporator condenses water out of the air stream. As a result, the HPCD can achieve 50% energy savings compared to a conventional electric resistance dryer. We developed a physics-based, quasi-steady-state HPCD system model with detailed heat exchanger and compressor models. In a novel approach, we applied a heat and mass transfer effectiveness model to simulate the drying process of the clothes load in the drum. The system model is able to simulate the inherently transient HPCD drying process, to size components, and to reveal trends in key variables (e.g. compressor discharge temperature, power consumption, required drying time, etc.) The system model was calibrated using experimental data on a prototype HPCD. In the paper, the modeling method is introduced, and the model predictions are compared with experimental data measured on a prototype HPCD.

  18. 76 FR 50145 - Energy Conservation Program: Test Procedures for Residential Clothes Dryers

    Science.gov (United States)

    2011-08-12

    ... (AHAM) clothes dryer test standard HLD-1-2009, ``Household Tumble Type Clothes Dryers,'' and the International Electrotechnical Commission (IEC) test standard 61121, ``Tumble dryers for household use--Methods... Residential Clothes Dryers AGENCY: Office of Energy Efficiency and Renewable Energy, Department of...

  19. Engineering analysis of a rotary dryer: drying of wood particles

    Energy Technology Data Exchange (ETDEWEB)

    Kamke, F.A.

    1984-01-01

    Rotary dryers are the most commonly used wood drying system in the particleboard industry. These dryers also play an increasingly important role in drying wood residues for fuel. A rotary dryer simulation model was developed, in the form of a computer program, for the purpose of analyzing the drying behavior of wood particles. The approach used in the model development analyzed the rotary drying process in a sequential manner. Beginning with a study of particle residence time in a rotary drum, the process of heat transfer, and then mass transfer, were incorporated to yield a complete rotary dryer simulation model. The resultant computer program does not require empirical constants or equations developed for a particular rotary dryer system. Experiments on a commercially manufactured rotary dryer were performed to check the performance of the simulation model as a predictor of overall residence time and drying behavior. Comparison between the predictions and the measured results were good, indicating a percent root mean square error of 22.2 in the prediction of the outlet particle moisture content. The rotary dryer simulation model developed in this study should prove useful for optimizing process parameters in the drying of wood particles.

  20. Rayon from Dryer Lint: A Demonstration

    Science.gov (United States)

    Knopp, Michael A.

    1997-04-01

    In this demonstration, ordinary household dryer lint from the laundering of cotton items is stirred into the traditional Schweizer reagent mixture, a saturated solution of copper (II) carbonate in concentrated ammonium hydroxide. Any insoluble material (i.e. hair) is removed with a glass rod. The resulting deep blue viscous solution is taken up in an eye dropper and extruded into a 190 x 100 mm glass recrystallizing dish, which contains a dilute (3M) solution of sulfuric acid. Threads of rayon several cm in length can be thus formed. These threads are best viewed by the audience on an overhead projector. The sulfuric acid solution and threads are disposed of in compliance with local environmental regulations.

  1. Heat transfer and energy efficiency in infrared paper dryers

    Energy Technology Data Exchange (ETDEWEB)

    Pettersson, Magnus

    1999-11-01

    Infrared (IR) dryers are widely used in the paper industry, mainly in the production of coated paper grades. The thesis deals with various aspects of heat transfer and energy use in infrared heaters and dryers as employed in the paper industry. Both gas-fired and electric IR dryers are considered and compared. The thesis also provides an introduction to infrared heaters and infrared drying, including a review of recent literature in the field. The transport of thermal radiation inside a paper sheet was investigated and different IR dryers were compared in terms of their ability to transfer energy to the internal parts of a paper sheet. Although there were evident differences in the absorption of radiation between gas-fired and electric IR dryers, the distinction was found not to be as important as has generally been believed. The main differences appeared to be due to the choice of a one- or a two-sided dryer solution, rather than the spectral distributions emitted by the dryers. A method for evaluating the radiation efficiency of IR heaters was proposed. An electric IR heater was evaluated in the laboratory. The radiation efficiency of the heater was shown to be strongly dependent on the power level. The maximum efficiency, found at high power level, was close to 60 %. A procedure for evaluation of the total energy transfer efficiency of an infrared paper dryer was proposed and used in the evaluation of an electric IR dryer operating in an industrial coating machine. The efficiency of the dryer was roughly 40 %. A model for an electric IR heater was developed. The model includes non-grey radiative heat transfer between the different parts of the heater, as well as conduction in reflector material and convective cooling of the surfaces. Using IR module voltage as the only input, model predictions of temperatures and heat flux were found to agree well with experimental data both at steady state and under transient conditions. The model was also extended to include

  2. [Burn wounds caused by a hair-dryer].

    Science.gov (United States)

    Paulsen, Ida Felbo; Alsbjørn, Bjarne

    2014-06-01

    Burn wounds (ambustio) in children are frequent and occur in about 5% of all children and in about half of these before the age of three. The majority of the burn wounds in children occur at home, most frequently in the kitchen or the bathroom. This case describes an accidental ambustio caused by a hair dryer in a 3-month-old baby. Hair-dryers have become widely used in drying soar baby buttoms. Therefore, professionals as well as parents should be better informed about the potential risks of using hair-dryers for this purpose.

  3. Heat-pump-assisted dryer: Pt. 1; Mathematical model

    Energy Technology Data Exchange (ETDEWEB)

    Pendyala, V.R.; Devotta, S.; Patwardhan, V.S. (National Chemical Lab., Poona (India))

    1990-07-01

    A mathematical model for an integrated heat-pump-assisted dryer has been developed. The dryer has been modelled considering the heat transfer and simultaneous heat and mass transfer zones. The heat-pump heat exchangers have been modelled by writing the enthalpy balance for differential lengths considering the various zones on the air and working-fluid sides. The compressor has been described by the polytropic compression equation. The model has been used for simulating an existing system using R11 to study the effect of approach velocity of air to the evaporator and of the suction superheat on the specific energy consumption of the heat pump assisted dryer. (author).

  4. Review:Resuspension of wall deposits in spray dryers

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    Wall deposition occurs in spray dryers when dried or partially dried particles contact and adhere to the walls during operation, thus reducing the yield of product collected. Wall deposits also present a product contamination risk and a fire or explosion risk when spray drying products that oxidize exothermically, such as milk powder. Re-entrainment is the resuspension of spray dryer wall deposits into the main gas stream for collection as product. Literature suggests that the process for re-entrainment of particles from spray dryer wall deposits is strongly dependent on particle size and gas velocity.

  5. Critical Point Dryer: Tousimis 916B Series C

    Data.gov (United States)

    Federal Laboratory Consortium — Description:CORAL Name: Critical Point DryerThis system utilizes CO 2to dry fragile suspended and floating structures Specifications / Capabilities:Wafer size up to...

  6. Modeling and simulation of milk emulsion drying in spray dryers

    Directory of Open Access Journals (Sweden)

    V. S. Birchal

    2005-06-01

    Full Text Available This work aims at modeling and simulating the drying of whole milk emulsion in spray dryers. Drops and particles make up the discrete phase and are distributed into temporal compartments following their residence time in the dryer. Air is the continuous and well-mixed phase. Mass and energy balances are developed for each phase, taking into account their interactions. Constitutive equations for describing the drop swelling and drying mechanisms as well as the heat and mass transfer between particles and hot air are proposed and analyzed. A set of algebraic-differential equations is obtained and solved by specific numerical codes. Results from experiments carried out in a pilot spray dryer are used to validate the model developed and the numerical algorithm. Comparing the simulated and experimental data, it is shown that the model predicts well the individual drop-particle history inside the dryer as well as the overall outlet air-particle temperature and humidity.

  7. Analysis of Slurry Drying in a Spray Dryer

    Directory of Open Access Journals (Sweden)

    Wittaya Julklang

    2014-01-01

    Full Text Available Spray drying has recently been exploited to prepare a large variety of high-value particles. The aim of the present paper is to analyze the drying mechanism of slurry droplets consist of nanosized particles in an industrial-scale spray dryer. For this purpose, a mathematical model is developed comprising a comprehensive model for the heat and mass transfer for a single droplet and a model for the flow of droplets and gas, and the heat and mass transfer in the dryer. Using the developed model, the drying behaviour of slurry droplets in the spray dryer is investigated in the initial heating-up, constant rate and falling rate periods by analyzing the profiles of air temperature and humidity, and the droplet velocity, average temperature and moisture content in the dryer axial direction as well as the distributions of temperature and water vapor concentration in the droplet.

  8. Application of Constrained Linear MPC to a Spray Dryer

    OpenAIRE

    2014-01-01

    In this paper we develop a linear model predictive control (MPC) algorithm for control of a two stage spray dryer. The states are estimated by a stationary Kalman filter. A non-linear first-principle engineering model is developed to simulate the spray drying process. The model is validated against experimental data and able to precisely predict the temperatures, the air humidity and the residual moisture in the dryer. The MPC controls these variables to the target and reject disturbances. Sp...

  9. Evaluation of hybrid solar – biomass dryer with no load

    Directory of Open Access Journals (Sweden)

    Yassen Tadahmun Ahmed

    2014-07-01

    Full Text Available Experimental study was carried out to investigate the performance of designed and fabricated hybrid solar-biomass dryer without load. The solar side was a natural convection mixed mode, while the biomass side was a hot air produced from a burner/gas to gas heat exchanger. The experiments have been conducted to test the dryer temperature, inlet and outlet relative humidity, outlet velocity, and biomass feeding rate. In the solar mode the maximum dryer temperature was 63°C. Behaviours of the velocity in the dryer was found to follow solar radiation available to the dryer. The velocity was in the range of 0.6 – 1.35 m/s through the 0.0176 m2 area of the outlet when the solar radiation was in the range of 150 – 880 W/m2. Two feeding rates of wood were used to investigate the dryer performance through the night. The results showed that at feeding rate 278 g/hr, the drying air mean temperature was 62 ºC. This temperature was more suitable than the measured drying air temperature at feeding rate 490 g/hr. Also the 62 °C drying environment is more stable and feasible for drying almost all types of products.

  10. Bed mixing dryer for high moisture content fuels

    Energy Technology Data Exchange (ETDEWEB)

    Hulkkonen, S.; Heinonen, O. [Imatran Voima Oy, Vantaa (Finland)

    1997-12-31

    Bed mixing dryer is a new type of fuel drying technology for fluidized bed combustion. The idea is to extract hot bed material from the fluidized bed and use it as a heat source for drying the fuel. Drying occurs at steam atmosphere which makes it possible to recover the latent heat of evaporation to process. This improves the thermal efficiency of the power plant process considerably, especially in combined heat and power applications. Imatran Voima Oy (IVO) has developed the Bed Mixing Dryer technology since early 1990s. The first pilot plant was built in 1994 to IVO`s Kuusamo peat and wood fired power plant. The capacity of the plant is 6 MW{sub e} and 20 MW of district heat. In Kuusamo the dryer is connected to a bubbling fluidized bed. Since it`s commissioning the dryer has been used successfully for about 3000 hours during the heating season in wintertime. The second application of the technology will be a demonstration project in Oerebro (S). IVO Power Engineering Ltd will supply in 1997 a dryer to Oerebro Energi`s peat, wood and coal fired CHP plant equipped with circulating fluidized bed boiler. The fuel to be dried is sawdust with fuel input of about 60 MW. In Kuusamo the dryer produces 3 MW of additional district heat and in Oerebro 6 MW. The fuels in Kuusamo are peat, saw dust and bark. In addition to the municipal heat production this type of drying technology has its benefits in pulp and paper industry processes. Disposal of paper mill sludges is becoming more difficult and costly which has resulted in need of alternative treatment. Drying of the sludge before combustion in a boiler for power production is an attractive option. At the moment IVO is carrying out several studies to apply the Bed Mixing Dryer in pulp and paper industry processes. Economy of drying the sludge looks promising

  11. Performance of modified greenhouse dryer with thermal energy storage

    Directory of Open Access Journals (Sweden)

    Om Prakash

    2016-11-01

    Full Text Available In this attempt, the main goal is to do annual performance, environomical analysis, energy analysis and exergy analysis of the modified greenhouse dryer (MGD operating under active mode (AM and passive mode (PM. Thermal storage is being applied on the ground of MGD. It is applied in three different ways namely barren floor, floor covered with black PVC sheet (PVC and Black Coated. Experimental study of dryers in no-load conditions reveals that floor covered with a black PVC sheet is more conducive for drying purpose than other floors. The MGD under AM is found to be more effective as compared to PM for tomato and capsicum, which are high moisture content crops. For medium moisture content crop (potato chips, both dryers show relatively similar drying performance. Crops dried inside the greenhouse dryer are found to be more nutrient than open sun dried crops. The payback period of the modified greenhouse dryer under passive mode is found to be 1.11 years. However, for the active mode of the modified greenhouse dryer is only 1.89 years. The embodied energy of the passive mode of the dryer is a 480.277 kWh and 628.73 kWh for the active mode of the dryer. The CO2 emissions per annum for passive and active mode greenhouse dryers are found to be 13.45 kg and 17.6 kg respectively. The energy payback time, carbon mitigation and carbon credit have been calculated based type of crop dried. The range of exergy efficiency is 29%–86% in MGD under PM and 30%–78% in the MGD under AM. The variation of Heat utilization factor (HUF for MGD under PM is 0.12–0.38 and 0.26–0.53 for MGD under AM. The range of co-efficient of performances (COP for MGD under PM is 0.55–0.87 and 0.58–0.73 for MGD under AM.

  12. Noise impacts from professional dog grooming forced-air dryers

    Directory of Open Access Journals (Sweden)

    Peter M Scheifele

    2012-01-01

    Full Text Available This study was designed to measure the sound output of four commonly used brands of forced-air dryers used by dog groomers in the United States. Many dog groomers have questions about the effect of this exposure on their hearing, as well as on the hearing of the dogs that are being groomed. Readings taken from each dryer at 1 meter (the likely distance of the dryer from the groomer and the dog showed average levels ranging from 105.5 to 108.3 dB SPL or 94.8 to 108.0 dBA. Using the 90 dBA criterion required by the US Occupational Safety and Health Administration, dog groomers/bathers are at risk if exposure to the lowest intensity dryer (94.8 dBA exceeds 4 hours per day. If the more stringent 85 dBA criterion and 3 dB tradeoff is applied, less than one hour of exposure is permissible in an 8 hour day. Cautions are recommended for any persons exposed to noise from forced-air dryers.

  13. Study on Predrying by Spin Flash Dryer for Granulation

    Institute of Scientific and Technical Information of China (English)

    王晓静; 叶鸣; 钱树德

    2004-01-01

    Spin flash dryer has the advantages of both fluidized bed dryer and pneumatic dryer.It has predominance in dealing with thermal sensitive materials.In this paper,the distribution of the air velocity in the spin flash dryer is discussed,which indicates that the rotating air in the dryer chamber can be divided into two areas,potential flow area and plane swirl area.Experiments show that air tangent velocity effects the process of granulation most remarkably.The radial distribution and moisture content of the particles have their intrinsic rules along either the diameter or height of the drying chamber.Besides,the operating parameters of predrying on bleaching powder are optimized.To meet the strict standard of the wet-pressing granulator on the moisture content of the feeder,a narrow lap is made at proper height in the wall of the drying chamber,where a chute and a rotating valve are installed in order to predry the filter cake and remove a part of water.Then the material is fed into the wet-pressing granulator.

  14. 75 FR 27504 - Substantial Product Hazard List: Hand-Held Hair Dryers

    Science.gov (United States)

    2010-05-17

    ... substantial product hazard.'' B. The Product A hand-held hair dryer is a portable electrical appliance with a..., electrically energized wires across which a fan blows air. These dryers are typically used in bathrooms...

  15. 76 FR 37636 - Substantial Product Hazard List: Hand-Supported Hair Dryers

    Science.gov (United States)

    2011-06-28

    .... The Product A hand-supported hair dryer is a portable electrical appliance with a cord-and-plug..., electrically energized wires, across which a fan blows air. These dryers are typically used in bathrooms...

  16. 78 FR 42389 - Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and...

    Science.gov (United States)

    2013-07-16

    ... Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and Room Air.... SUMMARY: This final rule corrects the energy conservation standards for room air conditioners. In the direct final rule establishing amended energy conservation standards for residential clothes dryers...

  17. Bringing coal preheating in drum dryers to a commercial level

    Energy Technology Data Exchange (ETDEWEB)

    Babanin, B.I.; Proushin, Yu.E.; Dinel' t, V.M.; Nikolaeva, V.Z.; Shabarshova, Yu.V.; Patrushev, A.N.; Vodop' yanov, A.G.; Vlasov, V.S.; Sementin, V.P.

    1988-10-01

    Discusses operation of a system for coal charge preheating used in Western Siberia since 1965. It is the first coal preheating system constructed in the USSR. The following aspects of system operation are discussed: composition of combustion gases used for coal drying, drying temperature, consumption rate of combustion gases depending on coal moisture content, flue gas recirculation system, transport and storage of dried coal, methods for dust separation (wet and dry), air pollution from coal dryers, and efficiency of air pollution control. Operation of the coal preheating system shows that one-stage coal drying and preheating is economic but associated with increased investment (construction cost) and with increased coal comminution. Large one-stage dryers also cause irregular coal preheating depending on distribution of coal grain size (with overheating of coal fines). Recommendations for design modifications of one-stage dryers are made. 3 refs.

  18. Development of polyhouse type solar dryer for Kashmir valley.

    Science.gov (United States)

    Shahi, Navin Chandra; Khan, Junaid N; Lohani, Umesh C; Singh, Anupama; Kumar, Anil

    2011-06-01

    Polyhouse type solar dryer (PSD) consist of drying chamber, drying trays and exhaust fan was developed for drying fruits and vegetables. The relative humidity (RH) inside the PSD varied in between 21 to 74% as compared to outside RH which ranged from 40 to 75%. The performance was found suitable and resulted in efficient drying at low RH. The thermal performance test for PSD under full and no load testing conditions were calculated. The temperature inside the dryer was 62 to 76% higher than the ambient conditions. PSD was helpful in reducing the drying ranging from 33 to 53%. The capacity of PSD was 100-150 kg per batch. The economic cost of solar dryer was compared with mechanical drying for beneficial to local producer. The cost of PSD Rs 80,000 could recover within the period of 1.5 years by adopting solar drying technology.

  19. Behavior of a portable solar dryer for pineapple fiber

    OpenAIRE

    Moya, Róger; Solano, Marco

    2012-01-01

    In Costa Rica, there has been a growing interest to use pineapple fiber from plant, for which current processes need to be improved or new processes need to be developed, with emphasis on drying methods. This work presents the design and evaluation of the behavior of a prototype portable solar dryer in four sites of Costa Rica. The design describes the main parts of the dryer, as well as how they were constructed. The behavior was evaluated according to temperature and relative humidity insid...

  20. PIV measurements of flow structures in a spray dryer

    DEFF Research Database (Denmark)

    Meyer, Knud Erik; Velte, Clara Marika; Ullum, Thorvald

    2011-01-01

    Stereoscopic Particle Image Velocimetry (PIV) measurements are made in horizontal planes in a simplified scale model of a spray dryer using water as fluid. The sample rate was sufficient to resolve phenomena at lower frequencies. Data reveal asymmetric velocity fields in both mean fields and dyna......Stereoscopic Particle Image Velocimetry (PIV) measurements are made in horizontal planes in a simplified scale model of a spray dryer using water as fluid. The sample rate was sufficient to resolve phenomena at lower frequencies. Data reveal asymmetric velocity fields in both mean fields...

  1. Performance of a solar box cooker-cum-dryer

    Energy Technology Data Exchange (ETDEWEB)

    Patel, R.S. [VP and RPTP Science College, Vallabh Vidyanagar, Gujarat (India); Patel, P.D.; Vinodkumar, P.C.; Joshipura, K.N. [Sardar Patel Univ., Vallabh Vidyanagar, Gujarat (India)

    2004-07-01

    The present investigation aims at a simultaneous theoretical and experimental investigation on different aspects of box type solar cooker, and its conversion as a dryer. A theoretical model has been attempted to simulate various thermal processes in a box type solar cooker. The theoretical study has also helped us to identify the sensitive heat exchange coefficients of the different cooker elements. The cooker-dryer designed presently has a potential of enhancing the device utility factor by a fairly large magnitude. This device will also give boost to adopt the solar energy utilization especially in the tropical developing countries. (orig.)

  2. 75 FR 37593 - Energy Conservation Program for Consumer Products: Test Procedures for Clothes Dryers and Room...

    Science.gov (United States)

    2010-06-29

    ... procedure additional language based upon provisions from European Standard EN 61121, ``Tumble dryers for... Dryers and Room Air Conditioners; Proposed Rule #0;#0;Federal Register / Vol. 75 , No. 124 / Tuesday... Conservation Program for Consumer Products: Test Procedures for Clothes Dryers and Room Air Conditioners...

  3. 78 FR 151 - Energy Conservation Program: Test Procedures for Residential Clothes Dryers

    Science.gov (United States)

    2013-01-02

    ... clothes dryer to mean a cabinet-like appliance designed to dry fabrics in a tumble- type drum with forced... standard HLD-1-2009, ``Household Tumble Type Clothes Dryers,'' and the IEC test standard 61121, ``Tumble... Procedures for Residential Clothes Dryers; Proposed Rule #0;#0;Federal Register / Vol. 78 , No. 1 /...

  4. Polybrominated Diphenyl Ethers in Dryer Lint: An Advanced Analysis Laboratory

    Science.gov (United States)

    Thompson, Robert Q.

    2008-01-01

    An advanced analytical chemistry laboratory experiment is described that involves environmental analysis and gas chromatography-mass spectrometry. Students analyze lint from clothes dryers for traces of flame retardant chemicals, polybrominated diphenylethers (PBDEs), compounds receiving much attention recently. In a typical experiment, ng/g…

  5. Design and Construction of a Passive Solar Power Clothing Dryer

    Directory of Open Access Journals (Sweden)

    Ali Alahmer

    2014-04-01

    Full Text Available This manuscript presents the design and construction of the energy efficient, time saving, cost effective of passive solar powered clothes dryer. This manuscript begins with a derivation of mathematical model represents of solar dryer followed with an analysis of the elements necessary for successfully designing the various components of a solar dryer. The solar drying performance achieved an average drying rate of 0.35 kg/h and drying time of 3 h in a typical day, even under local low ambient humidity of around 35% and at moderate outdoor wind speed. Also, the computational fluid dynamic CFD of transient thermal behavior based on Navier-Stokes equations was used to demonstrate the prevailing temperature rises in the solar natural-ventilation system associated with the internal heat flux due to solar radiation and moisture removal. The efficiency of solar dryer was improved using Nano coating technology. The result showed good agreement between the computational solid simulation and the experimental measurements obtained from this system.

  6. Configuration and Development of a Solar Cloth Dryer

    Directory of Open Access Journals (Sweden)

    Kirar Dheeraj Singh

    2016-01-01

    Full Text Available This unique duplicate shows effective blueprint and headway of effective imperativeness profitable, effective, useful of disconnected sun arranged energized pieces of clothing dryer. This unique duplicate begins with an incitement of numerical model addresses of sun arranged dryer brought after with an examination of effective segments basic as long as viably arranging effective distinctive parts of daylight based dryer. Effective sun arranged drying execution achieved an ordinary drying rate of 0.35 kg/h and drying time of 3 h in a regular day, even under neighborhood low incorporating clamminess of around 35% and at moderate outside wind speed. Fur effective more, effective computational fluid component CFD of transient warm direct in light of Navies-Stokes numerical articulations was used to demonstrate effective overall temperature rises in effective sun based typical ventilation system associated with effective inside warmth flux on account of sun fueled radiation and moistness clearing. Effective viability of sun situated dryer was upgraded using Nano covering development. Effective result showed incredible assertion between effective computational solid multiplication and effective test estimations procured from this system.

  7. Solar dryer with thermal storage and biomass-backup heater

    Energy Technology Data Exchange (ETDEWEB)

    Madhlopa, A. [Department of Physics and Biochemical Sciences, Malawi Polytechnic, P/Bag 303, Blantyre 3 (Malawi); Ngwalo, G. [Department of Mechanical Engineering, Malawi Polytechnic, P/Bag 303, Blantyre 3 (Malawi)

    2007-04-15

    An indirect type natural convection solar dryer with integrated collector-storage solar and biomass-backup heaters has been designed, constructed and evaluated. The major components of the dryer are biomass burner (with a rectangular duct and flue gas chimney), collector-storage thermal mass and drying chamber (with a conventional solar chimney). The thermal mass was placed in the top part of the biomass burner enclosure. The dryer was fabricated using simple materials, tools and skills, and it was tested in three modes of operation (solar, biomass and solar-biomass) by drying twelve batches of fresh pineapple (Ananas comosus), with each batch weighing about 20 kg. Meteorological conditions were monitored during the dehydration process. Moisture and vitamin C contents were determined in both fresh and dried samples. Results show that the thermal mass was capable of storing part of the absorbed solar energy and heat from the burner. It was possible to dry a batch of pineapples using solar energy only on clear days. Drying proceeded successfully even under unfavorable weather conditions in the solar-biomass mode of operation. In this operational mode, the dryer reduced the moisture content of pineapple slices from about 669 to 11% (db) and yielded a nutritious dried product. The average values of the final-day moisture-pickup efficiency were 15%, 11% and 13% in the solar, biomass and solar-biomass modes of operation respectively. It appears that the solar dryer is suitable for preservation of pineapples and other fresh foods. Further improvements to the system design are suggested. (author)

  8. Operation experiences of biofuel dryers; Drifterfarenheter fraan aangtorkar och direkta roekgastorkar

    Energy Technology Data Exchange (ETDEWEB)

    Berge, Christian; Dejfors, Charlotte [AaF Energikonsult Stockholm AB (Sweden)

    2000-01-01

    A study regarding operation experiences of indirect steam dryers and direct flue gas dryers of biofuels has been conducted. In the study, plants with the two types of dryers have been visited and operational experiences have been gathered and analysed. Results show that the well proven technique with flue gas dryers has a higher availability than the steam dryers. Several plants have problem with the feeding and discharge systems. Material selection is very important to prevent corrosion. Indirect steam dryers have more environmental regulations than flue gas dryers because of the generated condensate from the fuel drying process. Future work should concentrate on material selections, refining the feeding and discharge systems and control system.

  9. Performances of continuous dryer with inert medium fluidized bed

    Directory of Open Access Journals (Sweden)

    Arsenijević Zorana Lj.

    2008-01-01

    Full Text Available A fluid bed dryer with inert particles represents a very attractive alternative to other drying technologies according to the main efficiency criteria, i.e. specific water evaporation rate, specific heat consumption and speci­fic air consumption. A high drying efficiency results from the large con­tact area and from the large temperature difference between the inlet and outlet air. A rapid mixing of the particles leads to nearly isothermal conditions throughout the bed. A fluid bed dryer with inert particles was used for drying of slurries. Experiments were performed in a cylindrical column 215 mm in diameter with glass spheres as inert particles. In this paper, results of drying experi­ments with slurries of Zineb fungicide, copper hydroxide, calcium carbo­nate and pure water used as the feed material are presented. In our fluidized bed we successfully dried a number of other materials such as: fungicides and pesticides (Ziram, Propineb, Mangozeb, copper oxy-chloride, copper oxy-sulphate, Bordeaux mixture, other inorganic compounds (calcium sulphate, cobalt carbonate, electrolytic copper, sodium chloride, and a complex compound (organo-bentonite. The effects of operating conditions on dryer throughput and product quality were investigated. Main performance criteria, i.e. specific water evaporation rate, specific heat consumption and specific air consumption, were quantified. Temperature profile along the bed was mapped, and nearly isothermal conditions were found due to thorough mixing of the particles. Analysis of drying and energy efficiencies as a function of inlet and outlet air temperature difference was performed for deeper insight in dryer behavior and for optimizing dryer design and operation from an energy point of view. A simple mathematical model based on an overall heat balance predicts the dryer performance quite well. The industrial prototype with fluid bed of 0.8 m in diameter and capacity 650 kg of evaporated moisture per

  10. Design and performance evaluation of a new hybrid solar dryer for banana

    Energy Technology Data Exchange (ETDEWEB)

    Amer, B.M.A. [Agricultural Engineering Department, Faculty of Agriculture, Cairo University, Giza 12613 (Egypt); Hossain, M.A. [FMP Engineering Division, Bangladesh Agricultural Research Institute, Gazipur 1701 (Bangladesh); Gottschalk, K. [Leibniz-Institut fuer Agrartechnik Potsdam-Bornim, 100 Max-Eyth-Allee, 14467 Potsdam (Germany)

    2010-04-15

    A hybrid solar dryer was designed and constructed using direct solar energy and a heat exchanger. The dryer consists of solar collector, reflector, heat exchanger cum heat storage unit and drying chamber. The drying chamber was located under the collector. The dryer was operated during normal sunny days as a solar dryer, and during cloudy day as a hybrid solar dryer. Drying was also carried out at night with stored heat energy in water which was collected during the time of sun-shine and with electric heaters located at water tank. The efficiency of the solar dryer was raised by recycling about 65% of the drying air in the solar dryer and exhausting a small amount of it outside the dryer. Under Mid-European summer conditions it can raise up the air temperature from 30 to 40 C above the ambient temperature. The solar dryer was tested for drying of ripe banana slices. The capacity of the dryer was to dry about 30 kg of banana slices in 8 h in sunny day from an initial moisture content of 82% to the final moisture content of 18% (wb). In the same time it reduced to only 62% (wb) moisture content in open sun drying method. The colour, aroma and texture of the solar dried products were better than the sun drying products. (author)

  11. Energy Efficient Dryer with Rice Husk Fuel for Agriculture Drying

    Directory of Open Access Journals (Sweden)

    M. Djaeni

    2015-02-01

    Full Text Available Energy usage is crucial aspect on agriculture drying process. This step spends about 70% of total energy in post harvest treatment. The design of efficient dryer with renewable energy source is urgently required due to the limitation of fossil fuel energy. This work discusses the performance of air dehumidification using rice husk fuel as heat source for onion, and paddy drying. Unlike conventional dryer, the humidity of air during the drying was dehumidified by adsorbent. Hence, the driving force of drying can be  kept high.  As consequences, the drying time and energy usage can be reduced. Here, the research was conducted in two step: laboratory and pilot scale tests. Results showed that the lowering air humidity with rice husk fuel has improved the energy efficiency. At operational temperature 60oC, the heat efficiency of 75%  was achieved. 

  12. Application of Constrained Linear MPC to a Spray Dryer

    DEFF Research Database (Denmark)

    Petersen, Lars Norbert; Poulsen, Niels Kjølstad; Niemann, Hans Henrik;

    2014-01-01

    In this paper we develop a linear model predictive control (MPC) algorithm for control of a two stage spray dryer. The states are estimated by a stationary Kalman filter. A non-linear first-principle engineering model is developed to simulate the spray drying process. The model is validated against...... experimental data and able to precisely predict the temperatures, the air humidity and the residual moisture in the dryer. The MPC controls these variables to the target and reject disturbances. Spray drying is a cost-effective method to evaporate water from liquid foods and produces a free flowing powder....... The main challenge of spray drying is to meet the residual moisture specification and prevent powder from sticking to the chamber walls. By simulation we compare the performance of the MPC against the conventional PID control strategy. During an industrially recorded disturbance scenario, the MPC increases...

  13. Performance Evaluation Of A Grain Maize Solar Dryer

    OpenAIRE

    Osondu L. C.; Ugwuoke E.C; Chikelu C. C.; Eze N.N; Ukwuani S.T

    2015-01-01

    Abstract Drying under direct sunlight is one of the oldest techniques used by mankind to preserve Agriculture based food and non-food products. This paper focused on the use of solar dryer to reduce the moisture content of Agriculture produce such as maize. The experiment performed showed the moisture content of maize reduced from 20 to 13. It was also observed that the temperature increased with time. The assumed maximum temperature of the collector plate in the experiment was 100.

  14. The effect of dryer load on freeze drying process design.

    Science.gov (United States)

    Patel, Sajal M; Jameel, Feroz; Pikal, Michael J

    2010-10-01

    Freeze-drying using a partial load is a common occurrence during the early manufacturing stages when insufficient amounts of active pharmaceutical ingredient (API) are available. In such cases, the immediate production needs are met by performing lyophilization with less than a full freeze dryer load. However, it is not obvious at what fractional load significant deviations from full load behavior begin. The objective of this research was to systematically study the effects of variation in product load on freeze drying behavior in laboratory, pilot and clinical scale freeze-dryers. Experiments were conducted with 5% mannitol (high heat and mass flux) and 5% sucrose (low heat and mass flux) at different product loads (100%, 50%, 10%, and 2%). Product temperature was measured in edge as well as center vials with thermocouples. Specific surface area (SSA) was measured by BET gas adsorption analysis and residual moisture was measured by Karl Fischer. In the lab scale freeze-dryer, the molar flux of inert gas was determined by direct flow measurement using a flowmeter and the molar flux of water vapor was determined by manometric temperature measurement (MTM) and tunable diode laser absorption spectroscopy (TDLAS) techniques. Comparative pressure measurement (capacitance manometer vs. Pirani) was used to determine primary drying time. For both 5% mannitol and 5% sucrose, primary drying time decreases and product temperature increases as the load on the shelves decreases. No systematic variation was observed in residual moisture and vapor composition as load decreased. Further, SSA data suggests that there are no significant freezing differences under different load conditions. Independent of dryer scale, among all the effects, variation in radiation heat transfer from the chamber walls to the product seems to be the dominant effect resulting in shorter primary drying time as the load on the shelf decreases (i.e., the fraction of edge vials increases).

  15. Learning sustainability by developing a solar dryer for microalgae retrieval

    Directory of Open Access Journals (Sweden)

    Benedita Malheiro

    2016-01-01

    Full Text Available Excessive fossil fuel consumption is driving the search for alternative energy production solutions and, in particular, for sustainable sources of energy such as microalgae, from which biodiesel, among other useful compounds, can be obtained. After producing the microalgae, they must be harvested and dried. Existing drying solutions consume too much energy and are, therefore, expensive and unsustainable. The goal of this EPS@ISEP Spring 2013 project was to develop a solar microalgae dryer for the microalgae laboratory of ISEP. A multinational team of five students from distinct fields of study was responsible for designing and building the solar microalgae dryer prototype. The prototype includes a control system to ensure that the microalgae are not destroyed during the drying process. The solar microalgae dryer works as a distiller, extracting the excess water from the microalgae suspension. This paper details the design steps, the building technologies, the ethical and sustainable concerns and compares the prototype with existing solutions. The proposed sustainable microalgae drying process is competitive as far as energy usage is concerned. Finally, the project contributed to increase the team’s sustainable development awareness, active learning and motivation.

  16. PERFORMANCE ASSESSMENT OF SOLAR DRYER WITH INDIRECT HEATING

    Directory of Open Access Journals (Sweden)

    Boryana Brashlyanova

    2014-03-01

    Full Text Available The performed tests were designed to identify and analyze the parameters of drying in a authors model solar dryer. They to be the basis for constructing of an improved model. Drying was carried out in a pilot model solar dryer with prunes in two cycles. Both samples were run under steady sunshine in outdoor air temperature ranging between 20-22°C in the morning and 33-35°C in the early afternoon hours. Depending on the ambient conditions, the drying temperature was found in the range of 30 to 50°C. The dried samples had a water activity Aw> 0.9, due to which the storage is at -18°C. The duration of the drying process of prunes was inconstant and lasted from 2 to 3 days, depending on the final moisture content of the product and the external temperature, humidity, and intensity of solar radiation. The obtained two products intermediate moisture prunes, in addition to direct human consumption could be used as a base for incorporation into other products. Prunes with intermediate moisture content 40% could be consumed directly at ambient temperature or after freezing and tempering at -6 to -5ºC. Based on the established parameters we are to design and produce an improved solar dryer model that allows better utilization of heat and shortening the process duration.

  17. Modelling of Specific Moisture Extraction Rate and Leakage Ratio in a Condensing Tumble Dryer

    OpenAIRE

    Stawreberg, Lena; Nilsson, Lars

    2010-01-01

    Abstract The use of tumble dryers in households is becoming more common. Tumble dryers, however, consume large amounts of electric energy. A statistical model over the tumble dryer is created from a design of experiments. The model will be used to find the best settings for the power supply to the heater, the internal airflow and the external airflow in order to reach a high specific moisture extraction rate (SMER) and a low leakage ratio of water vapour. The aim also involves expl...

  18. Hand dryer noise in public restrooms exceeds 80 dBA at 10 ft (3 m).

    Science.gov (United States)

    Berkowitz, Shari Salzhauer

    2015-01-01

    High airflow hand dryers are found in many public restrooms today. These dryers offer quick and clean hand drying, and are seen as being an environment-friendly alternative to paper towels. However, many new hand dryers are loud, exposing individuals using the facilities as well as those employees who clean the facilities to potentially dangerous noise. Prolonged exposure to high levels of occupational noise can cause damage to hair cells in the cochlea, resulting in varying degrees of noise-induced hearing loss. This study examined the intensity (in dBA) of the noise produced by the air dryers in campus restrooms. Hand dryer peak and average noise was measured with a sound level meter at 2.5 ft, 5 ft, and 10 ft from the dryer. Noise measurements did not decrease as predicted by the inverse-square law, probably because of the reverberative surfaces found in the restrooms. The small sample of hand dryers tested was mostly found to be producing more noise than the manufacturer claimed they would; indeed, none of the dryers would be safe for an 8-h workday exposure. While hand dryers do reduce paper trash, they pose as a different sort of hazard to our environment and population.

  19. Hand dryer noise in public restrooms exceeds 80 dBA at 10 ft (3 m

    Directory of Open Access Journals (Sweden)

    Shari Salzhauer Berkowitz

    2015-01-01

    Full Text Available High airflow hand dryers are found in many public restrooms today. These dryers offer quick and clean hand drying, and are seen as being an environment-friendly alternative to paper towels. However, many new hand dryers are loud, exposing individuals using the facilities as well as those employees who clean the facilities to potentially dangerous noise. Prolonged exposure to high levels of occupational noise can cause damage to hair cells in the cochlea, resulting in varying degrees of noise-induced hearing loss. This study examined the intensity (in dBA of the noise produced by the air dryers in campus restrooms. Hand dryer peak and average noise was measured with a sound level meter at 2.5 ft, 5 ft, and 10 ft from the dryer. Noise measurements did not decrease as predicted by the inverse-square law, probably because of the reverberative surfaces found in the restrooms. The small sample of hand dryers tested was mostly found to be producing more noise than the manufacturer claimed they would; indeed, none of the dryers would be safe for an 8-h workday exposure. While hand dryers do reduce paper trash, they pose as a different sort of hazard to our environment and population.

  20. Design, Construction and Testing of Simple Solar Maize Dryer

    OpenAIRE

    Folaranmi, Joshua

    2008-01-01

    This project reports the design, construction and testing of a simple solar maize dryer. It is design in such a way that solar radiation is not incident directly on the maize, but preheated air warmed during its flow through a low pressure thermosphonic solar energy air heater or collector made up of an insulating material (polystyrene) of size 100mmx50mmx25.4mm, absorber plate (aluminium) sheet painted black of size 100mmx50mm and a cover glass (5mm thickness) measuring 100mmx50mm all arrang...

  1. Estimation of drying parameters in rotary dryers using differential evolution

    Energy Technology Data Exchange (ETDEWEB)

    Lobato, F S; Jr, V Steffen; Barrozo, M A S; Arruda, E B, E-mail: vsteffen@mecanica.ufu.br, E-mail: masbarrozo@ufu.br

    2008-11-01

    Inverse problems arise from the necessity of obtaining parameters of theoretical models to simulate the behavior of the system for different operating conditions. Several heuristics that mimic different phenomena found in nature have been proposed for the solution of this kind of problem. In this work, the Differential Evolution Technique is used for the estimation of drying parameters in realistic rotary dryers, which is formulated as an optimization problem by using experimental data. Test case results demonstrate both the feasibility and the effectiveness of the proposed methodology.

  2. Heat-pump tumble dryers; Waermepumpen-Tumbler

    Energy Technology Data Exchange (ETDEWEB)

    Bluemig, N.; Gatter, R.

    2004-07-01

    Commonly available tumble dryers with air-vented or condenser systems in combination with electrical heating have a high specific energy consumption and never fulfil the requirements for Energy Label Class A (<= 0.55 kWh/kg.). The development of a tumbler with a heat pump system has enabled a reduction of almost 50% in the specific energy consumption. In addition to ecological aspects, this means that a significant reduction in energy costs is achieved as well as a beneficial effect on room climate. Other considerations taken into account in the development of the 6.5 kg tumbler were: (i) Compact modular design; integration of the heat pump in the appliance casing; (ii) Long operating life without clogging-up of the heat exchanger by fluff; (iii) Stable process throughout the drying in ambient temperatures of up to 35 {sup o}C. Process stability in particular presented a tough challenge. The solution came in the form of an additional booster condenser that prevents overheating of the compressor towards the end of the process when only negligible amounts of energy are being carried away as a result of the low residual moisture in the laundry. It proved possible to reduce the specific power consumption to less than 0.4 kWh/kg and the leak rate to less 30 %. Thanks to the compact, modular design, the heat pump could be integrated in a housing which has the same size as a conventional 6.5 kg dryer. Clogging-up of the heat exchanger surfaces with fluff was prevented by a multi-stage cascade filtration system. With this heat pump dryer it has been possible for the very first time to develop to series production and launch an appliance in the up to 6.5 kg category that not only fulfils the requirements of Energy Label Class A but also offers a serious alternative to conventional tumble dryers thanks to its compact design, operating safety and ease of operation. Future development opportunities lie in more cost-effective production of the heat pump module, shortening of

  3. Improving Dryer and Press Efficiencies Through Combustion of Hydrocarbon Emissions

    Energy Technology Data Exchange (ETDEWEB)

    Sujit Banerjee

    2005-10-31

    Emission control devices on dryers and presses have been legislated into the industry, and are now an integral part of the drying system. These devices consume large quantities of natural gas and electricity and down-sizing or eliminating them will provide major energy savings. The principal strategy taken here focuses on developing process changes that should minimize (and in some cases eliminate) the need for controls. A second approach is to develop lower-cost control options. It has been shown in laboratory and full-scale work that Hazardous Air Pollutants (HAPs) emerge mainly at the end of the press cycle for particleboard, and, by extension, to other prod-ucts. Hence, only the air associated with this point of the cycle need be captured and treated. A model for estimating terpene emissions in the various zones of veneer dryers has been developed. This should allow the emissions to be concentrated in some zones and minimized in others, so that some of the air could be directly released without controls. Low-cost catalysts have been developed for controlling HAPs from dryers and presses. Catalysts conventionally used for regenerative catalytic oxidizers can be used at much lower temperatures for treating press emissions. Fluidized wood ash is an especially inexpensive mate-rial for efficiently reducing formaldehyde in dryer emissions. A heat transfer model for estimating pinene emissions from hot-pressing strand for the manufacture of flakeboard has been constructed from first principles and validated. The model shows that most of the emissions originate from the 1-mm layer of wood adjoining the platen surface. Hence, a simple control option is to surface a softwood mat with a layer of hardwood prior to pressing. Fines release a disproportionate large quantity of HAPs, and it has been shown both theo-retically and in full-scale work that particles smaller than 400 µm are principally responsible. Georgia-Pacific is considering green

  4. Kinetics of potato drying using fluidized bed dryer.

    Science.gov (United States)

    Bakal, Sushant Balasaheb; Sharma, Gyanendra Prasad; Sonawane, Somnath P; Verma, Radhachran C

    2012-10-01

    The effect of air temperature and two different shapes (cuboidal and cylindrical) with 3 aspect ratio of each shape on the drying kinetics of potato (Solanum tuberosum) in fluidized bed dryer was investigated. Drying was carried out at 50, 60 and 70°C at 7 m/s air velocity. Drying data were analysed to obtain effective diffusivity of moisture transfer. During drying moisture transfer from potato were described by Fick's diffusion model. Two mathematical models were fitted to experimental data. The Page model gave better fit than simple exponential model. The Arrehnious activation energy value expresses the effect of temperature on diffusivity.

  5. Performance Evaluation Of A Grain Maize Solar Dryer

    Directory of Open Access Journals (Sweden)

    Osondu L. C.

    2015-08-01

    Full Text Available Abstract Drying under direct sunlight is one of the oldest techniques used by mankind to preserve Agriculture based food and non-food products. This paper focused on the use of solar dryer to reduce the moisture content of Agriculture produce such as maize. The experiment performed showed the moisture content of maize reduced from 20 to 13. It was also observed that the temperature increased with time. The assumed maximum temperature of the collector plate in the experiment was 100.

  6. A greenhouse type solar dryer for small-scale dried food industries: Development and dissemination

    Energy Technology Data Exchange (ETDEWEB)

    Janjai, Serm [Solar Energy Research Laboratory, Department of Physics, Faculty of Science, Silpakorn University, Nakhon Pathom 73000 (Thailand)

    2012-07-01

    In this study, a greenhouse type solar dryer for small-scale dried food industries was developed and disseminated. The dryer consists of a parabolic roof structure covered with polycarbonate sheets on a concrete floor. The system is 8.0m in width, 20.0m in length and 3.5m in height, with a loading capacity about 1,000kg of fruits or vegetables. To ensure continuous drying operation, a 100kW-LPG gas burner was incorporated to supply hot air to the dryer during cloudy or rainy days. Nine 15-W DC fans powered by three 50-W PV modules were used to ventilate the dryer. This dryer was installed for a small-scale food industry at Nakhon Pathom in Thailand to produce osmotically dehydrated tomato. To investigate its performance, the dryer was used to dry 3 batches of osmotically dehydrated tomato. Results obtained from these experiments showed that drying air temperatures in the dryer varied from 35 C to 65 C. In addition, the drying time for these products was 2-3 days shorter than that of the natural sun drying and good quality dried products were obtained. A system of differential equations describing heat and moisture transfers during drying of osmotically dehydrated tomato was also developed. The simulated results agreed well with the experimental data. For dissemination purpose, other two units of this type of dryer were constructed and tested at two locations in Thailand and satisfactory results were obtained.

  7. 76 FR 971 - Energy Conservation Program for Consumer Products: Test Procedures for Clothes Dryers and Room...

    Science.gov (United States)

    2011-01-06

    ...) Standard HLD-1-1974, ``AHAM Performance Evaluation Procedure for Household Tumble Type Clothes Dryers... Consumption of Household Tumble Type Clothes Dryers'' December 1975 (AHAM Standard HLD-2EC). The test... test procedure additional language based on provisions from European Standard EN 61121, ``Tumble...

  8. Model-Based Energy Efficiency Optimization of a Low-Temperature Adsorption Dryer

    NARCIS (Netherlands)

    Atuonwu, J.C.; Straten, G. van; Deventer, H.C. van; Boxtel, A.J.B. van

    2011-01-01

    Low-temperature drying is important for heat-sensitive products, but at these temperatures conventional convective dryers have low energy efficiencies. To overcome this challenge, an energy efficiency optimization procedure is applied to a zeolite adsorption dryer subject to product quality. The

  9. 78 FR 8992 - Energy Conservation Program: Test Procedures for Residential Clothes Dryers

    Science.gov (United States)

    2013-02-07

    ... Part 430 RIN 1904-AC63 Energy Conservation Program: Test Procedures for Residential Clothes Dryers... procedures for residential clothes dryers established under the Energy Policy and Conservation Act. The... Background Title III of the Energy Policy and Conservation Act (42 U.S.C. 6291, et seq.; ``EPCA'' or...

  10. Development and Evaluation of Solar Tunnel Dryer for Commercial Fish Drying

    Science.gov (United States)

    Mohod, A. G.; Khandetod, Y. P.; Shrirame, H. Y.

    2014-01-01

    The local practice of drying fish in open sun drying poses problems such as high moisture content, uncontrolled drying and contamination. These problems can be avoided by proper use of improved methods such as the solar tunnel dryer, which results in faster drying of fish. The semi cylindrical walk-in type natural convection solar tunnel dryer, having drying area of 37.5 m2 was developed and evaluated for the drying of fish products in comparison with the conventional method of open sun drying. The experiments were conducted without fish and with fish to evaluate the performance of solar tunnel dryer. The average rise in temperature inside the solar tunnel dryer was found to be 11.24 °C and 18.29 °C over the ambient temperature during no load test in winter and summer respectively. The average 28 % saving in time was observed for selected fish drying using solar tunnel dryer over open sun drying method with average drying efficiency of 19 %. The economics was calculated for drying of prawns ( Parapaeneopsis stylifera) by solar tunnel dryer and open sun drying system on the basis of business as a whole. The economics of the solar tunnel dryer is presented in term of Net present worth, Benefit-Cost Ratio, Payback period, Profitability index and Internal rate of return. The pay back period for solar tunnel dryer was found to be 2.84 years.

  11. 40 CFR 63.2264 - Initial compliance demonstration for a hardwood veneer dryer.

    Science.gov (United States)

    2010-07-01

    ... hardwood veneer dryer. 63.2264 Section 63.2264 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY... CATEGORIES National Emission Standards for Hazardous Air Pollutants: Plywood and Composite Wood Products Initial Compliance Requirements § 63.2264 Initial compliance demonstration for a hardwood veneer dryer....

  12. 40 CFR 63.2265 - Initial compliance demonstration for a softwood veneer dryer.

    Science.gov (United States)

    2010-07-01

    ... softwood veneer dryer. 63.2265 Section 63.2265 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY... CATEGORIES National Emission Standards for Hazardous Air Pollutants: Plywood and Composite Wood Products Initial Compliance Requirements § 63.2265 Initial compliance demonstration for a softwood veneer dryer....

  13. Design of solar thermal dryers for 24-hour food drying processes (abstract)

    Science.gov (United States)

    Solar drying is a ubiquitous method that has been adopted for many years as a food preservation method. Most of the published articles in the literature provide insight on the performance of solar dryers in service but little information on the dryer construction material selection process or mater...

  14. MICROBIOLOGICAL CHARACTERISTICS OF THE AIR BLOWN BY WARM AIR HAND DRYERS

    Directory of Open Access Journals (Sweden)

    Recai OÐUR; Omer Faruk TEKBAS; Osman HANCI; Umut OZCAN

    2005-02-01

    Full Text Available The aim of the study was to determine the microbiological characteristics of air blown from warm air hand dryers, and to compare findings with the microbiological characteristics of indoor air in which the dryer settled. Air samples was taken from different public places (shopping centers, restaurants and hospitals and investigated for total viable counts, coagulase negative Staphylococcus, E. Coli, Staphylococcus aureus and enteric pathogens. There were differences between sampling indoor places for some of the microorganisms, but all of the air samples taken from dryers contained more microorganisms than indoor air, and the differences between hand dryers and indoor air were statistically significant (p<0.05 except for enteric pathogens. As a result it could be said that warm air hand dryers could be microbiological contamination sources in restrooms or the other places that they are used. [TAF Prev Med Bull 2005; 4(1.000: 1-7

  15. Experimental Analysis of Open, Simple and Modified Greenhouse Dryers for Drying Potato Flakes Under Forced Convection

    Directory of Open Access Journals (Sweden)

    Tanuj Kumar Sahu

    2016-07-01

    Full Text Available Drying using burning of fossil fuels and open sun drying are traditional way to dry crops, fruits, vegetables etc. But there are some disadvantages associated with them such as crops are affected by dirt and other impurities. To overcome the problems associated with open sun drying and drying using burning of fossil fuels, solar greenhouse drying is found out to be the best alternative. In present work the performance of simple and modified greenhouse dryer is evaluated and effort is made to increase the drying rate of greenhouse dryer which has been achieved in modified greenhouse dryer with inclined roof. Total weight of potato flakes was reduced by 80.1 % in modified greenhouse dryer in just 5 hours whereas it took 6 hours in simple greenhouse dryer for achieving nearly same values.

  16. Hair Shaft Damage from Heat and Drying Time of Hair Dryer

    Science.gov (United States)

    Lee, Yoonhee; Kim, Youn-Duk; Hyun, Hye-Jin; Pi, Long-quan; Jin, Xinghai

    2011-01-01

    Background Hair dryers are commonly used and can cause hair damage such as roughness, dryness and loss of hair color. It is important to understand the best way to dry hair without causing damage. Objective The study assessed changes in the ultra-structure, morphology, moisture content, and color of hair after repeated shampooing and drying with a hair dryer at a range of temperatures. Methods A standardized drying time was used to completely dry each hair tress, and each tress was treated a total of 30 times. Air flow was set on the hair dryer. The tresses were divided into the following five test groups: (a) no treatment, (b) drying without using a hair dryer (room temperature, 20℃), (c) drying with a hair dryer for 60 seconds at a distance of 15 cm (47℃), (d) drying with a hair dryer for 30 seconds at a distance of 10 cm (61℃), (e) drying with a hair dryer for 15 seconds at a distance of 5 cm (95℃). Scanning and transmission electron microscopy (TEM) and lipid TEM were performed. Water content was analyzed by a halogen moisture analyzer and hair color was measured with a spectrophotometer. Results Hair surfaces tended to become more damaged as the temperature increased. No cortex damage was ever noted, suggesting that the surface of hair might play a role as a barrier to prevent cortex damage. Cell membrane complex was damaged only in the naturally dried group without hair dryer. Moisture content decreased in all treated groups compared to the untreated control group. However, the differences in moisture content among the groups were not statistically significant. Drying under the ambient and 95℃ conditions appeared to change hair color, especially into lightness, after just 10 treatments. Conclusion Although using a hair dryer causes more surface damage than natural drying, using a hair dryer at a distance of 15 cm with continuous motion causes less damage than drying hair naturally. PMID:22148012

  17. Evaluating the parameters of a mobile maize dryer in practice

    Directory of Open Access Journals (Sweden)

    Josef Los

    2013-01-01

    Full Text Available The method of drying maize for grain has been recently employed on a large scale in the Czech Republic not only thanks to new maize hybrids but also thanks to the existence of new models of drying plants. One of the new post-harvest lines is a plant in Lipoltice (mobile dryer installed in 2010, storage base in 2012 where basic operational measurements were made of the energy intensiveness of drying and operating parameters of the maize dryer were evaluated. The process of maize drying had two stages, i.e. pre-drying from the initial average grain humidity of 28.55% to 19.6% in the first stage, and the additional drying from 16.7% to a final storage grain humidity of 13.7%. Mean volumes of natural gas consumed per 1 t% for drying in the first and second stage amounted to 1.275 m3 and 1.56 m3, respectively. The total mean consumption of electric energy per 1 t% was calculated to be 1.372 kWh for the given configuration of the post-harvest line.

  18. Drying characteristics of paddy in an integrated dryer.

    Science.gov (United States)

    Manikantan, M R; Barnwal, P; Goyal, R K

    2014-04-01

    Drying characteristics of paddy (long grain variety PR-118 procured from PAU, Ludhiana) in an integrated dryer using single as well as combined heating source was studied at different air temperatures. The integrated dryer comprises three different air heating sources such as solar, biomass and electrical. Drying of paddy occurred in falling rate period. It was observed that duration of drying of paddy from 22 to 13 % moisture content (w.b.) was 5-9 h depending upon the source of energy used. In order to select a suitable drying curve, six thin layer-drying models (Newton, Page, Modified Page, Henderson and Pabis, Logarithmic and Wang and Singh) were fitted to the experimental moisture ratio data. Among the mathematical models investigated, Wang and Singh model best described the drying behaviour of paddy using solar, biomass and combined heating sources with highest coefficient of determination (r (2)) values and least chi-square, χ (2), mean bias error (MBE) and root mean square error (RMSE) values. However, Page model adequately described the drying behavior of paddy using electrical heating source.

  19. Design, Construction and Testing of Simple Solar Maize Dryer

    Directory of Open Access Journals (Sweden)

    Joshua FOLARANMI

    2008-12-01

    Full Text Available This project reports the design, construction and testing of a simple solar maize dryer. It is design in such a way that solar radiation is not incident directly on the maize, but preheated air warmed during its flow through a low pressure thermosphonic solar energy air heater or collector made up of an insulating material (polystyrene of size 100mmx50mmx25.4mm, absorber plate (aluminium sheet painted black of size 100mmx50mm and a cover glass (5mm thickness measuring 100mmx50mm all arranged in this order contributed to the heating. The test results gave temperature above 45OC in the drying chamber, and the moisture content of 50kg of maize reduced to about 12.5% in three days of 9hours each day of drying.

  20. Heat-pump-assisted dryer: Pt. 2; Experimental study

    Energy Technology Data Exchange (ETDEWEB)

    Pendyala, V.R.; Devotta, S.; Patwardhan, V.S. (National Chemical Lab., Poona (India))

    1990-07-01

    The performance of an experimental heat-pump-assisted dryer under operating conditions of some practical interest was studied. The system was operated using R11 and R12. The approach velocity of air to the evaporator and the superheat of the working fluid at the exit of the evaporator were identified as the critical parameters for optimization. The system was evaluated with respect to coefficient of performance (COP) and specific energy consumption (SEC). The (COP){sub A} and (SEC) values obtained using R11 were 3.5 and 3500 kJ/kg, respectively, and the corresponding values for R12 were 2.5 and 1800 kJ/kg. In spite of the lower (COP){sub A} for R12, the corresponding (SEC) values were better because the system could be operated without any additional electrical heating with R12. (author).

  1. Soybean drying characteristics in microwave rotary dryer with forced convection

    Institute of Scientific and Technical Information of China (English)

    Ruifang WANG; Zhanyong LI; Yanhua LI; Jingsheng YE

    2009-01-01

    A new hybrid drying technique by combining microwave and forced convection drying within a rotary drum, i.e., microwave rotary drying, was developed with the purpose to improve the uniformity of microwave drying. In a laboratory microwave rotary dryer, rewetted soybean was utilized as experimental material to study the effects of drum rotating speed, ventilation flow rate, and specific microwave power on the drying kinetics and cracking ratio of soybean. It was found that, with rotation, the cracking ratio can be lowered but without distinct improvement in the drying rate. Increasing ventilation flow rate and specific microwave power can improve the drying rate, but the cracking ratio also increases as a negative result. The cracking ratio lower than 10% can be attained for ventilation flow rate lower than 2.0 m3·h-1 or specific microwave energy lower than 0.4 kW·kg-1 in the present experiments.

  2. Spray dryer/baghouse system testing - CRADA 92-001. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Pennline, H. W.

    1992-04-28

    A series of seven tests were conducted to evaluate the effectiveness of scrubbing both NO{sub 2} and SO{sub 2} in a spray dryer/baghouse system. The operating conditions specified were a high spray dryer inlet temperature (500{degrees}F), and a high spray dryer outlet temperature (250 to 300 {degrees}F). The data required to adequately evaluate the effectiveness of this technology is enclosed. Discussion of some of the variables as well as an itemized list of the testing information is part of the report.

  3. Press and Dryer Roll Surgaces and Web Transfer Systems for Ultra High Paper Maching Speeds

    Energy Technology Data Exchange (ETDEWEB)

    T. F. Patterson

    2004-03-15

    The objective of the project was to provide fundamental knowledge and diagnostic tools needed to design new technologies that will allow ultra high speed web transfer from press rolls and dryer cylinders.

  4. Energy Efficiency Improvements of Tumble Dryers : -Technical Development, Laundry Habits and Energy Labelling

    OpenAIRE

    Stawreberg, Lena

    2011-01-01

    Tumble dryers are becoming more and more common in ordinary households as a complement to the washing machine. Tumble dryers offer a fast drying cycle independent on weather conditions and require small space. They do, however, considering the large number of units use a large amount of electricity. The main objective in this thesis is to identify possibilities in order to reach a reduced electricity use for domestic tumble-drying of clothes. This involves an investigation of the condensing t...

  5. Diabetes, damp casts, and hair dryers are not a good combination.

    Science.gov (United States)

    Henderson, Bernardine C; Lawson, Derek; Conley, G Reid

    2013-01-01

    Second- and third-degree burns of the toes resulted when a 69-year-old man with Charcot foot and a recent fractured ankle followed the advice of his local podiatrist. The man got his fiberglass cast wet while showering and was told to dry his cast using the low setting on a blow dryer. The following presents a literature review of cast drying, hair dryers, and this unfortunate man's case.

  6. Technical and environmental analysis of biofuel dryers; Teknisk och miljoemaessig analys av biobraensletorkar

    Energy Technology Data Exchange (ETDEWEB)

    Muenter, M.; Hagman, U.; Harnevie, H.; Johansen, H.; Kristensson, I.; Westermark, M.; Viberg, T. [Vattenfall Energimarknad, Stockholm (Sweden)

    1999-03-01

    A study regarding technology and environmental impact of the drying process of biofuels has been conducted. In the study two different types of dryers are analyzed. The result from the study shows that emissions of primarily hydrocarbons is high from the direct technic. The emission can be decreased considerably by improving the burner of the dryer. For the indirect technic the evaporated water give rise to problems in the sewage treatment plant. Studies show that biological treatment will result in an acceptable condensate.

  7. Designing, constructing and evaluating a dynamic prototype dryer for obtaining rolled dehydrated fruit pulp

    OpenAIRE

    Vanegas Mahecha, Pedro; Parra Coronado, Alfonso

    2011-01-01

    This paper describes how a functional prototype for a dynamic dryer was designed, along with its basic parts: drying tunnel, mechanical transport system for material inside the equipment and selecting and designing a system for supplying hot air. A simple transport mechanism was implemented which allowed combining two flow dispositions: parallel and countercurrent flow. Mango (Mangifera indica L) pulp was dehydrated using three dryer air temperatures (50°C, 60°C and 70°C) and three drying air...

  8. Further development of a mixed-dryer for wood biomass; Sekoituskuivurin jatkokehitys

    Energy Technology Data Exchange (ETDEWEB)

    Heinonen, O. [Imatran Voima Oy, Vantaa (Finland). Research and Development; Parvio, E. [IVO International Oy, Vantaa (Finland)

    1995-12-31

    Imatran Voima Oy and IVO International Ltd are developing a new, advanced drying method for high moisture content fuels such as peat, biomass, and brown coal. The drying technology is based on using the heat of the fluidized bed directly for drying. The drying takes place at steam atmosphere, which makes it possible to recover the latent heat of evaporation back to process at high temperature level. This improves the thermal efficiency of the plant considerably. The technology is called bed mixing dryer. The pilot plant of the bed mixing dryer was built to IVO`s Kuusamo peat and wood fired power plant that was commissioned in the beginning of 1994. The Kuusamo district heating power plant has a fuel input of 27 MW that gives a power output of 6 MWe and district heat output of 17.5/21.2 MWth. As fuels are used peat, saw dust and wood wastes. The boiler is a bubbling fluidized bed boiler and the steam cycle is a conventional back pressure steam process. The unique feature in the plant is the new dryer that increases the overall thermal efficiency of the plant 10 to 15 units of percentage. In this project the operation and behaviour of the bed mixing dryer has been examined. Various components of the dryer were developed by the cold model tests carried out at IVO`s laboratory in Helsinki. Testing with the Kuusamo bed mixing dryer consisted of about 390 hours of drying tests with peat, bark and saw dust. The dryer operated well, and the drying was effective. The measured final moisture content varied from 7 to 19 % depending on the fuel particle size and the temperature level of the dryer

  9. A greenhouse type solar dryer for small-scale dried food industries: Development and dissemination

    Directory of Open Access Journals (Sweden)

    Serm Janjai

    2012-01-01

    Full Text Available In this study, a greenhouse type solar dryer for small-scale dried food industries was developed and disseminated. The dryer consists of a parabolic roof structure covered with polycarbonate sheets on a concrete floor. The system is 8.0m in width, 20.0m in length and 3.5m in height, with a loading capacity about 1,000kg of fruits or vegetables. To ensure continuous drying operation, a 100kW-LPG gas burner was incorporated to supply hot air to the dryer during cloudy or rainy days. Nine 15-W DC fans powered by three 50-W PV modules were used to ventilate the dryer. This dryer was installed for a small-scale food industry at Nakhon Pathom in Thailand to produce osmotically dehydrated tomato. To investigate its performance, the dryer was used to dry 3 batches of osmotically dehydrated tomato. Results obtained from these experiments showed that drying air temperatures in the dryer varied from 35°C to 65°C. In addition, the drying time for these products was 2-3 days shorter than that of the natural sun drying and good quality dried products were obtained. A system of differential equations describing heat and moisture transfers during drying of osmotically dehydrated tomato was also developed. The simulated results agreed well with the experimental data. For dissemination purpose, other two units of this type of dryer were constructed and tested at two locations in Thailand and satisfactory results were obtained.

  10. Preparation of powdered egg yolk using a mini spray dryer Estudo da obtenção de ovo em pó usando mini spray dryer

    Directory of Open Access Journals (Sweden)

    Rene Maria Ignário

    2007-12-01

    Full Text Available Powdered egg is used as an emulsifying agent in emulsion formulations. It is an excellent source of high quality protein, of which the yolk contains 44% and the egg white 56%. Spray drying is a widely applied method for drying aqueous or organic solutions and emulsions in the chemical and food industries. Spray drying can be used to preserve food or simply as a rapid drying method. The objective of this work was to study the viability of obtaining powdered egg yolk powder using a Büchi B-190 Mini Spray Dryer. The egg yolk protein was evaluated by the semi-micro Kjeldahl method. It was concluded that the use of the Büchi B-190 Mini Spray Dryer to produce powdered egg yolk is perfectly feasible.Ovo em pó pode ser usado como agente emulsificante. É uma excelente fonte de alta qualidade protéica contendo 44% na gema e 56% na clara. Spray dryer é um método amplamente usado para secar soluções aquosas ou orgânicas, emulsões, na indústria química e alimentícia. Spray dryer pode ser usado para preservar alimentos ou simplesmente como um método rápido de secagem. O objetivo deste trabalho foi estudar a viabilidade de obtenção de gema de ovo em pó utilizando o Büchi B-190 Mini Spray Dryer. O teor de proteínas da gema de ovo foi analisado pelo método semi-micro Kjeldahl. Concluiu-se o uso do Büchi B-190 Mini Spray Dryer para a obtenção de gema de ovo em pó é perfeitamente viável.

  11. Study on effectiveness of continuous solar dryer integrated with desiccant thermal storage for drying cocoa beans

    Directory of Open Access Journals (Sweden)

    Sari Farah Dina

    2015-03-01

    Full Text Available The main objective is to assess effectiveness of continuous solar dryer integrated with desiccant thermal storage for drying cocoa beans. Two type of desiccants were tested, molecular sieve 13× (Na86 [(AlO286·(SiO2106]·264H2O as an adsorbent type and CaCl2 as an absorbent type. The results revealed that during sunshine hours, the maximum temperature within the drying chamber varied from 40 °C to 54 °C. In average, it was 9–12 °C higher than ambient temperature. These temperatures are very suitable for drying cocoa beans. During off-sunshine hours, humidity of air inside the drying chamber was lower than ambient because of the desiccant thermal storage. Drying times for intermittent directs sun drying, solar dryer integrated with adsorbent, and solar dryer integrated with absorbent were 55 h, 41 h, and 30 h, respectively. Specific energy consumptions for direct sun drying, solar dryer integrated with adsorbent, and solar dryer integrated with absorber were 60.4 MJ/kg moist, 18.94 MJ/kg moist, and 13.29 MJ/kg moist, respectively. The main conclusion can be drawn here is that a solar dryer integrated with desiccant thermal storage makes drying using solar energy more effective in term of drying time and specific energy consumption.

  12. Performance study of a heat pump dryer system for speciality crops - Pt. 2: model verification

    Energy Technology Data Exchange (ETDEWEB)

    Adapa, P.K.; Schoenau, G.J.; Sokhansanj, S. [University of Saskatchewan (Canada). College of Engineering

    2002-07-01

    The experimental and predicted performance data of a heat pump dryer system is reported. Chopped alfalfa was dried in a cabinet dryer in batches and also by emulating continuous bed drying using two heat pumps operating in parallel. Results showed that alfalfa was dried from an initial moisture content of 70% (wb) to a final moisture content of 10% (wb). The batch drying took about 4.5 h while continuous bed drying took 4 h to dry the same amount of material. The average air velocity inside the dryer was 0.36 m s{sup -1}. Low temperatures (30-45{sup o}C) for safe drying of specialty crops were achieved experimentally. The heat pump drying system used in this study was about 50% more efficient in recovering the latent heat from the dryer exhaust compared to the conventional dryers. Specific moisture extraction rate (SMER) was maximum when relative humidity stayed above 40%. The dryer was shown to be capable of SMER of between 0.5 and 1.02 kg kW{sup -1} h{sup -1}. It was concluded that continuous bed drying is potentially a better option than batch drying because high process air humidity ratios at the entrance of the evaporator and constant moisture extraction rate and specific moisture extraction rate values can be maintained. An uncertainty analysis confirmed the accuracy of the model. (author)

  13. 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...

  14. Performance study of a heat pump dryer system for speciality crops - Pt. 1: development of a simulation model

    Energy Technology Data Exchange (ETDEWEB)

    Adapa, P.K.; Schoenau, G.J.; Sokhansanj, S. [University of Saskatchewan (Canada). College of Engineering

    2002-07-01

    This research is concerned with the technology of heat pump assisted drying of specialty crops. A simplified procedure for modelling the performance of a low temperature heat pump dryer was developed. The system modelled consists of a vapour compression heat pump coupled to a continuous cross flow bed dryer. The model takes into account the detailed heat and mass transfer phenomena taking place in the heat pump and dryer circuits. (author)

  15. Feasibility study on pliant media drying using fluidized bed dryer

    Science.gov (United States)

    Zakaria, J. H.; Zaid, M. H. H. M.; Batcha, M. F. M.; Asmuin, N.

    2015-09-01

    The usage of pliant media for blasting in surface preparation has gained substantial interest in various industries, particularly oil and gas. Being a clean technology, this relatively new method of surface preparation has become an alternative to conventional abrasive blasting technique which lowers fugitive emissions from blasting process and hence lowering risk to workers in the industry. Despite proven to be effective and cost efficient, the usage of pliant media in tropical climate poses a new challenge due to the torrential rain in the monsoon season. During rainy and wet conditions, the pliant media was literally soaked and the recovery rate of the pliant media for a continuous blasting becomes retarded. A viable technique for drying of this pliant media has then become imperative. The present study proposes to dry water laden pliant media in a Swirling Fluidized Bed Dryer (SFBD). In this preliminary study, three bed loadings of 1.7, 2.0 and 2.3 kg of pliant media was dried in the SfBd at 80°C, 90°C and 100°C. The experimental works revealed that the SFBD has shown excellent potential to dry the pliant media with a relatively short drying time. The behaviour of moisture ratio and drying rate against time are discussed. The findings conclude that the SFBD is a feasible technique for wet pliant media drying and can be extended for continuous processing system.

  16. Particle size control of detergents in mixed flow spray dryers

    Directory of Open Access Journals (Sweden)

    Mark Jonathan Crosby

    2015-03-01

    Full Text Available Particle size is a key quality parameter of a powder detergent as it determines its performance, the bulk density and the look and feel of the product. Consequently, it is essential that particle size is controlled to ensure the consistency of performance when comparing new formulations. The majority of study reported in the literature relating to particle size control, focuses on the spray produced by the atomisation technique. One approach advocated to achieve particle size control is the manipulation of the ratio of the mass slurry rate and mass flow rate of gas used for atomisation. Within this study, ratio control was compared with an automatic cascade loop approach using online measurements of the powder particle size on a small-scale pilot plant. It was concluded that cascade control of the mean particle size, based on manipulating the mass flow rate of gas, resulted in tighter, more responsive control. The effect of a ratio change varied with different formulations and different slurry rates. Furthermore, changes in slurry rate caused complications, as the impact on particle size growth in the dryer is non-linear and difficult to predict. The cascade loop enables further study into the effect of particle size on detergent performance.

  17. DESIGN AND THERMAL PERFORMANCE OF THE SOLAR BIOMASS HYBRID DRYER FOR CASHEW DRYING

    Directory of Open Access Journals (Sweden)

    Saravanan Dhanuskodi

    2014-12-01

    Full Text Available Drying of Cashew nut to remove testa is one of the most energy-intensive processes of cashew nut process industry. For this reason a hybrid dryer consisting of a solar flat plate collector, a biomass heater and a drying chamber is designed and fabricated. 40 kg of Cashew nut with initial moisture of 9 % is used in the experiment. The performance test of the dryer is carried out in two modes of operation: hybrid-forced convection and hybrid-natural convection. Drying time and drying efficiency during these two modes of operation are estimated and compared with the sun drying. The system is capable of attaining drying temperature between 50º and 70ºC. In the hybrid forced drying, the required moisture content of 3% is achieved within 7 hours and the average system efficiency is estimated as 5.08%. In the hybrid natural drying, the required moisture content is obtained in 9 hours and the average system efficiency is 3.17%. The fuel consumption during the drying process is 0.5 kg/hr and 0.75 kg/hr for forced mode and natural mode, respectively. The drying process in the hybrid forced mode of operation is twice faster than the sun drying. The dryer can be operated in any climatic conditions: as a solar dryer on normal sunny days, as a biomass dryer at night time and as a hybrid dryer on cloudy days. Based on the experimental study, it is concluded that the developed hybrid dryer is suitable for small scale cashew nut farmers in rural areas of developing countries.

  18. Assessment of differences between products obtained in conventional and vacuum spray dryer

    Directory of Open Access Journals (Sweden)

    Fernanda de Melo RAMOS

    Full Text Available Abstract In this work, an experimental unit of a vacuum spray dryer was built. This prototype attempted to combine the advantages of freeze-drying (drying at low temperatures due to vacuum and spray drying (increase of surface area aiming the improvement of heat transfer efficiency. Maltodextrin solutions were dried in the vacuum operated equipment and in conventional spray dryer. The vacuum spray dryer system allowed obtaining powder at low temperatures due to the lowering of pressure conditions (2-5 kPa inside the drying chamber. The products obtained in the two systems were characterized and compared for particle size distribution, moisture content, water activity, bulk density and solubility in water. The processes yields were also evaluated and compared. The vacuum spray dryer system allowed the production of larger, more soluble and less dense particles than those obtained in the conventional configuration of the equipment, resulting in drier and, therefore, with lower water activity particles. Thus, the use of the vacuum spray dryer as a drying technique may be an alternative for the production of powder rich in thermosensitive compounds.

  19. Enhancement of Energy Efficiency and Food Product Quality Using Adsorption Dryer with Zeolite

    Directory of Open Access Journals (Sweden)

    Moh Djaeni

    2013-06-01

    Full Text Available Drying is a basic operation in wood, food, pharmaceutical and chemical industry. Currently, several drying methods are often not efficient in terms of energy consumption (energy efficiency of 20-60% and have an impact on product quality degradation due to the introduction of operational temperature upper 80oC. This work discusses the development of adsorption drying with zeolite to improve the energy efficiency as well as product quality. In this process, air as drying medium is dehumidified by zeolite. As a result humidity of air can be reduced up to 0.1 ppm. So, for heat sensitive products, the drying process can be performed in low or medium temperature with high driving force. The study has been conducted in three steps: designing the dryer, performing laboratory scale equipment (tray, spray, and fluidised bed dryers with zeolite, and evaluating the dryer performance based on energy efficiency and product quality. Results showed that the energy efficiency of drying process is 15-20% higher than that of conventional dryer. In additon, the dryer can speed up drying time as well as retaining product quality.

  20. Review on advanced of solar assisted chemical heat pump dryer for agriculture produce

    Energy Technology Data Exchange (ETDEWEB)

    Fadhel, M.I. [Solar Energy Research Institute, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor (Malaysia); Faculty of Engineering and Technology, Multimedia University, Jalan Ayer Keroh Lama, 75450 Melaka (Malaysia); Sopian, K.; Daud, W.R.W.; Alghoul, M.A. [Solar Energy Research Institute, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor (Malaysia)

    2011-02-15

    Over the past three decades there has been nearly exponential growth in drying R and D on a global scale. Improving of the drying operation to save energy, improve product quality as well as reduce environmental effect remained as the main objectives of any development of drying system. A solar assisted chemical heat pump dryer is a new solar drying system, which have contributed to better cost-effectiveness and better quality dried products as well as saving energy. A solar collector is adapted to provide thermal energy in a reactor so a chemical reaction can take place. This reduces the dependency of the drying technology on fossil energy for heating. In this paper a review on advanced of solar assisted chemical heat pump dryer is presented (the system model and the results from experimental studies on the system performance are discussed). The review of heat pump dryers and solar assisted heat pump dryer is presented. Description of chemical heat pump types and the overview of chemical heat pump dryer are discussed. The combination of chemical heat pump and solar technology gives extra efficiency in utilizing energy. (author)

  1. Performance Analysis of a Solar Dryer Equipped with a Recycling Air System and Desiccant Chamber

    Directory of Open Access Journals (Sweden)

    M.H Aghkhani

    2013-09-01

    Full Text Available Drying is a high energy consuming process. Solar drying is one of the most popular methods for dehydration of agricultural products. In the present study, the performance of a forced convection solar dryer equipped with recycling air system and desiccant chamber was investigated. The solar dryer is comprised of solar collector, drying chamber, silica jell desiccant chamber, air ducts, fan and measuring and controlling system. Drying rate and energy consumption in three levels of air temperature (40, 45 and 50 oC and two modes of drying (with recycling air and no-recycling with open duct system were measured and compared. The results showed that increasing the drying air temperature decreased the drying time and increased the energy consumption in the mode of non-recycling air system. The dryer efficiency and drying rate were better in the mode of recycling air system than open duct system. The highest dryer efficiency was obtained from drying air temperature of 50 oC and the mode of recycling air system. In general, the efficiency of solar collector and the highest efficiency of the dryer were 0.34 and 0.41, respectively.

  2. Droplet size measurements for spray dryer scale-up.

    Science.gov (United States)

    Thybo, Pia; Hovgaard, Lars; Andersen, Sune Klint; Lindeløv, Jesper Saederup

    2008-01-01

    This study was dedicated to facilitate scale-up in spray drying from an atomization standpoint. The purpose was to investigate differences in operating conditions between a pilot and a production scale nozzle. The intension was to identify the operating ranges in which the two nozzles produced similar droplet size distributions. Furthermore, method optimization and validation were also covered. Externally mixing two-fluid nozzles of similar designs were used in this study. Both nozzles are typically used in commercially available spray dryers, and they have been characterized with respect to droplet size distributions as a function of liquid type, liquid flow rate, atomization gas flow rate, liquid orifice diameter, and atomization gas orifice diameter. All droplet size measurements were carried out by using the Malvern Spraytec with nozzle operating conditions corresponding to typical settings for spray drying. This gave droplets with Sauter Mean Diameters less than 40 microm and typically 5-20 microm. A model previously proposed by Mansour and Chigier was used to correlate the droplet size to the operating parameters. It was possible to make a correlation for water incorporating the droplet sizes for both the pilot scale and the production scale nozzle. However, a single correlation was not able to account properly for the physical properties of the liquid to be atomized. Therefore, the droplet size distributions of ethanol could not be adequately predicted on the basis of the water data. This study has shown that it was possible to scale up from a pilot to production scale nozzle in a systematic fashion. However, a prerequisite was that the nozzles were geometrically similar. When externally mixing two-fluid nozzles are used as atomizers, the results obtained from this study could be a useful guideline for selecting appropriate operating conditions when scaling up the spray-drying process.

  3. A Planning Experimental Investigation on Tobacco Leaves Dryer Using Paddy Husk and Coal

    Directory of Open Access Journals (Sweden)

    Huy Bich Nguyen

    2014-01-01

    Full Text Available In Viet Nam, the drying technology and techniques for tobacco leaves is one of the most difficulties and plays as key point to get high economic efficiency in tobacco production. To drying for tobacco leaves of 3,500 hectare, for example in Gia Lai province, there needs about 3000 dryers and there is more than 100,000 cubic meter of wood have been burned for drying which equivalent to more than 300 hectare of forest is deforested annually. A designing and manufacturing study for new tobacco dryer to replace the wood fuel by paddy-husk or coal-wood has been implemented. The results indicate that the new dryer using rice-husk or coal can be replaced for the actual drying system used fire wood with the high quality of tobacco leaves and high efficiency. The planning experimental investigation has found the function of the rate of energy consumption and the quality of drying products successful

  4. Injuries sustained by children inside clothes dryers: a report of a fatality and review of the literature.

    Science.gov (United States)

    Saunders, Sarah; Coombes, Anthony; Rutty, Guy

    2012-05-01

    We report a case of a 4-year-old child found dead at his home inside a domestic clothes (tumble) dryer. The child had been reported missing in the morning by his mother and found a short time later inside the dryer with the door shut. The child was pronounced dead at the scene. A pre-autopsy computed tomography scan identified findings associated with aggressive resuscitation attempts. Post-mortem examination showed generalised blunt trauma to his head and limbs, a thin film subdural haemorrhage and burns from contact with hot components and hot air whilst being trapped alive inside the active dryer. A forensic examination of the dryer revealed that it was possible for the child to become trapped in the dryer by his own action and that the dryer could operate for sufficient time to allow for the causation of the injuries to the child. A review of the medical literature and media reports of deaths related to clothes dryer, injuries sustained to survivors and use of dryers as a body disposal site is presented.

  5. 10 CFR Appendix D to Subpart B of... - Uniform Test Method for Measuring the Energy Consumption of Clothes Dryers

    Science.gov (United States)

    2010-01-01

    ... Tumble Type Clothes Dryers”, June 1974, and designated as HLD-1. 1.8“HLD-2EC” means the test standard... of Clothes Dryers D Appendix D to Subpart B of Part 430 Energy DEPARTMENT OF ENERGY ENERGY... Dryers 1. Definitions 1.1“AHAM” means the Association of Home Appliance Manufacturers. 1.2“Bone...

  6. Performance of a Forced-Convection Greenhouse Dryer for Fish Drying

    Directory of Open Access Journals (Sweden)

    Martunis Martunis

    2013-04-01

    Full Text Available ABSTRACT. This research present experimental performance of a forced convection greenhouse dryer for drying of fish. The greenhouse dryer was installed at Aceh province, Indonesia. It has a concrete floor with the area of 6×4 m2. The roof of dryer is built in semi-cylindrical shape and covered with transparent polycarbonate sheets. Two axial flow fans powered by a 50-watt solar cell module was used to generate forced convection for ventilating the dryer.To investigate its performance, the dryer was used to dry two batches of fish. The Results showed that to dry 50 kg fish with initial moisture 68 % required 11 hours. Incontrast, to dry the same amount of fish using sun drying take a time about 2 days. The air temperature inside greenhouse dryer at noon in the clear day was 45-55°C. Kinerja Pengering Rumah Kaca Dengan Metode Konveksi Paksa Untuk Pengeringan Ikan ABSTRAK. Penelitian ini memperlihatkan hasil percobaan terhadap kinerja pengering rumah kaca dengan metode konveksi udara secara paksa pada pengeringan ikan. Penelitian pengering rumah kaca ini dilakukan di Propinsi Aceh, Indonesia. Pengering ini berlantaikan beton dengan luas sebesar 6x4 m2. .Atapnya dibuat berbentuk semi-selinder dan ditutup dengan lembaran plastik transparan berbahan polikarbonat. Dua buah kipas dengan aliran udara secara aksial dipasang dengan sumber daya berasal dari panel surya sebesar 50 Watt dan dipakai untuk menghasilkan konveksi udara paksa pada ventilasi pengering. Untuk menginvestigasi kinerja rumah kaca ini, pengering ini digunakan untuk mengeringkan dua tumpukan ikan. Hasilnya menunjukkan bahwa untuk mengeringkan sebanyak 50 kg ikan dengan kadar air awalnya sebesar 68% membutuhkan waktu selama 11 jam. Sebaliknya, dengan menggunakan sinar matahari secara langsung, untuk mengeringkan ikan dengan jumlah yang sama, maka waktu yang dibutuhkan lebih lama yaitu sekitar 2 hari. Suhu udara di dalam rumah pengering tepat pada siang hari yang cerah berkisar antara 45

  7. Performance of solar dryer chamber used for convective drying of sponge-cotton

    Directory of Open Access Journals (Sweden)

    Aissa Walid

    2014-01-01

    Full Text Available Solar dryer chamber is designed and operated for five days of July 2008. Drying experiments are conducted for sponge-cotton; as a reference drying material in the ranges between 35.0 to 49.5°C of ambient air temperature, 35.2 to 69.8 °C drying air temperature, 30 to 1258 W/m2 solar radiation and 0.016 to 0.08 kg/s drying air flow rate. For each experiment, the mass flow rate of the air remained constant throughout the day. The variation of moisture ratio, drying rate, overall dryer efficiency, and temperature distribution along the dryer chamber for various drying air temperatures and air flow rates are discussed. The results indicated that drying air temperature is the main factor in controlling the drying process and that air mass flow rate has remarkable influence on overall drying performance. For the period of operation, the dryer attained an average temperature of 53.68°C with a standard deviation of 8.49°C within a 12-h period from 7:00 h to 19:00 h. The results of this study indicated that the present drying system has overall efficiency between 1.85 and 18.6 % during drying experiments. Empirical correlations of temperature lapse and moisture ratio in the dryer chamber are found to satisfactorily describe the drying curves of sponge-cotton material which may form the basis for the development of solar dryer design charts.

  8. Modelling and experimentation for the fabric-drying process in domestic dryers

    Energy Technology Data Exchange (ETDEWEB)

    Yadav, V.; Moon, C.G. [Department of Mechanical Engineering, The University of Auckland, Auckland 1142 (New Zealand)

    2008-05-15

    Theoretical analysis of the physical drying process occurring inside the household electric tumbler cloth-dryer is performed to determine various thermo-physical parameters affecting the energy consumption and for the development of a simulation model. Experiments are conducted on a test set-up based on a compact tumble-dryer to measure the values of parameters necessary for evaluating the performance. Three widely-accepted economy standards are considered for comparison of simulation and experimental results. Simulation results are in fair agreement with experimental data. An empirical correlation for the specific moisture-extraction rate (SMER) is developed to translate energy consumption information from one standard to the other. (author)

  9. An industrial batch dryer simulation tool based on the concept of the characteristic drying curve

    DEFF Research Database (Denmark)

    Kærn, Martin Ryhl; Elmegaard, Brian; Schneider, P.

    2013-01-01

    In this study an industrial batch dryer simulation tool is presented. The numerical model behind the scene is developed using the simulation software Engineering Equation Solver (EES) and compared to measurements from a batch dryer facility in Denmark producing insulation boards. In the constant...... content in the material to be invariant in the airflow direction. In the falling-rate period, the concept of the Characteristic Drying Curve (CDC) is used as proposed by Langrish et al. (1991), but modified to account for a possible end-drying rate. Using the CDC both hygroscopic and non...

  10. Loading and unloading of freeze-dryers: airborne contamination risks for aseptically manufactured sterile drug products.

    Science.gov (United States)

    Ljungqvist, Bengt; Reinmüller, Berit

    2007-01-01

    In pharmaceutical manufacturing, freeze-drying processes can be adversely affected by temperature differences relative to the surrounding air. Loading and unloading of freeze-dryers are performed either without or with temperature differences between the cleanroom and the chamber of the freeze-dryer. This operation can cause a flow of room air through the opening, creating a contamination risk, especially when manual handling of material is performed in this area. To minimize this risk, a high-efficiency particulate air (HEPA) filter unit should be installed above the opening to provide clean air and protect the opening. Here the theoretical relationships are discussed and design criteria are presented.

  11. Design, Development and Performance Evaluation of a Small Scale Solar Assisted Paddy Dryer for on Farm Processing

    Directory of Open Access Journals (Sweden)

    Sidrah Ashfaq

    2016-04-01

    Full Text Available With the continued escalation in population growth and the expansion of international food trade and demand of high quality product for food security at low cost has created considerable interest in the development of new post-harvest technologies. This is particularly important for developing countries where post-harvest losses of cereals are between 10-20% and of fruits and vegetables as high as 20- 100% A new solar assisted paddy dryer with central air distribution model (along the length of drying chamber has been developed. Due to this distinct feature of the dryer high drying rate was achieved during the drying processes .Other components of the dryer are perforated drying chamber, blower and flat plat solar air collector. Dryer was evaluated using 100kg of freshly harvested paddy at 23.78% moisture content (wb. Performance evaluation results showed that the mean drying rate of the solar assisted paddy dryer was 0.87kg/hr per for every 100kg, whereas 0.46kg/hr was the sun drying rate comparatively. The faster drying rate of the dryer reveals its suability to dry the paddy for its safe storage moisture content rapidly. By using the solar assisted paddy dryer, approximately 50% saving in time was also achieved as compared with the traditional sun drying method. Solar assisted paddy dryer took 10hr for drying the 100kg paddy up to 14%, while sun drying method dried paddy up to 13.89% in 19 hours. Cost analysis also showed that, by using solar assisted paddy dryer we candry good quality paddy at low cost as compared with the open sun drying method. For development of agriculture in the rural areas, commercial size of the solar assisted paddy dryer can be amplified and produced at community level.

  12. Processamento de achocolatado de cupuaçu por spray-dryer Cupuassu chocolate drink powder processed by spray-dryer

    Directory of Open Access Journals (Sweden)

    Suzana Caetano da Silva Lannes

    2003-03-01

    Full Text Available O achocolatado de cupuaçu é uma mistura do pó de cupuaçu, açúcar, aroma e outros ingredientes constantes da formulação. Este produto formulado foi processado por spray-dryer, gerando um produto seco, pulverizado e instantaneizado. O achocolatado acrescido de água (concentrado passa pelo spray-dryer formando glóbulos de pequeno diâmetro que são arrastados por uma corrente de ar quente. A rápida evaporação de líquido permite manter baixa a temperatura do ar na secagem, não afetando o produto. O pó de cupuaçu não dispersa prontamente em água devido ao seu conteúdo de óleo. Conseqüentemente, necessita-se de uma forma desengordurada para se obter instantaneização. A secagem por spray-dryer reúne as melhores condições de rendimento técnico em comparação com outros processos. Obtiveram rendimentos de processo acima de 20% e a instantaneização completa do produto.Cupuassu chocolate drink powder is a mixture of cupuassu powder, sugar, flavour and other ingredients of formulation. The product was processed by spray-dryer, leading a dry, pulverized and instantised product. The chocolate drink powder with water (concentrated pass through spray-dryer forming small diameter globules that are arrested by a hot air stream. The rapid evaporation allows keeping low temperature at drying air, and no affecting the product. The process is a set of better conditions of technique and economical efficiency in comparison to other process. Cupuassu powder does not disperse readily in water owing to its oil content. Consequently, a form of cocoa with the oil removed is needed to produce an acceptably instant drink. The results obtained were satisfactory, due to the complete instantisation of the product after processing.

  13. Cementitious Spray Dryer Ash-Tire Fiber Material for Maximizing Waste Diversion

    Directory of Open Access Journals (Sweden)

    Charles E. Riley

    2011-01-01

    Full Text Available Spray dryer absorber (SDA material, also known as spray dryer ash, is a byproduct of coal combustion and flue gas scrubbing processes that has self-cementing properties similar to those of class C fly ash. SDA material does not usually meet the existing standards for use as a pozzolan in Portland cement concrete due to its characteristically high sulfur content, and thus unlike fly ash, it is rarely put to beneficial use. This paper presents the results of a study with the objective of developing beneficial uses for SDA material in building materials when combined with tire fiber reinforcement originating from a recycling process. Specifically, spray dryer ash was investigated for use as the primary or even the sole binding component in a mortar or concrete. This study differs from previous research in that it focuses on very high contents of spray dryer ash (80 to 100 percent in a hardened product. The overarching objective is to divert products that are normally sent to landfills and provide benefit to society in beneficial applications.

  14. 76 FR 52852 - Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and...

    Science.gov (United States)

    2011-08-24

    ... Part 430 RIN 1904-AA89 Energy Conservation Program: Energy Conservation Standards for Residential....S. Department of Energy (DOE) adopted amended energy conservation standards for residential clothes dryers and room air conditioners. As required by the Energy Policy and Conservation Act (EPCA), DOE...

  15. Modeling and design of a high efficiency hybrid heat pump clothes dryer

    Energy Technology Data Exchange (ETDEWEB)

    TeGrotenhuis, Ward; Butterfield, Andrew; Caldwell, Dustin; Crook, Alexander; Winkelman, Austin

    2017-09-01

    Computational modeling is used to design a hybrid heat pump clothes dryer capable of saving 50% of the energy used by residential clothes dryers with comparable drying times. The model represents the various stages of a drying cycle from warm-up through constant drying rate and falling drying rate phases and finishing with a cooldown phase. The model is fit to data acquired from a U.S. commercial standard vented electric dryer, and when a hybrid heat pump system is added, the energy factor increases from 3.0 lbs/kWh to 5.7-6.0 lbs/kWh, depending on the increase in blower motor power. The hybrid heat pump system is designed from off-the-shelf components and includes a recuperative heat exchanger, an electric element, and an R-134a vapor compression heat pump. Parametric studies of element power and heating element use show a trade-off between energy savings and cycle time. Results show a step-change in energy savings from heat pump dryers currently marketed in the U.S. based on performance represented by Enery Star from standardized DOE testing.

  16. Performance analysis of greenhouse dryer by using insulated north-wall under natural convection mode

    Directory of Open Access Journals (Sweden)

    Prashant Singh Chauhan

    2016-11-01

    Full Text Available A prototype north wall insulated greenhouse dryer has been fabricated and tested in no-load conditions under natural convection mode. Experimentation has been conducted in two different cases. Case-I is when solar collector placed inside the dryer and Case-II is North wall insulated greenhouse dryer without solar collector. Coefficient of performance, heat utilisation factor, convective heat transfer coefficient and coefficient of diffusivity have been evaluated in thermal performance analysis. The difference of the highest convective heat transfer coefficient of both cases is 29.094W/m2°C which is showing the effectiveness of insulated north wall and solar collector. The maximum coefficient of diffusivity (0.0827 was achieved during the third day of experiment in Case-II. The inside room temperature of wall insulated greenhouse dryer for Case-I is 4.11%, 5.08 % and 11.61 % higher than the Case-II during the day 1, day 2 and day 3 respectively. This result is also showing the effectiveness of solar collector and insulated north wall. The highest heat utilisation factor (0.616 is obtained during the second day for Case-I while for Case-II it is 0.769 during the third day of experimentation. Maximum coefficient of performance achieved is 0.892 during the third day of the experiment for Case-I whereas 0.953 is obtained on the first day of experimentation for Case-II.

  17. Spray dryer/ESP testing for utility retrofit applications on high-sulfur coal

    Energy Technology Data Exchange (ETDEWEB)

    Robards, R.F.; Deguzman, J.S.; Runyan, R.A.; Flora, H.B. II

    1986-01-01

    The Tennessee Valley Authority's continuing research and development efforts for evaluating dry flue gas desulfurization (DFGD) at the Shawnee Test Facility have resulted in the testing of a 1- to 2-MW spray dryer electrostatic precipitator (ESP) system. In this program, three test blocks were used to determine the effectiveness of this concept on high-sulfur coal (3.5- to 4.0-percent sulfur on a dry basis) application. The main ESP variables evaluated included 12- and 15-inch plate spacing using a Duratrode discharge electrode as well as spray dryer variables of lime stoichiometry, approach-to-saturation temperature, residence time, and others. The results indicate that DFGD products are easier to collect than fly ash with removal efficiencies of 96.4 to 99.2 percent at low SCA values. SO/sub 2/ removal across the ESP typically ran 10 to 25 percent (spray dryer SO/sub 2/ removal efficiencies can range up to about 65 percent). Thus, a spray dryer appears to be a potential option for SO/sub 2/ control in a utility retrofit application where an ESP currently exists for particulate collection. Data supporting this conclusion are presented. 3 references.

  18. Spray dryer/ESP testing for utility retrofit applications on high-sulfur coal

    Energy Technology Data Exchange (ETDEWEB)

    Robards, R.F.; DeGuzman, J.S.; Runyan, R.A.; Flora, H.B. II

    1986-04-01

    The Tennessee Valley Authority's continuing research and development efforts for evaluating dry flue gas desulfurization (DFGD) at the Shawnee Test Facility have resulted in the testing of a 1- to 2-MW spray dryer electrostatic precipitator (ESP) system. In this program, three test blocks were used to determine the effectiveness of this concept on high-sulfur coal (3.5- to 4.0-percent sulfur on a dry basis) application. The main ESP variables evaluated included 12- and 15-inch plate spacing using a Duratrode discharge electrode as well as spray dryer variables of lime stoichiometry, approach-to-saturation temperature, residence time, and others. The results indicate that DFGD products are easier to collect than fly ash with removal efficiencies of 96.4 to 99.2% at low SCA values. SO/sub 2/ removal across the ESP typically ran 10 to 25% (spray dryer SO/sub 2/ removal efficiences can range up to about 65%). Thus, a spray dryer appears to be a potential option for SO/sub 2/ control in a utility retrofit application where an ESP currently exists for particulate collection. Data supporting this conclusion are presented.

  19. Development of Simple Drying Model for Performance Prediction of Solar Dryer: Theoretical Analysis

    DEFF Research Database (Denmark)

    Singh, Shobhana; Kumar, Subodh

    2012-01-01

    of experimental drying parameters. A laboratory model of mixed-mode solar dryer system is tested with cylindrical potato samples of thickness 5 and 18 mm under simulated indoor conditions. The potato samples were dried at a constant absorbed thermal energy of 750 W/m2 and air mass flow rate of 0.011 kg...

  20. Design of solar thermal dryers for 24-hour food drying processes

    Science.gov (United States)

    Solar drying is a method that has been adopted for many years as a food preservation method. To this date, significant advancements have been made in this field with the adoption of a multitude of solar thermal dryer designs for single-layer and multi-layer drying of fruit and vegetables e.g. cabine...

  1. Improvement of the Rotary Dryers of Wet Pelletized Oil-Furnace Carbon Blacks

    Directory of Open Access Journals (Sweden)

    Zečević, M

    2010-05-01

    Full Text Available Due to the demand for higher production capacity and natural-gas energy savings, improvements were made to the rotary dryers in the drying process of wet pelletized oil-furnace carbon blacks. Since the rotary dryers were originally designed for drying semi-wet pelletized oil-furnace carbon blacks, they did not entirely satisfy optimal conditions for drying wet pelletized oil-furnace carbon blacks. Figure 1 shows the drying principle with key dimensions. The energy for drying the wet pelletized oil-furnace carbon blacks was provided by natural gas combustion in an open-furnace system with an uncontrolled feed of combustion air. Improvements on the rotary dryers were carried out by adjusting the excess oxygen in the gases passing through the butterfly valve on the dryer exhaust stack. By regulating the butterfly valve on the dryer exhaust stack, and applying the prescribed operations for drying wet pelletized oil furnace carbon blacks, the excess oxygen in the tail gases was adjusted in the range of φ = 3.0 % and 5.0 %, depending on the type of oil-furnace carbon blacks. Suggested also is installation of a direct-reverse automatic butterfly valve on the dryer exhaust stack to automatically determine the volume fraction of oxygen in the tail gas, and the volume flow rate of natural gas for combustion. The results the improvements carried out are shown in Tables 3 to 5. Table 2 shows the thermal calculations for the hood of the rotary dryer. Preheating of the process water in the temperature range of 70 °C and 80 °C is also recommended using the net heat from the oil-furnace process for wet pelletization. The results of preheating the process water are shown in Table 1. Depending on the type of oil-furnace carbon black, the aforementioned improvements resulted in natural gas energy savings ranging from 25 % to 35 % in relation to the average natural gas requirement in the drying process, and thus a reduction in carbon emissions of up to 40

  2. Amorphous particle deposition and product quality under different conditions in a spray dryer

    Institute of Scientific and Technical Information of China (English)

    Meng Wai Woo; Wan Ramli Wan Daud; Siti Masrinda Tasirin; Meor Zainal Meor Talib

    2008-01-01

    Deposition of amorphous particles, as a prevalent problem particularly in the spray drying of fruit and vegetable juices, is due to low-molecular weight sugars and is strongly dependent on the condition of the particles upon collision with the dryer wall. This paper investigates the condition of the amorphous particles impacting the wall at different drying conditions with the aim of elucidating the deposition mechanism and physical phenomena in the drying chamber. A model sucrose-maltodextrin solution was used to represent the low-molecular-weight sugar. Particle deposits were collected on sampling plates placed inside the dryer for analyses of moisture content, particle rigidity (using SEM) and size distribution. Moisture content was adopted as a general indicator of stickiness. Product particles collected at the bottom of the experimental dryer were found to have higher moisture than particle deposits on samplers inside the dryer. Moisture content profile in the dryer shows that apart from the atomizer region, where particles are relatively wet, particle deposits at other regions exhibit similar lower moisture content. At the highest temperature adopted in the experiments, particles became rubbery suggesting liquid-bridge formation as the dominant deposition mechanism. Further analysis on particles size distribution reveals a particle segregation mechanism whereby smaller particles follow preferentially to the central air stream while larger particles tend to re-circulate in the chamber, as predicted in past CFD simulation. The findings from this work will form the basis and provide validating data for further modeling of wall deposition of amorphous particles in spray drying using CFD.

  3. PENGARUH PENGERINGAN DENGAN FAR INFRARED DRYER, OVEN VAKUM DAN FREEZE DRYER TERHADAP WARNA, KADAR TOTAL KAROTEN, BETA KAROTEN DAN VITAMIN C PADA DAUM BAYAM (Amaranthus Tricolor L. [Effect of Drying with Far Infrared Dryer, Oven Vacuum, and Freeze Dryer on the Color, Total Carotene, Beta-Carotene, and Vitamin C of Spinach Leaves (Amaranthus Tricolor L.

    Directory of Open Access Journals (Sweden)

    Ridwan Thahir2

    2005-08-01

    Full Text Available Spinach is a well known vegetable as a source of nutrition especially for is carotene. Soinach leaves need to be dried for application in product development of food like biscuit, extruded products and analysis. One the drying method that became popular is drying using infrared wave. The aim of this research was to compare the effect of blanching and drying (far infrared dryer, oven vacuum, and freeze dryer on the color, total carotene, beta-carotene, and vitamin C of spinach leaves. Blanching and drying of increased brightness, a value, and b value. The a value is shows spinach brightness in mix red-green color while b value shows mix blue-yellow. Total carotene of fresh spinach decreased by 10.47% after blanching. Drying with vacuum decreased the total carotene by 39.31% (with blanching and 31.66 (with blanching. Drying with freeze dryer decreased the beta carotene by 4.99% (with blanching and 18.60% (with blanching. Drying with FIR dryer decreased spinach total carotene by 34.90% (with blanching and 24.86% (with blanching. The beta-carotene of fresh spinach with balancing treatment decreased of by 16.53%.drying oven vacuum decreased the beta carotene by 42.80% (wiyh blanching and 18.91% (with blanching. Drying with freeze dyer decreased the beta carotene by 29.03% (with blanching the beta carotene. The decreased of beta-carotene is bigger than total carotene. Vitamin C of fresh spinach decreased by 20.35% after blanching. Drying with oven vacuum decreased of 55.77% (without blanching and 65.42% (with blanching f the vitamin C. drying with freeze dryer decreased the vitamin C by 13.21% (without blanching and 30.67% (with blanching. Meanwhile, the vitamin C of spinach after drying with FIR dyer decreased of 60.53% (without blanching and 70.29% (with blanching.

  4. Performance Investigation of a Chimney-Dependent Solar Crop Dryer for Different Inlet Areas with a Fixed Outlet Area

    OpenAIRE

    J. K. Afriyie; Bart - Plange, A.

    2012-01-01

    The paper describes the performance of a direct-mode solar crop dryer with a solar chimney. Tests were performed for three differently inclined drying-chamber roofs, each with three inlet areas for a given exit area. Cassava was used as the test crop. The results show that the increase in the inlet area for a given exit area can improve the ventilation in the dryer. However, this does not necessarily improve the drying performance of the direct-mode dryer. A wide inlet area for a given exit a...

  5. Prediction of wall deposition behaviour in a pilot-scale spray dryer using deposition correlations for pipe flows

    Institute of Scientific and Technical Information of China (English)

    KOTA K.; LANGRISH T.A.G.

    2007-01-01

    The particle deposition behaviour of skim milk, water and maltodextrin in the conical section of a pilot-scale spray dryer was predicted using simple correlations for particle depositions in pipes. The predicted particle deposition fluxes of these materials were then compared with the measured deposition fluxes. The predicted particle deposition regimes of the spray dryer were expected to be in the diffusional and mixed (diffusional and inertial) regimes, but the experimental results suggested that the particle deposition was mainly in the inertial regime. Therefore, using the pipe correlations for predicting deposition in a pilot-scale spray dryer suggests that they do not sufficiently represent the actual deposition behaviour. This outcome indicates that a further study of particle flow patterns needs to be carried out using numerical simulations (computational fluid dynamics,CFD) in view of the additional geometrical complexity of the spray dryer.

  6. Development of a Mini-Freeze Dryer for Material-Sparing Laboratory Processing with Representative Product Temperature History.

    Science.gov (United States)

    Obeidat, Wasfy M; Sahni, Ekneet; Kessler, William; Pikal, Michael

    2017-09-13

    The goal of the work described in this publication was to evaluate a new, small, material-sparing freeze dryer, denoted as the "mini-freeze dryer or mini-FD", capable of reproducing the product temperature history of larger freeze dryers, thereby facilitating scale-up. The mini-FD wall temperatures can be controlled to mimic loading procedures and dryer process characteristics of larger dryers. The mini-FD is equipped with a tunable diode laser absorption spectroscopy (TDLAS) water vapor mass flow monitor and with other advanced process analytical technology (PAT) sensors. Drying experiments were performed to demonstrate scalability to larger freeze dryers, including the determination of vial heat transfer coefficients, K v . Product temperature histories during K v runs were evaluated and compared with those obtained with a commercial laboratory-scale freeze dryer (LyoStar II) for sucrose and mannitol product formulations. When the mini-FD wall temperature was set at the LyoStar II band temperature (- 20°C) to mimic lab dryer edge vials, edge vial drying in the mini-FD possessed an average K v within 5% of those obtained during drying in the LyoStar II. When the wall temperature of the mini-FD was set equal to the central vial product temperature, edge vials behaved as center vials, possessing a K v value within 5% of those measured in the LyoStar II. During both K v runs and complete product freeze drying runs, the temperature-time profiles for the average edge vials and central vial in the mini-FD agreed well with the average edge and average central vials of the LyoStar II.

  7. Experimental and simulated performance of a PV-ventilated solar greenhouse dryer for drying of peeled longan and banana

    Energy Technology Data Exchange (ETDEWEB)

    Janjai, S.; Lamlert, N.; Intawee, P. [Solar Energy Research Laboratory, Department of Physics, Faculty of Science, Silpakorn University, Nakhon Pathom 73000 (Thailand); Mahayothee, B. [Department of Food Technology, Faculty of Engineering and Industrial Technology, Silpakorn University, Nakhon Pathom 73000 (Thailand); Bala, B.K. [Department of Farm Power and Machinery, Bangladesh Agricultural University, Mymensingh 2202 (Bangladesh); Nagle, M.; Mueller, J. [Institute of Agricultural Engineering, University of Hohenheim, Stuttgart 70593 (Germany)

    2009-09-15

    This paper presents experimental and simulated performance of a PV-ventilated solar greenhouse dryer for drying of peeled longan and banana. The dryer consists of a parabolic roof structure covered with polycarbonate plates on a concrete floor. Three fans powered by a 50-W PV module ventilate the dryer. To investigate the experimental performances of the solar greenhouse dryer for drying of peeled longan and banana, 10 full scale experimental runs were conducted. Of which five experimental runs were conducted for drying of peeled longan and another five experimental runs were conducted for drying of banana. The drying air temperature varied from 31 C to 58 C during drying of peeled longan while it varied from 30 C to 60 C during drying of banana. The drying time of peeled longan in the solar greenhouse dryer was 3 days, whereas 5-6 days are required for natural sun drying under similar conditions. The drying time of banana in the solar greenhouse dryer was 4 days, while it took 5-6 days for natural sun drying under similar conditions. The quality of solar dried products in terms of colour and taste was high-quality dried products. A system of partial differential equations describing heat and moisture transfer during drying of peeled longan and banana in the solar greenhouse dryer was developed and this system of non-linear partial differential equations was solved numerically using the finite difference method. The numerical solution was programmed in Compaq Visual FORTRAN version 6.5. The simulated results reasonably agreed with the experimental data for solar drying of peeled longan and banana. This model can be used to provide the design data and is also essential for optimal design of the dryer. (author)

  8. A flowsheet model of a well-mixed fluidized bed dryer: Applications in controllability assessment and optimization

    Energy Technology Data Exchange (ETDEWEB)

    Langrish, T.A.G.; Harvey, A.C.

    2000-01-01

    A model of a well-mixed fluidized-bed dryer within a process flowsheeting package (SPEEDUP{trademark}) has been developed and applied to a parameter sensitivity study, a steady-state controllability analysis and an optimization study. This approach is more general and would be more easily applied to a complex flowsheet than one which relied on stand-alone dryer modeling packages. The simulation has shown that industrial data may be fitted to the model outputs with sensible values of unknown parameters. For this case study, the parameter sensitivity study has found that the heat loss from the dryer and the critical moisture content of the material have the greatest impact on the dryer operation at the current operating point. An optimization study has demonstrated the dominant effect of the heat loss from the dryer on the current operating cost and the current operating conditions, and substantial cost savings (around 50%) could be achieved with a well-insulated and airtight dryer, for the specific case studied here.

  9. THE EFFECT OF THE THICKNESS OF A PACKED BED ON THE DYNAMIC AND THERMAL BEHAVIOR OF A SOLAR DRYER

    Directory of Open Access Journals (Sweden)

    S KHALDI

    2015-06-01

    Full Text Available Drying food in the sun is a safe, easy and economical way to preserve food, especially fruits. Cabinet dryers are the most popular equipment for fruit drying. Because of intermittent nature of solar energy, storage is required for uninterrupted supply in order to match the needs. The main objective of this study is to assess effectiveness of continuous solar dryer integrated with packed bed as thermal storage with natural airflow for drying figs (Ficuscarica. The cabinet dryer were envisaged theoretically (computational fluid dynamics (CFD. The distribution of the velocity and temperature of air within the solar dryer were presented during one day of August and under the climate conditions of Tlemcen (Algeria.  The effects of presence of a packed bed on the distribution of velocity and temperature of airflow and on the temperature of figs were analyzed. The results show that the solar dryer design, incorporating a packed bed enhances the capabilities and performance of the solar dryer, through increasing time of drying.

  10. Modelling and simulation of processes by smart sensing : a solar dryer for plant material

    Energy Technology Data Exchange (ETDEWEB)

    Correa, E.C.; Diezma, B.; Ruiz-Altisent, M. [LPF-TAGRALIA Univ. Politecnica, CENIM-CSIC, Madrid (Spain)

    2010-07-01

    This paper reported on a study in which as small wood dryer was modelled. Studies have shown that properly designed solar dryers may prove to be energy saving devices for drying processes. The drying rate expressed as -dX/dt=f/X (where X is DB wood moisture content), allows to identify 2 different kinetics, notably for high X values or fibre saturation point (FSP) and for X values under FSP, in which diffusion is the mechanism that governs a decreasing drying rate at this stage. The complex drying rate model developed in this study made it possible the determine the wood and convective mass transfer at the wood-air interface. Validation and application to fruit and plant drying cycles is currently underway. Three different proposed models are used in the software for a smart sensor system, which is based on Sensirion sensors for temperature and relative humidity in the air, and thermocouples for timber temperature.

  11. Temperature and energy consumption for clothing dryer; Temperatura e consumo de energia em secadora de vestuario

    Energy Technology Data Exchange (ETDEWEB)

    Ribeiro, Jefferson Almeida; Magalhaes Filho, Paulo [UNESP, Guaratingueta, SP (Brazil). Faculdade de Engenharia. Dept. de Energia]. E-mail: pfilho@feg.unesp.br

    2000-07-01

    The cloth dehumidification is done by hot air circulation through it in dryers. The air circulation is done by a fan, run by an electrical motor, and the air temperature raise, which goes through the cloths aiming their moisture dragging, is gotten by the heat dissipation from electrical resistance. This work shows the results of an experimental modeling, examining the behavior of several kinds of cloth in a vertical suspense-type dryer, such as: polyester, cotton-spandex, flannel, blue-jeans and viscose rayon. It was analyzed the behavior of the moisture content in these cloths related to controlled-temperature-air flows, determining the needed heat to reach the required drying standards. The drying device fans were tested for the determination of their flow rate and energy consumption, establishing a flow rate versus consumption relationship. Comparative results among the various kinds of cloths are presented. (author)

  12. Pronounced increase in breathing rate in the "hair dryer model" of experimental febrile seizures.

    Science.gov (United States)

    Schuchmann, Sebastian; Tolner, Else A; Marshall, Pepin; Vanhatalo, Sampsa; Kaila, Kai

    2008-05-01

    In a study using a heated chamber for induction of experimental febrile seizures (eFS) in rat pups, ictal activity was shown to be precipitated by a respiratory alkalosis (Schuchmann et al., 2006). In sharp contrast to this, in a recent review Dubé et al., (2007) suggest that the respiratory alkalosis is model specific, and that no increase in respiratory rate is observed in the widely used "hair dryer model" of eFS. The data in the present work, based on well-established techniques for measuring respiratory rates in rat pups, show a pronounced increase in the "hair dryer model" with values that are slightly higher than those recorded in the heated chamber model. Hence, a temperature-evoked increase in respiration is a common feature of these two models of eFS.

  13. Polychlorinated biphenyls removal from contaminated soils using a transportable indirect thermal dryer unit: implications for emissions.

    Science.gov (United States)

    Yang, Bing; Xue, Nandong; Ding, Qiong; Vogt, Rolf David; Zhou, Lingli; Li, Fasheng; Wu, Guanglong; Zhang, Shilei; Zhou, Dandan; Liu, Bo; Yan, Yunzhong

    2014-11-01

    An assessment in China of the application of a transportable indirect thermal dryer unit for the remediation of soils contaminated with polychlorinated biphenyls (PCBs) demonstrated that it is well suited to remove PCBs from soils. A remarkable reduction of total PCBs in soils from 163-770 μg g(-1) to 0.08-0.15 μg g(-1) was achieved. This represented removal efficiencies of greater than 99.9% and an approximate 100% removal of the toxic equivalent of the PCBs. Furthermore, the emissions to the atmosphere from the unit were in compliance with current PCBs regulations. In conclusion, remediation of PCBs-contaminated soils based on a transportable indirect thermal dryer unit appears to be a highly efficient and environmentally sound treatment technology that has huge implications for cleaning thousands of regionally dispersed sites of PCBs contamination in China.

  14. Theoretical Model for Predicting Moisture Ratio during Drying of Spherical Particles in a Rotary Dryer

    Directory of Open Access Journals (Sweden)

    F. T. Ademiluyi

    2013-01-01

    Full Text Available A mathematical model was developed for predicting the drying kinetics of spherical particles in a rotary dryer. Drying experiments were carried out by drying fermented ground cassava particles in a bench scale rotary dryer at inlet air temperatures of 115–230°C, air velocities of 0.83 m/s–1.55 m/s, feed mass of 50–500 g, drum drive speed of 8 rpm, and feed drive speed of 100 rpm to validate the model. The data obtained from the experiments were used to calculate the experimental moisture ratio which compared well with the theoretical moisture ratio calculated from the newly developed Abowei-Ademiluyi model. The comparisons and correlations of the results indicate that validation and performance of the established model are rather reasonable.

  15. Slurry atomizer for a coal-feeder and dryer used to provide coal at gasifier pressure

    Science.gov (United States)

    Loth, John L.; Smith, William C.; Friggens, Gary R.

    1982-01-01

    The present invention is directed to a coal-water slurry atomizer for use a high-pressure dryer employed in a pumping system utilized to feed coal into a pressurized coal gasifier. The slurry atomizer is provided with a venturi, constant area slurry injection conduit, and a plurality of tangentially disposed steam injection ports. Superheated steam is injected into the atomizer through these ports to provide a vortical flow of the steam, which, in turn, shears slurry emerging from the slurry injection conduit. The droplets of slurry are rapidly dispersed in the dryer through the venturi where the water is vaporized from the slurry by the steam prior to deleterious heating of the coal.

  16. Thin layer drying of cassava starch using continuous vibrated fluidized bed dryer

    Science.gov (United States)

    Suherman, Trisnaningtyas, Rona

    2015-12-01

    This paper present the experimental work and thin layer modelling of cassava starch drying in continuous vibrated fluidized bed dryer. The experimental data was used to validate nine thin layer models of drying curve. Cassava starch with 0.21 initial moisture content was dried in different air drying temperature (50°C, 55°C, 60°C, 65°C, 70°C), different weir height in bed (0 and 1 cm), and different solid feed flow (10 and 30 gr.minute-1). The result showed air dryer temperature has a significant effect on drying curve, while the weir height and solid flow rate are slightly. Based on value of R2, χ2, and RMSE, Page Model is the most accurate simulation for thin layer drying model of cassava starch.

  17. Effect of Selected Factors on Drying Process of Tomato in Forced Convection Solar Energy Dryer

    OpenAIRE

    U.S. Muhammed; A.M.I. El-Okene; Isiaka, M

    2012-01-01

    The effect of air velocity, slice thickness and grazing materials in drying process of tomato in forced convection solar energy dryer was evaluated. The result is to serve as an input for solar energy development for drying of vegetable and fruit products in North West Ecological zone of Nigeria. In order to evaluate the effects of the above factors in drying operation, a split-split-plot experimental design was used. Differences among the treatments and their interactions were tested with or...

  18. Design and Fabrication of a Direct Natural Convection Solar Dryer for Tapioca

    OpenAIRE

    Diemuodeke E. OGHENERUONA; Momoh O.L. YUSUF

    2011-01-01

    Based on preliminary investigations under controlled conditions of drying experiments, a direct natural convection solar dryer was designed and fabricated to dry tapioca in the rural area. This paper describes the design considerations followed and presents the results of MS excel computed results of the design parameters. A minimum of 7.56 m2 solar collector area is required to dry a batch of 100 kg tapioca in 20 hours (two days drying period). The initial and final moisture content consider...

  19. Sanitary condition of electrical hand dryers in toilets of shopping centres in Kraków

    Directory of Open Access Journals (Sweden)

    Anna Lenart-Boroń

    2015-06-01

    Full Text Available Introduction. Shopping habits have changed over the past several years and consumers choose shopping centres, where they can spend time and visit restaurants. People usually wash hands before meals, but toilets in shopping centres are visited by hundreds of users every day which makes their cleanliness questionable. Therefore, the aim of this study was to assess the sanitary condition of electrical hand dryers in toilets of the selected shopping centres in Kraków. Material and methods. Air was sampled at the outlet of electrical hand dryers and surface swabs of hand dryers were taken in toilets of five shopping centres. Air sampling was conducted using the MAS-100 impactor. The number of mesophilic bacteria, fungi, actinomycetes, staphylococci and Escherichia coli was determined. The results of air analyses were compared with the limits provided by the Polish Standards on air quality. Results. The number of microorganisms varied between the studied centres. In terms of mesophilic bacteria and fungi the air was unpolluted. The concentration of actinomycetes however significantly exceeded the limits set by the Polish Standards. Numerous Escherichia coli were found both in the air and in swabs in one of the centres. However the number of E. coli and staphylococci did not exceed the minimum infective dose. Conclusions. The studies showed high concentrations of airborne actinomycetes and staphylococci. Also the presence of E. coli in the air and swabs allows the conclusion that legal regulations for concentrations of airborne microorganisms are necessary to make people aware of this problem. However, it was found that using electrical hand dryers does not have impact on human health.

  20. Performance of a Big Scale Green House Type Dryer for Coffee Drying Process

    OpenAIRE

    Sukrisno Widyotomo

    2014-01-01

    Dying is one of important steps in coffee processing to produce good quality. Greenhouse is one of artificial drying alternatives that potential for coffee drying method cause of cleans environmental friendly, renewable energy sources and chippers. Indonesian Coffee and Cocoa Research Institute has developed and testing a big scale greenhouse type dryer for fresh coffee cherries and wet parchment coffee drying process. Greenhouse has 24 m length, 18 m width, also 3 m high of the front side an...

  1. Performance of a convective, infrared and combined infrared- convective heated conveyor-belt dryer.

    Science.gov (United States)

    El-Mesery, Hany S; Mwithiga, Gikuru

    2015-05-01

    A conveyor-belt dryer was developed using a combined infrared and hot air heating system that can be used in the drying of fruits and vegetables. The drying system having two chambers was fitted with infrared radiation heaters and through-flow hot air was provided from a convective heating system. The system was designed to operate under either infrared radiation and cold air (IR-CA) settings of 2000 W/m(2) with forced ambient air at 30 °C and air flow of 0.6 m/s or combined infrared and hot air convection (IR-HA) dryer setting with infrared intensity set at 2000 W/m(2) and hot at 60 °C being blown through the dryer at a velocity of 0.6 m/s or hot air convection (HA) at an air temperature of 60 °C and air flow velocity 0.6 m/s but without infrared heating. Apple slices dried under the different dryer settings were evaluated for quality and energy requirements. It was found that drying of apple (Golden Delicious) slices took place in the falling rate drying period and no constant rate period of drying was observed under any of the test conditions. The IR-HA setting was 57.5 and 39.1 % faster than IR-CA and HA setting, respectively. Specific energy consumption was lower and thermal efficiency was higher for the IR-HA setting when compared to both IR-CA and HA settings. The rehydration ratio, shrinkage and colour properties of apples dried under IR-HA conditions were better than for either IR-CA or HA.

  2. Thermal sludge dryer demonstration: Bird Island Wastewater Treatment Plant, Buffalo, NY. Final report

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1995-01-01

    The Buffalo Sewer Authority (BSA), in cooperation with the New York State Energy Research and Development Authority (Energy Authority), commissioned a demonstration of a full scale indirect disk-type sludge dryer at the Bird Island Wastewater Treatment Plant (BIWWTP). The purpose of the project was to determine the effects of the sludge dryer on the sludge incineration process at the facility. Sludge incineration is traditionally the most expensive, energy-intensive unit process involving solids handling at wastewater treatment plants; costs for incineration at the BIWWTP have averaged $2.4 million per year. In the conventional method of processing solids, a series of volume reduction measures, which usually includes thickening, digestion, and mechanical dewatering, is employed prior to incineration. Usually, a high level of moisture is still present within sewage sludge following mechanical dewatering. The sludge dryer system thermally dewaters wastewater sludge to approximately 26%, (and as high as 38%) dry solids content prior to incineration. The thermal dewatering system at the BIWWTP has demonstrated that it meets its design requirements. It has the potential to provide significant energy and other cost savings by allowing the BSA to change from an operation employing two incinerators to a single incinerator mode. While the long-term reliability of the thermal dewatering system has yet to be established, this project has demonstrated that installation of such a system in an existing treatment plant can provide the owner with significant operating cost savings.

  3. Effect of brining on the drying rate of tilapia in a solar tunnel dryer

    Energy Technology Data Exchange (ETDEWEB)

    Kituu, G.M.; Shitanda, D.; Kanali, C.L.; Mailutha, J.T. [Jomo Kenyatta Univ. of Agriculture and Technology, Nairobi (Kenya). BEED

    2008-07-01

    In addition to being a source of protein, fish is an important source of local and foreign currency earnings in Kenya. A substantial amount of fish production is exported. Approximately 30 per cent is exported to the European Union, the United States, and countries in the Middle East, but nearly half of the total annual fish harvest in Kenya goes to waste due to poor processing and preservation. Measures must be taken to ensure the fish industry is protected and waste is minimized, since the livelihood of over 500,000 people depends on fish as a source of proteins and employment. Therefore, it is necessary to implement appropriate and affordable processing and preservation techniques for fish at the artisanal landing sites in order to reduce the wastage and spoilage of fish during oversupply, and to enhance long storage. This paper presented studies that were conducted to determine the effect of brining on the drying rate of tilapia in a solar tunnel dryer. The paper discussed the materials and methods, including a description of the solar tunnel dryer system; the brining process of fish; the fish drying process; and data analysis. It was concluded that limiting the amount of salt used in brining, and subsequently dehydrating fish with a solar tunnel dryer achieves a more stable and suitable dried fish product than osmotic dehydration or solar drying process separately. 19 refs., 5 figs., 2 appendices.

  4. PADDY DRYING IN MIXED ADSORPTION DRYER WITH ZEOLITE: DRYING RATE AND TIME ESTIMATION

    Directory of Open Access Journals (Sweden)

    Mochammad Djaeni

    2013-11-01

    Full Text Available Recently, the main problem of the rice stock and distribution in Indonesia is the quality degradation as indicated in unpleasant odor (smelly, stained, yellowness, and high percentage of broken rice. This is due to the low of paddy quality dried by from either direct sunlight or conventional fluidized bed dryer. As a result, the paddy cracks and breaks easily during milling in which causes the storage life being shorter as the enzymatic degradation by germ or fungi occurs. Air dehumidified with zeolite at drying medium temperature is potential to improve the quality of paddy. Zeolite is a material having high affinity to water vapor. In this case, the paddy and zeolite was mixed and fluidized with the air. The air will evaporate water from paddy, and at same time, the zeolite will adsorb water from air. Hence, the humidity of dryer can be kept low in which improves the driving force for drying. This work discusses the effect of presence of zeolite in the dryer, operational drying temperature, air velocity and relative humidity on drying rate of paddy. The results showed that increasing of zeolite as well as operational temperature increased the drying rate. In addition, using the model, the air dehumidification with zeolite and increase of air velocity can speed up drying time significantly at operational temperature below 80oC. This condition is very suitable for paddy drying since the quality degradation can be avoided.

  5. Modeling and simulation of the drying of thin sheets in a continuous infrared dryer

    Energy Technology Data Exchange (ETDEWEB)

    Dhib, R.; Broadbent, A.D.; Therien, N. (Sherbrooke Univ., PQ (Canada))

    1994-10-01

    A differential model describing the dynamics of the infrared drying process has been set up from mass and energy balances between the moving wet material, the radiant emitters, and the air forced inside the dryer. The objective of the study is to provide a predictive model that can be used to assess the dynamic behavior of the infrared drying of a thin sheet of porous material (e.g. paper or textile). The process output responses to changes in material velocity, heating power, and water content of the entering sheet are presented. Thin sheets of bleached cotton were used to calibrate the model, and experiments were conducted to cover the entire range of operating conditions of an infrared pilot-plant dryer. The model consists of a set of four coupled hyperbolic partial differential equations describing the variations of the air and web temperatures and humidities as a function of time and space along the dryer length. The model predictions agreed well with the experimental data. Model predictions using arithmetic averages for the parameters, and parameters correlated with operational variables, are also presented and discussed. 30 refs., 9 figs., 5 tabs.

  6. Design and development of desiccant seed dryer with airflow inversion and recirculation.

    Science.gov (United States)

    Gill, R S; Singh, Sukhmeet; Singh, Parm Pal

    2014-11-01

    A desiccant seed dryer has been developed to dry seed in deep bed at safe temperatures for good shelf life and germination. The dryer consists of two chambers viz., air conditioning control unit and seed drying chamber. It operates in seed drying mode and desiccant regeneration mode. It has provision for recirculation of the drying air to minimise the moisture removal from drying air. Also, it has provision of airflow inversion through deep seed bed for uniform drying. Moisture removal from drying air has been done using silica gel desiccant. Chilly 'Punjab Surakh', Chilly 'Punjab Guchhedaar', Paddy, Coriander, Fenugreek and Radish seeds was dried with hot air at 38 °C from initial moisture content of 26.9 to 5 % (wb) in 2 h, 46.52 to 4.19 % (wb) in 4.25 h, 13.3 to 2.61 % (wb) in 4 h, 13.4 to 10.08 % (wb) in 3 h, 12.4 to 8.22 % (wb) in 4¼ h and 10.6 to 6.08 % (wb) in 4 h respectively. The statistical analysis based on paired t-test showed that seed drying in this dryer has no adverse effect on seed germination.

  7. Designing, constructing and evaluating a dynamic prototype dryer for obtaining rolled dehydrated fruit pulp

    Directory of Open Access Journals (Sweden)

    Pedro Vanegas Mahecha

    2011-01-01

    Full Text Available  This paper describes how a functional prototype for a dynamic dryer was designed, along with its basic parts: drying tunnel, mechanical transport system for material inside the equipment and selecting and designing a system for supplying hot air. A simple transport mechanism was implemented which allowed combining two flow dispositions: parallel and countercurrent flow. Mango (Mangifera indica L pulp was dehydrated using three dryer air temperatures (50°C, 60°C and 70°C and three drying air speeds inside the dryer (1.6, 2.2, 3.4 m s-1 for evaluating the prototype. Propane gas was used as fuel for heating the air. The prototype design led to dehydrating fruit pulp having 4.26 bs smooth initial humidity content up to a 0.11 db final humidity content, with 8-hour drying time (70°C and 3.4 m s-1 air speed, assuming 4.5 0.5 mm pulp thickness, in 300 x 180 mm and 15 mm height rectangular trays. 1.5 0.5 mm thickness rolled dehydrated pulps were obtained in these conditions  The final product had 0.60a (aw water activity providing for a stable product, having low water content and very similar characteristics to those of the fresh product (shown by Weende analysis. 

  8. Drying of Rosella (Hibiscus sabdariffa Flower Petals using Solar Dryer with Double Glass Cover Collector

    Directory of Open Access Journals (Sweden)

    Tjukup Marnoto

    2014-10-01

    Full Text Available Chemical ingredients in rosella petals are very beneficial for health. Rosella petals needed to be drained for storage and packing purpose. The traditional drying takes 5 days and less healthy. Solar dryer technology can speed up the drying process and protect materials from dust contamination. Solar dryer with double glass covered collector has been designed and made for drying of agricultural products such as rosella flowers. Rosella petals as much as 2300 grams with initial moisture content of 90.84 % be dried with this dryer until the moisture content of 7.67 % takes only 2 days, although the weather was less sunny . The temperature in the drying chamber was not more than 50° C, so it was good for drying groceries, not damaging chemical ingredients. The relative humidity in the space dryeris was about 40 % and it was still relative low. Drying rate and drying performance was expressed by the efficiency and Specific Moisture Evaporation Rate ( SMER were influenced by water content of the dried material and weather. Daily efficiency at the first and the second day: 14.931 % and 5.78%, while the daily SMER on the first and the second day: 0.222 and 0.0256 ( kg / kWh .

  9. Design and Fabrication of a Direct Natural Convection Solar Dryer for Tapioca

    Directory of Open Access Journals (Sweden)

    Diemuodeke E. OGHENERUONA

    2011-06-01

    Full Text Available Based on preliminary investigations under controlled conditions of drying experiments, a direct natural convection solar dryer was designed and fabricated to dry tapioca in the rural area. This paper describes the design considerations followed and presents the results of MS excel computed results of the design parameters. A minimum of 7.56 m2 solar collector area is required to dry a batch of 100 kg tapioca in 20 hours (two days drying period. The initial and final moisture content considered were 79 % and 10 % wet basis, respectively. The average ambient conditions are 32ºC air temperatures and 74 % relative humidity with daily global solar radiation incident on horizontal surface of 13 MJ/m2/day. The weather conditions considered are of Warri (lat. 5°30’, long. 5°41’, Nigeria. A prototype of the dryer so designed was fabricated with minimum collector area of 1.08 m2. This prototype dryer will be used in experimental drying tests under various loading conditions.

  10. Drying operation of ceramic tile bodies n vertical dryers (first part); Le sechage des carreaux ceramiques dans les sechoirs verticaux (1. partie)

    Energy Technology Data Exchange (ETDEWEB)

    Mallol, G.; Mezquita, A.; Llorens, D.; Jarque, J.C. [Universitat Jaume I., Istituto de Tecnologia Ceramica, ITC, Association de Investigacion de las Industrias Ceramicas, Castellon (Spain); Sahun, J.; Valle, F. [Gas Natural SDF, S.A., Barcelona (Spain)

    2002-05-01

    Using different types of sensors, the operation in a steady and non-steady state of a vertical dryer used for drying ceramic tile bodies was studied. The evolution of tile body characteristics at the dryer exists is analysed in the first part of this article; Actions performed and optimising efficiency in the use of co-generation system output in vertical dryers will be handled in IC and V next issue. (authors)

  11. A comparative life cycle assessment of conventional hand dryer and roll paper towel as hand drying methods.

    Science.gov (United States)

    Joseph, Tijo; Baah, Kelly; Jahanfar, Ali; Dubey, Brajesh

    2015-05-15

    A comparative life cycle assessment, under a cradle to gate scope, was carried out between two hand drying methods namely conventional hand dryer use and dispenser issued roll paper towel use. The inventory analysis for this study was aided by the deconstruction of a hand dryer and dispenser unit besides additional data provided by the Physical Resources department, from the product system manufacturers and information from literature. The LCA software SimaPro, supported by the ecoinvent and US-EI databases, was used towards establishing the environmental impacts associated with the lifecycle stages of both the compared product systems. The Impact 2002+ method was used for classification and characterization of these environmental impacts. An uncertainty analysis addressing key input data and assumptions made, a sensitivity analysis covering the use intensity of the product systems and a scenario analysis looking at a US based use phase for the hand dryer were also conducted. Per functional unit, which is to achieve a pair of dried hands, the dispenser product system has a greater life cycle impact than the dryer product system across three of four endpoint impact categories. The use group of lifecycle stages for the dispenser product system, which represents the cradle to gate lifecycle stages associated with the paper towels, constitutes the major portion of this impact. For the dryer product system, the use group of lifecycle stages, which essentially covers the electricity consumption during dryer operation, constitutes the major stake in the impact categories. It is evident from the results of this study that per dry, for a use phase supplied by Ontario's grid (2010 grid mix scenario) and a United States based manufacturing scenario, the use of a conventional hand dryer (rated at 1800 W and under a 30s use intensity) has a lesser environmental impact than with using two paper towels (100% recycled content, unbleached and weighing 4 g) issued from a roll

  12. Rice Grain Physical and Chemical analysis from Paddy Drying by Using a Solar Tunnel Dryer at Prathum Tani, Thailand

    Directory of Open Access Journals (Sweden)

    Sookramoon Krissadang

    2016-01-01

    Full Text Available This paper presents the RD31 rice grain physical and chemical analysis from paddy drying by using a solar tunnel dryer. RD31 paddy was dried in a compact solar tunnel dryer, with a drying chamber volume in the size of 0.113 m3 and 2.112 m2 flat plate collectors. The experiment was performed on May 15, 2014 at Faculty of Industrial Technology Vallaya Alongkorn Rajabhat University Pathum Tani Thailand. The samples for testing were three varieties of Thai rice namely RD31 (from the farm, RD31 (dried in a solar tunnel dryer, and Prathum Tani 1 (from the market. The test consists of RD 31 dried by a solar tunnel dryer; the moisture content was reduced to about 14 wt. %. Then 3 varieties of rice were milled and sent to the laboratory for analyzing physical and chemical properties, repeated 3 times. The results showed that the average drying temperature was 67.75 °C. The paddy moisture reduction content was estimated from 49.96 to 14.64 MC (% w.b. within 6 hours. All dimensions of RD31, dried by using solar tunnel dryer milled rice were closely related to those of the Prathum Tani 1, purchased from the market. The ratio of length to width of 3 samples: RD31 (raw rice, RD31 (dried in solar tunnel dryer, and Prathum Tani 1 (from the market were 3.54, 3.47, and 3.44, respectively. 3 rice grain varieties were slender. The yield percentage was 60%, 75 %, and 70 %, respectively. Results from chemical test showed that the alkaline spreading value were 4-5, 3, and 2, respectively. The quality of the RD31 rice grain dried in a solar tunnel dryer passed the Thailand Ministry of Agriculture rice quality standard

  13. A large-scale solar greenhouse dryer using polycarbonate cover: Modeling and testing in a tropical environment of Lao People's Democratic Republic

    Energy Technology Data Exchange (ETDEWEB)

    Janjai, Serm; Intawee, Poolsak; Kaewkiew, Jinda; Sritus, Chanoke [Solar Energy Research Laboratory, Department of Physics, Faculty of Science, Silpakorn University, Nakhon Pathom 73000 (Thailand); Khamvongsa, Vathsana [Department of Physics, Faculty of Natural Science, National University of Laos, P O Box 7322, Vientiane (Lao People' s Democratic Republic)

    2011-03-15

    A large-scale solar greenhouse dryer with a loading capacity of 1000 kg of fruits or vegetables has been developed and tested at field levels. The dryer has a parabolic shape and the dryer is covered with polycarbonate sheets. The base of the dryer is a black concrete floor with an area of 7.5 x 20.0 m{sup 2}. Nine DC fans powered by three 50-W solar cell modules are used to ventilate the dryer. The dryer was installed at Champasak (15.13 N, 105.79 E) in Lao People's Democratic Republic (Lao PDR). It is routinely used to dry chilli, banana and coffee. To assess the experimental performances of the dryer, air temperature, air relative humidity and product moisture contents were measured. One thousand kilograms of banana with the initial moisture content of 68% (wb) was dried within 5 days, compared to 7 days required for natural sun drying with the same weather conditions. Also three hundred kilograms of chilli with the initial moisture content of 75% (wb) was dried within 3 days while the natural sun drying needed 5 days. Two hundred kilograms of coffee with the initial moisture content of 52% (wb) was dried within 2 days as compared to 4 days required for natural sun drying. The chilli, coffee and banana dried in this dryer were completely protected from insects, animals and rain. Furthermore, good quality of dried products was obtained. The payback period of the dryer is estimated to be 2.5 years. A system of partial differential equations describing heat and moisture transfer during drying of chilli, coffee and banana in the greenhouse dryer was developed. These equations were solved by using the finite different method. The simulated results agree well with the experimental data. This model can be used to provide the design data for this type of dryer in other locations. (author)

  14. UPAYA PENINGKATAN MUTU DAN EFISIENSI PROSES PENGERINGAN JAGUNG DENGAN MIXED-ADSORPTION DRYER

    Directory of Open Access Journals (Sweden)

    Luqman Buchori

    2013-11-01

    Full Text Available THE EFFORT OF EFFICIENCY AND QUALITY IMPROVEMENT ON CORN DRYING PROCESS USING MIXED-ADSORPTION DRYER. The main problem in corn drying process is the low of energy efficiency (50% and quality products. Consequently, operating costs in large for fuel consumption and the short shelf life of corn. Zeolite adsorption dryers have the potential to overcome this problem. This research aims to study composition of corn-zeolite and the effect of temperature on drying speed and protein and fat content in corn. Research variables are the ratio of corn and zeolite (1:0, 1:3, 1:1, 3:1 and intake air temperature (room temperature, 30oC, 40oC, 50oC. Sampling for moisture testing performed every 15 minutes. For energy purposes also calculated the energy efficiency (h based on the amount of heat used to evaporate water from the corn (Qevap divided by the total heat requirement to regenerate the zeolite and raising the air temperature (Qintr. Profiles of temperature and water in the mixed adsorption dryer are also studied. The results showed that the greater number of zeolite used, the water content of the final outcome a little more drying, protein and fat content of the final result of drying is relatively constant. The larger intake air temperature, the water content of the less drying results, protein content decreases, and the fat content does not change/relatively constant. The best variable was a ratio of corn: zeolite is 1:3 and air temperature was 50oC. While the variables that are suitable and in accordance with ISO standards for dry foods (14% are air temperature of between 40oC and 50oC with a ratio of corn:zeolite is 1:3. The energy efficiency of 81.23% is obtained. Modeling done with FEMLAB (COMSOL can describe the moisture content and temperature profiles in the corn and zeolite. Keywords: corn; drying; energy efficiency; mixed adsorption dryer; zeolite Abstrak Masalah utama proses pengeringan jagung adalah rendahnya efisiensi energi (50% dan mutu

  15. Consumer product safety: Risk assessment of exposure to asbestos emissions from hand-held hair dryers

    Science.gov (United States)

    Hallenbeck, William H.

    1981-01-01

    The United States Consumer Product Safety Commission (CPSC) is concerned that consumer exposure to asbestos from consumer products may present an unreasonable risk of injury. Recently, CPSC has obtained agreement by industry to cease production and distribution of hair dryers containing asbestos heat insulation. CPSC intends to broaden its investigation by selecting consumer products containing asbestos for “priority attention.” The Commission does not intend to make quantitative estimates of cancer risks posed by exposure to asbestos fibers in making regulatory decisions. This position may lead to a serious waste of resources for the Commission, industry, and society. The Commission should focus its initial attention on those products for which the release of asbestos is significant enough to cause an unreasonable health risk. To make a risk assessment for a particular use of asbestos, CPSC must acquire or request data on asbestos emissions and define “unreasonable risk to health.” In an attempt to give some meaning to the phrase “risk assessment,” the primary goal of this paper is to present a detailed risk assessment of exposure to asbestos from hand-held hair dryers. Several scenarios of use are presented using various assumptions regarding time of operation, mixing of fibers in a small room, rate of fiber emission, and time of exposure. The worst case analysis of the health risk of exposure to hair dryer emissions is based on several conservative assumptions and shows that the increased number of deaths per year due to respiratory cancer is 4 for the entire United States population. A more representative case analysis shows the increased number of deaths to be on the order of 0.15 per year.

  16. Survey on solar dryers for drying of food and wood in Ghana

    Energy Technology Data Exchange (ETDEWEB)

    Oestergaard Jensen, S.; Correll Frank, F. [Danish Technological Inst., Taastrup (Denmark); Floejgaard Kristensen, E. [Danish Inst. of Agricultural Sciences, Tjele (Denmark)

    1999-11-01

    The survey was conducted as a part of the project 'Test and Research Project into the Drying of Food and Wood Products with Solar Heat'. The aim of the survey was to investigate the need for drying of food and wood in Ghana and the already existing experience on solar drying in order to form a basis for the initial decisions within the project concerning the location of three demonstration solar dryers for crops, fish and wood, which species to dry and the type of solar dryers. The project deals with transfer of knowledge in the field of drying of crops and wood and solar air heating systems from Denmark to Ghana. The aim of the survey was, therefore, also to give the Danish experts an impression of the conditions in Ghana in order to facilitate an appropriate design of the solar dryers. Three of the four Danish partners participated in the survey. The fourth Danish partner - the manufacturer of solar heating systems Aidt Miljoe - are already familiar with the conditions in Ghana due to an earlier project in Ghana. The survey was planed by the Energy Commission of Ghana, the Ghanaian partner and consultants: DENG, University of Science and Technology, Kumasi and Econkoad. The time schedules for the survey - one for crops/fish and one for wood - are found in Annex A. The schedules were very well prepared and the sites to visit were well chosen. The visits gave the Danish experts a good overview of the situation in Ghana in the field of post harvesting of crops, handling of fish, drying and manufacturing of wood and existing experience on solar drying. The schedules included a large variety of different information and impressions e.g. ranging from large sawmill to small carpenters and workshops. Despite tight schedules the consultants managed to stick very close to the time schedules shown in Annex A. (au)

  17. Performance evaluation of solar assisted dryers for low temperature drying applications: Pt. 1; Plants description

    Energy Technology Data Exchange (ETDEWEB)

    Arata, A. (Universidad Tecnica Federico Santa Maria, Valparaiso (Chile)); Sharma, V.K. (Commission of the European Communities, Ispra (Italy))

    1991-01-01

    Research aimed at investigating the most appropriate cost effective food preservation technology suitable for implementation with limited financial resources is reported. It is hoped that the simple designs discussed in the present communication can be fabricated by small-scale industries using simple tools and relatively cheap and locally available materials. This first paper presents a detailed description, along with a preliminary heat transfer analysis, for fruit dryers developed and tested experimentally. Results obtained from the experiments conducted will be reported in a second paper. (author).

  18. Study on effectiveness of continuous solar dryer integrated with desiccant thermal storage for drying cocoa beans

    OpenAIRE

    Sari Farah Dina; Himsar Ambarita; Farel H. Napitupulu; Hideki Kawai

    2015-01-01

    The main objective is to assess effectiveness of continuous solar dryer integrated with desiccant thermal storage for drying cocoa beans. Two type of desiccants were tested, molecular sieve 13× (Na86 [(AlO2)86·(SiO2)106]·264H2O) as an adsorbent type and CaCl2 as an absorbent type. The results revealed that during sunshine hours, the maximum temperature within the drying chamber varied from 40 °C to 54 °C. In average, it was 9–12 °C higher than ambient temperature. These temperatures are very ...

  19. Burn injuries caused by a hair-dryer--an unusual case of child abuse.

    Science.gov (United States)

    Darok, M; Reischle, S

    2001-01-01

    About 1.4-26% burn injuries in children appear to be abusive in origin. A 2.5-year-old girl was referred to our institute because of suspected child abuse. Clinical examination and later interrogation of the mother revealed non-recent deep second degree burn injuries on both gluteal regions, caused by the partner of the mother by pressing a hand-held hair-dryer against the skin. The authors present the findings of this unusual method of child abuse.

  20. Drying characteristics of garlic ( Allium sativum L) slices in a convective hot air dryer

    Science.gov (United States)

    Demiray, Engin; Tulek, Yahya

    2014-06-01

    The effects of drying temperatures on the drying kinetics of garlic slices were investigated using a cabinet-type dryer. The experimental drying data were fitted best to the Page and Modified Page models apart from other theoretical models to predict the drying kinetics. The effective moisture diffusivities varied from 4.214 × 10-10 to 2.221 × 10-10 m2 s-1 over the temperature range studied, and activation energy was 30.582 kJ mol-1.

  1. Comparison of Linear and Nonlinear Model Predictive Control for Optimization of Spray Dryer Operation

    DEFF Research Database (Denmark)

    Petersen, Lars Norbert; Poulsen, Niels Kjølstad; Niemann, Hans Henrik;

    2015-01-01

    In this paper, we compare the performance of an economically optimizing Nonlinear Model Predictive Controller (E-NMPC) to a linear tracking Model Predictive Controller (MPC) for a spray drying plant. We find in this simulation study, that the economic performance of the two controllers are almost...... equal. We evaluate the economic performance with an industrially recorded disturbance scenario, where unmeasured disturbances and model mismatch are present. The state of the spray dryer, used in the E-NMPC and MPC, is estimated using Kalman Filters with noise covariances estimated by a maximum...

  2. Mathematical simulation of acoustic and gas-dynamical processes in the channel of an acoustoconvective dryer

    Science.gov (United States)

    Fedorchenko, I. A.; Fedorov, A. V.

    2013-07-01

    This paper presents and analyzes the data of numerical simulation of nonstationary flow in the channel of an acoustoconvective dryer in which the acoustic field is produced by a Hartmann generator. The gas-dynamical flow field and frequency characteristics of the problem are calculated in axisymmetric and three-dimensional formulations. The jet outflowing from the generator nozzle with change in the resonator length and in the jet pressure ratio was investigated parametrically. The results of numerical calculations are compared with experimental data.

  3. Building solar dryer of tropical woods; Construccion de un secador solar de maderas tropicales

    Energy Technology Data Exchange (ETDEWEB)

    Hernandez R, J; Flores M, F. E; Cuevas D, O [Universidad de Quintana Roo, Chetumal, Quintana Roo (Mexico); Tolentino E, G [LABINTHAP-SEPI-ESIME-IPN, Mexico, D.F. (Mexico)

    2000-07-01

    In Quintana Roo, Mexico, several species of wood are used for handicrafts. The most commonly method used in the communities nearby Chetumal is natural drying, with the disadvantage of low quality in their products because the moisture contains in the wood. In this project studied the design of solar dryer for tropical woods in Quintana Roo. [Spanish] En este trabajo, se parte del analisis de las condiciones climatologicas existentes en el estado de Quintana Roo, Mexico, asi como de las necesidades de madera seca de una comunidad, como parametros basicos para el diseno y construccion de un secador solar de maderas tropicales.

  4. A low-cost ultrasonic spray dryer to produce spherical microparticles from polymeric matrices

    Directory of Open Access Journals (Sweden)

    Priscilla Paiva Luz

    2007-01-01

    Full Text Available The spray-drying technique has been widely used for drying heat-sensitive foods, pharmaceuticals, and other substances, because it leads to rapid solvent evaporation from droplets. This method involves the transformation of a feed from a fluid state into a dried particulate, by spraying the feed into a hot medium. Despite being most often considered a dehydration process, spray drying can also be used as an encapsulation method. Therefore, this work proposes the use of a simple and low-cost ultrasonic spray dryer system to produce spherical microparticles. This equipment was successfully applied to the preparation of dextrin microspheres on a laboratory scale and for academic purposes.

  5. ANALISIS KELAYAKAN TEKNIS DAN FINANSIAL DARI INVESTASI PENGADAAN TRAY DRYER BERBAHAN BAKAR BIOMASSA PADA USAHA ARANG TEMPURUNG KELAPA BERBASIS EKSPOR (Studi Kasus di Tropica Nucifera Industry – Yogyakarta

    Directory of Open Access Journals (Sweden)

    Fanny Widadie

    2013-11-01

    Full Text Available The purpose of the study is to assess the technical and financial feasibility of procurement investment Tray Dryer fueled biomass to operations of coconut shell charcoal briquette in PT. Tropica Nucifera Industry. The result showed that investment-Tray Dryer on cocnut shell charcoal briquette bussiness was highly feasibile both the technical and financial aspects. The technical aspect was seen that the quantity-production capabilities of coconut shell charcoal briquettes using a dryer-Tray Dryer could be increased 15 percent compared the previous consdition-used of solar energy. While the quality of the charcoal briquettes produced from Tray Dryer was a much butter quality, moisture content (6.39%; ash (2.65%; carbon-bound (85.83%, compared to using sunlight, water content (15.89; ash (2.57% and carbon-bound (77.32%.The financial aspects of procurement Tray Dryer investment that its value was more feasible than previous, nothing Tray Dryer. Coconut shell charcoal briquet enterprises without using Tray Dryer was feasible to be done with NPV 1,058,928.12, IRR 63%, Payback Period 1 year and 9 moths, Net B/C 2.25 and analysis of swicthcing value reached 20 percent. And after the business using Tray Drayer, the financial analysis was much more feasible with NPV 2,285,500,498.12, IRR 113%, Payback Period 11 months, Net B/C 3.5 and analysis of switching value reached 50 percent.

  6. Drying of Rhinacanthus nasutus (Linn. Kurz. using a solar dryer incorporated with a backup thermal energy storage from wood combustion

    Directory of Open Access Journals (Sweden)

    Perapong Tekasakul

    2006-05-01

    Full Text Available An indirect, natural convection, solar cabinet dryer incorporated with a backup thermal energy storage from wood combustion was designed and tested with the Thai herb, Rhinacanthus nasutus (Linn. Kurz. Most of Thai herbs are widely used as traditional medicine and drying is an initial step in the production process. Solar dryer with a biomass backup heating system is the most feasible solution to drying in Thailand. In this work, a 4 m x 5 m solar collector was used to absorb solar radiation for heating the incoming air during the daytime, while a biomass burner was used to supply heat when solar energy was not possible. Heat from fuelwood combustion was accumulated in the thermal storage system made of bricks, and was used to heat up the incoming air. Results showed that the herb was dried uniformly and the temperature inside the drying cabinet could be maintained above 50ºC for more than 10 hours. Thermal efficiency when using solar energy was 10.5%, but the value was less than 1% when using the heat from biomass burning. This resulted from the low moisture content of the products after being dried by the solar energy. The dryer is beneficial to the operators, particularly in southern Thailand, where continuous drying is required. This dryer is by no means limited to drying of the herb. Currently, four dryers of the same model have been used by farmer groups in southern Thailand for drying bananas, several types of herbs, fish, and other products. In economic consideration, its payback period is 5.5 years when compared with the LPG-equipped dryer. When the total cost and production capacity are considered, its payback period is about 6 years.

  7. Comparative performance of coriander dryer coupled to solar air heater and solar air-heater-cum-rockbed storage

    Energy Technology Data Exchange (ETDEWEB)

    Chauhan, P.M.; Choudhury, C.; Garg, H.P. [Indian Inst. of Technology, Centre for Energy Studies, New Delhi (India)

    1996-03-01

    In the present communication, efforts have been made to study the drying characteristics of coriander in a stationary 0.5 tonne/batch capacity deep-bed dryer coupled to a solar air heater and a rockbed storage unit to receive hot air during sunshine and off-sunshine hours, respectively. The drying bed was assumed to consist of a number of thin layers of grains stacked upon each other. The theoretical investigation was made by writing the energy and mass balance equations for different components of the dryer-cum-air-heater-cum-storage and by adopting a finite difference approach for simulation. (author)

  8. Performance Analysis of Solar Assisted Fluidized Bed Dryer Integrated Biomass Furnace with and without Heat Pump for Drying of Paddy

    OpenAIRE

    M. Yahya

    2016-01-01

    The performances of a solar assisted fluidized bed dryer integrated biomass furnace (SA-FBDIBF) and a solar assisted heat pump fluidized bed dryer integrated biomass furnace (SAHP-FBDIBF) for drying of paddy have been evaluated, and also drying kinetics of paddy were determined. The SA-FBDIBF and the SAHP-FBDIBF were used to dry paddy from 11 kg with moisture content of 32.85% db to moisture content of 16.29% db (14% wb) under an air mass flow rate of 0.1037 kg/s within 29.73 minutes and 22.9...

  9. Experimental investigation of a solar dryer with natural convective heat flow

    Energy Technology Data Exchange (ETDEWEB)

    Gbaha, P.; Yobouet Andoh, H.; Kouassi Saraka, J. [Laboratoire d' Energies d' Energies Nouvelles et Renouvelables, Institut National Polytechnique Felix Houphoeuet-Boigny, B.P. 1526 Yamoussoukro (Ivory Coast); Kamenan Koua, B.; Toure, S. [Laboratoire d' Energie Solaire, Universite de Cocody, 22 B.P.: 582, Abidjan 22 (Ivory Coast)

    2007-09-15

    A direct type natural convection solar dryer is designed. It is constructed in local materials (wood, blades of glass, metals) then tested experimentally in foodstuffs drying (cassava, bananas, mango). It is about an experimental approach which consists in analyzing the behavior of the dryer. The study relates mainly kinetics and establishment of drying heat balances. The influence of significant parameters governing heat and mass transfers, such as solar incident radiation, drying air mass flow and effectiveness, is analyzed in order to evaluate its thermal performances. Experimental data can be represented by empirical correlations of the form M(t)=M{sub i}exp(-kt) for representation of drying process. The resolution of these drying equations makes-possible to predict total drying time of each product. Moreover, this drying process allows to reduce the moisture content of cassava and sweet banana approximately to 80% in 19 and 22 h, respectively to reach the safety threshold value of 13%. This value permits the conservation of these products about one year without deterioration. The determination of parameters, like ambient temperature, drying chamber temperature, drying air mass flow and incident heat fluxes, allow to predict the drying effectiveness for modeling and refining the dimensioning of the elaborate prototype. (author)

  10. Modelling the drying kinetics of green peas in a solar dryer and under open sun

    Energy Technology Data Exchange (ETDEWEB)

    Sunil [Department of Mechanical Engineering, BRCM CET Bahal, Haryana–127028 (India); Varun [Department of Mechanical Engineering, NIT Hamirpur, (H.P.)–177005 (India); Sharma, Naveen [Department of Mechanical and Industrial Engineering, IITR, (U.K.)–247667 (India)

    2013-07-01

    The drying kinetics of green peas was investigated in an indirect solar dryer and under open sun. The entire drying process took place exclusively in falling rate period. The constant rate period was absent from the drying curves. The rehydration capacity was also determined for peas dried in solar dryer and under open sun. The rehydration capacity of solar dried peas was found higher than open sun dried peas. The drying data obtained from experiments were fitted to eight different mathematical models. The performance of these models was examined by comparing the coefficient of correlation (R2), sum of squares error (SSE), mean squared error (MSE) and root mean square error (RMSE) between observed and predicted values of moisture ratios. Among these models, the thin layer drying model developed by Page showed good agreement with the data obtained from experiments for bottom tray. The Midilli et al. model has shown better fit to the experimental data for top tray and open sun than other models.

  11. DESIGN AND PERFORMANCE TESTING OF AN INDUSTRIAL-SCALE INDIRECT SOLAR DRYER

    Directory of Open Access Journals (Sweden)

    R. KHAMA

    2016-09-01

    Full Text Available In this paper, an indirect solar dryer was developed and tested for drying food. This unit operation is an interesting technique for preservation in agricultural applications. The dryer was designed at industrial scale in order to carry out experiments in real applications and to get concrete results. It operated without additional energy in the passive and active modes, allowing the comparison between the two. The relationship between the solar collector air temperature and the relevant ambience parameters was deduced. The collector efficiency reached 66.56 % with forced ventilation and 46.32 % with natural ventilation. It also increased linearly with the solar radiation varying between 400-800 W/m2 for air velocities ranging between 1 and 1.40 m/s. The effect of the air velocity on the collector efficiency was negligible for solar intensities close to 800 W/m2.The tomato drying occurred mainly in the falling drying rate period. On average, the moisture content in dry basis was reduced from 14.32 kg water/kg dry matter to 0.14 kg water/kg dry matter. The equilibrium moisture content of tomatoes was reached after 12 when the system was used with one layer. In the case it was used with four layers, the difference among the four durations of drying was one hour between each tray.

  12. Mathematical Modelling of a Reduced Thermal Energy Consuming Spray Dryer for Evaporating Caustic Soda Solution

    Directory of Open Access Journals (Sweden)

    Babatope Olufemi

    2012-06-01

    Full Text Available Experimental demonstration, mathematical modelling and simulation of a technique for reducing thermal energy consumption in the diaphragm cell process using a techno-economically viable process to produce 73% wt. NaOH from electrolytic diaphragm cell catholytes of about 10% wt. NaOH was carried out in this work. The technique completely eradicated the use of thermal energy in concentrating catholyte effluents from about 10% wt. NaOH solution to 50% wt. NaOH solution. This resulted in a specific energy savings of about 2.68×106 J/kg NaOH. The use of a spray dryer for increasing the concentration of 50% wt. NaOH solution to 73% wt. NaOH solution further improved the energy savings compared to that of multiple effect evaporators by 1.41×106 J/kg of solution, which corresponds to about 61.05% specific energy savings. The deviation of all simulated results from experimental data was between -0.062 and +0.084, portraying a good predictive tool for probing into the spray dryer operations. This work is expected to reduce considerably the total energy consumption of the diaphragm cell process through process integration or new processing methodology, with improved equipment designs.

  13. Life Cycle Cost of Solar Biomass Hybrid Dryer Systems for Cashew Drying of Nuts in India

    Science.gov (United States)

    Dhanushkodi, Saravanan; Wilson, Vincent H.; Sudhakar, Kumarasamy

    2015-12-01

    Cashew nut farming in India is mostly carried out in small and marginal holdings. Energy consumption in the small scale cashew nut processing industry is very high and is mainly due to the high energy consumption of the drying process. The drying operation provides a lot of scope for energy saving and substitutions of other renewable energy sources. Renewable energy-based drying systems with loading capacity of 40 kg were proposed for application in small scale cashew nut processing industries. The main objective of this work is to perform economic feasibility of substituting solar, biomass and hybrid dryer in place of conventional steam drying for cashew drying. Four economic indicators were used to assess the feasibility of three renewable based drying technologies. The payback time was 1.58 yr. for solar, 1.32 for biomass and 1.99 for the hybrid drying system, whereas as the cost-benefit estimates were 5.23 for solar, 4.15 for biomass and 3.32 for the hybrid system. It was found that it is of paramount importance to develop solar biomass hybrid dryer for small scale processing industries.

  14. Drying process optimization for an API solvate using heat transfer model of an agitated filter dryer.

    Science.gov (United States)

    Nere, Nandkishor K; Allen, Kimberley C; Marek, James C; Bordawekar, Shailendra V

    2012-10-01

    Drying an early stage active pharmaceutical ingredient candidate required excessively long cycle times in a pilot plant agitated filter dryer. The key to faster drying is to ensure sufficient heat transfer and minimize mass transfer limitations. Designing the right mixing protocol is of utmost importance to achieve efficient heat transfer. To this order, a composite model was developed for the removal of bound solvent that incorporates models for heat transfer and desolvation kinetics. The proposed heat transfer model differs from previously reported models in two respects: it accounts for the effects of a gas gap between the vessel wall and solids on the overall heat transfer coefficient, and headspace pressure on the mean free path length of the inert gas and thereby on the heat transfer between the vessel wall and the first layer of solids. A computational methodology was developed incorporating the effects of mixing and headspace pressure to simulate the drying profile using a modified model framework within the Dynochem software. A dryer operational protocol was designed based on the desolvation kinetics, thermal stability studies of wet and dry cake, and the understanding gained through model simulations, resulting in a multifold reduction in drying time.

  15. Drying of suspensions and solutions on inert particle surface in mechanically spouted bed dryer

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    To eliminate some disadvantages of the conventional spouted bed dryers the mechanically spouted bed (MSB) system was developed. This dryer type is convenient to use inert particles providing an increased surface area for drying of materials of high-moisture content and heat sensitive materials. On three different drying tasks are demonstrated the experimental optimization of process parameters to obtain products of demanded quality. The main object was at drying of AlO(OH) suspension to preserve the particle size under 2.5 μm and to obtain product with a moisture content of about 0.05 kg/kg (d.b.). For this reason a very thin particle coating and intensive abrasion had to be assured. At drying of tomato concentrates the thermoplasticity makes the process very difficult. To jump over the deliquescent and sticky state developed at the critical temperature-moisture content values a very short drying time (8-10 s) must be provided. The third task was to form powder-like product from bovine serum albumin (BSA) solution having very low solid content (2-4%). The selected process parameters given in this paper resulted in a mean particle size of less than 20 μm while the soluble preserved protein content was higher than 90%.

  16. Making large, flowable particles of protein or disaccharide in a mini-scale spray dryer.

    Science.gov (United States)

    Schaefer, Joachim; Lee, Geoffrey

    2016-11-01

    A mini-scale spray dryer, the ProCept 4M8, with a 1.4 m or 2.1 m drying chamber length has been used to prepare large, flowable particles of catalase, trehalose or lactose. A 25 kHz ultrasonic nozzle or a Rayleigh breakup mono-disperse droplet generator was used for atomization. The ultrasonic nozzle produced dried particles of average diameter ≥30 µm that show incipient flow behavior when measured with the vibrating spatula method. A high solute concentration of 69% w/w in the liquid feed was required, which is readily achievable with trehalose but not with the viscous catalase solution. At lower solute concentrations, e.g. 20% w/w, the mono-disperse droplet generator was able to produce well flowable particles of approximately 50 µm diameter, although with a low yield. This is a result of collisions between the droplets falling through the drying chamber when then coalesce. It is possible to produce dried, flowable particles in milligram quantities on a mini-scale spray dryer such as the ProCept using the 25 kHz ultrasonic nozzle. With the mono-disperse droplet generator the long drying chamber ensures a residence time of a number of seconds, but this also allows droplet coalescence at fall heights >40 cm.

  17. Performance analysis of solar-assisted chemical heat-pump dryer

    Energy Technology Data Exchange (ETDEWEB)

    Fadhel, M.I. [Solar Energy Research Institute, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor (Malaysia); Faculty of Engineering and Technology, Multimedia University, Jalan Ayer Keroh Lama, 75450, Melaka (Malaysia); Sopian, K.; Daud, W.R.W. [Solar Energy Research Institute, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor (Malaysia)

    2010-11-15

    A solar-assisted chemical heat-pump dryer has been designed, fabricated and tested. The performance of the system has been studied under the meteorological conditions of Malaysia. The system consists of four main components: solar collector (evacuated tubes type), storage tank, solid-gas chemical heat pump unit and dryer chamber. A solid-gas chemical heat pump unit consists of reactor, condenser and evaporator. The reaction used in this study (CaCl2-NH{sub 3}). A simulation has been developed, and the predicted results are compared with those obtained from experiments. The maximum efficiency for evacuated tubes solar collector of 80% has been predicted against the maximum experiment of 74%. The maximum values of solar fraction from the simulation and experiment are 0.795 and 0.713, respectively, whereas the coefficient of performance of chemical heat pump (COP{sup h}) maximum values 2.2 and 2 are obtained from simulation and experiments, respectively. The results show that any reduction of energy at condenser as a result of the decrease in solar radiation will decrease the coefficient of performance of chemical heat pump as well as decrease the efficiency of drying. (author)

  18. Standard practice for acoustic emission examination of cast iron yankee and steam heated paper dryers

    CERN Document Server

    American Society for Testing and Materials. Philadelphia

    2007-01-01

    1.1 This practice provides guidelines for carrying out acoustic emission (AE) examinations of Yankee and Steam Heated Paper Dryers (SHPD) of the type to make tissue, paper, and paperboard products. 1.2 This practice requires pressurization to levels used during normal operation. The pressurization medium may be high temperature steam, air, or gas. The dryer is also subjected to significant stresses during the heating up and cooling down periods of operation. Acoustic Emission data maybe collected during these time periods but this testing is beyond the scope of this document. 1.3 The AE measurements are used to detect, as well as, localize emission sources. Other methods of nondestructive testing (NDT) may be used to further evaluate the significance of acoustic emission sources. 1.4 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine th...

  19. Drying kinetics of whole and sliced turmeric rhizomes (Curcuma longa L. in a solar conduction dryer

    Directory of Open Access Journals (Sweden)

    A. Borah

    2015-09-01

    Full Text Available Drying of turmeric was carried out in a solar conduction dryer (SCD. Drying air temperature was achieved around 39–51 °C for an ambient temperature in the range of 25–28 °C. Moisture content from 78.65% (wb, was reduced to 6.36% (wb and 5.50% (wb for solid and sliced samples respectively in 12 h effective drying time. Drying curve of sliced samples showed more uniform falling in comparison to that of whole samples. The average effective moisture diffusivity was found to be 1.852 × 10−10 m2 s−1 for slab samples and 1.456 × 10−10 m2 s−1 for solid samples. Out of four models tried for simulation, Page model was found as best fitted thin layer drying model when simulation was done for all the drying data. The overall thermal efficiency of the dryer was found to be 55%. Drying of sliced rhizomes showed better drying kinetics and effective drying time could be reduced by slicing instead of drying in whole form.

  20. Solar Drying Kinetics of Cass Ava Slices in a Mixed Flow Dryer

    Directory of Open Access Journals (Sweden)

    Dairo Olawale Usman

    2015-12-01

    Full Text Available Drying characteristics of cassava slices was investigated in a mixed mode natural convection solar dryer to obtain a suitable mathematical model describing the drying. The average drying chamber temperature was between 34 ±2 °C and 50 ±1.8 °C, while 10 commonly used thin layer drying models were used for drying curve modelling. Coefficient of determination (R2 and root mean square error (RMSE were used to determine the models performances. The drying curve of cassava slices showed a reduction of moisture content with increased drying time in the solar dryer, and the variation of moisture ratio exponentially decreased with increased drying time. The Midilli and Logarithmic models showed better fit to the experimental drying data of cassava slices. As compared with other models tested, there were no significant differences (p >0.05 in the R2 values obtained for the Midilli and Logarithmic models; hence, the Logarithmic model was preferable because of the lower RMSE. The diffusion mechanism could be used to describe the drying of cassava slices that was found to be in the falling rate period. A diffusion coefficient (Deff of 1.22 × 10-8 m2 s-1 was obtained, which was within the established standard for food products.

  1. Modelling the drying kinetics of green peas in a solar dryer and under open sun

    Directory of Open Access Journals (Sweden)

    Sunil, Varun, Naveen Sharma

    2013-01-01

    Full Text Available The drying kinetics of green peas was investigated in an indirect solar dryer and under open sun. The entire drying process took place exclusively in falling rate period. The constant rate period was absent from the drying curves. The rehydration capacity was also determined for peas dried in solar dryer and under open sun. The rehydration capacity of solar dried peas was found higher than open sun dried peas. The drying data obtained from experiments were fitted to eight different mathematical models. The performance of these models was examined by comparing the coefficient of correlation (R2, sum of squares error (SSE, mean squared error (MSE and root mean square error (RMSE between observed and predicted values of moisture ratios. Among these models, the thin layer drying model developed by Page showed good agreement with the data obtained from experiments for bottom tray. The Midilli et al. model has shown better fit to the experimental data for top tray and open sun than other models.

  2. Life Cycle Cost of Solar Biomass Hybrid Dryer Systems for Cashew Drying of Nuts in India

    Directory of Open Access Journals (Sweden)

    Dhanushkodi Saravanan

    2015-12-01

    Full Text Available Cashew nut farming in India is mostly carried out in small and marginal holdings. Energy consumption in the small scale cashew nut processing industry is very high and is mainly due to the high energy consumption of the drying process. The drying operation provides a lot of scope for energy saving and substitutions of other renewable energy sources. Renewable energy-based drying systems with loading capacity of 40 kg were proposed for application in small scale cashew nut processing industries. The main objective of this work is to perform economic feasibility of substituting solar, biomass and hybrid dryer in place of conventional steam drying for cashew drying. Four economic indicators were used to assess the feasibility of three renewable based drying technologies. The payback time was 1.58 yr. for solar, 1.32 for biomass and 1.99 for the hybrid drying system, whereas as the cost-benefit estimates were 5.23 for solar, 4.15 for biomass and 3.32 for the hybrid system. It was found that it is of paramount importance to develop solar biomass hybrid dryer for small scale processing industries.

  3. Analysis and Testing of a Natural Convection Solar Dryer for the Tropics

    Directory of Open Access Journals (Sweden)

    A. O. Adelaja

    2013-01-01

    Full Text Available Solar dryers are imperative for the tropical and sub-Saharan African countries, which are faced with the duo challenges of inadequate electrical energy supply, which has severely limited the application of conventional refrigeration as a means of preservation of agricultural produce, and the need to make produce competitive in the international market. In this study, a cost-effective natural convection solar dryer was developed; the thermal and drying analyses were done and tested to obtain some performance evaluation parameters for the system in order to examine its efficiency and effectiveness by drying some plantain fillets. The collector and system efficiencies are found to be 46.4% and 78.73%, respectively, while a percentage moisture removal of 77.5% was achieved at the 20th hour in order to give final moisture contents of 15.75% in the product, which still maintained its integrity. With a cost of about $195.00, it has been affordable for the small- and medium-scale enterprises as well as for private use in domestic applications.

  4. Formulation and evaluation of albumin microspheres and its enteric coating using a spray-dryer.

    Science.gov (United States)

    Bejugam, Naveen K; Uddin, Akm N; Gayakwad, Sanjay G; D'Souza, Martin J

    2008-12-01

    This study optimized and evaluated the conditions for surface coating of microspheres using a spray-dryer. Four formulations of Bromophenol blue (BPB)-loaded albumin microspheres were prepared using a spray-dryer, cross-linked at different concentrations and time periods. One of the optimized formulations with the desired characteristics was selected for enteric coating with Eudragit L100-55. The procedure involved suspending BPB microspheres in polymer solution and spray-drying it. Four enteric coated formulations were prepared with different concentrations of microspheres in suspension (0.25 and 0.5%w/v) and polymer concentrations (0.25 and 0.5%w/v). Change in the mean particle size after coating was determined using a Laser Particle Counter. The surface coating technique employed did not significantly increase the particle size. Enteric coating efficiency was determined in simulated gastric fluid. Compared to the uncoated microspheres the cumulative amount of drug released from coated microspheres was significantly lower for 3 h, implying efficient surface coating.

  5. An Analytical Solution Applied to Heat and Mass Transfer in a Vibrated Fluidised Bed Dryer

    Energy Technology Data Exchange (ETDEWEB)

    Picado, Apolinar

    2011-07-01

    A mathematical model for the drying of particulate solids in a continuous vibrated fluidised bed dryer was developed and applied to the drying of grain wetted with a single liquid and porous particles containing multicomponent liquid mixtures. Simple equipment and material models were applied to describe the process. In the plug-flow equipment model, a thin layer of particles moving forward and well mixed in the direction of the gas flow was regarded; thus, only the longitudinal changes of particle moisture content and composition as well as temperature along the dryer were considered. Concerning the material model, mass and heat transfer in a single isolated particle was studied. For grain wetted with a single liquid, mass and heat transfer within the particles was described by effective transfer coefficients. Assuming a constant effective mass transport coefficient and effective thermal conductivity of the wet particles, analytical solutions of the mass and energy balances were obtained. The variation of both transport coefficients along the dryer was taken into account by a stepwise application of the analytical solution in space intervals with non-uniform inlet conditions and averaged coefficients from previous locations in the dryer. Calculation results were verified by comparison with experimental data from the literature. There was fairly good agreement between experimental data and simulation but the results depend strongly on the correlation used to calculate heat and mass transfer coefficients. For the case of particles containing a multicomponent liquid mixture dried in the vibrated fluidised bed dryer, interactive diffusion and heat conduction were considered the main mechanisms for mass and heat transfer within the particles. Assuming a constant matrix of effective multicomponent diffusion coefficients and thermal conductivity of the wet particles, analytical solutions of the diffusion and conduction equations were obtained. The equations for mass

  6. Métodos de seleção de secadores Dryer selection methods

    Directory of Open Access Journals (Sweden)

    Luís Felipe Toro Alonso

    2005-06-01

    Full Text Available Quando uma etapa de secagem faz-se necessária, o engenheiro deve escolher um secador adequado que se integre no processo como um todo. E ele deverá comparar as vantagens e desvantagens dentre as várias alternativas disponíveis tomando em conta tanto o ponto de vista técnico como o econômico. Alguns autores escrevem sobre a seleção de secadores. Embora cada autor desenvolva seleção dos secadores de um modo próprio, identifica-se uma linha geral no procedimento de escolha do equipamento. Todos os autores estabelecem um roteiro ou um fluxograma com questionamentos segundo os quais somos dirigidos ao equipamento mais apropriado. De uma breve revisão sobre o tema, podemos notar dois mecanismos básicos para o desenvolvimento da seleção de secadores: analítico - em que uma seqüência de processos decisórios elimina os equipamentos inadequados à solução, conduzindo à determinação da melhor solução; numérico - em que cada equipamento recebe uma pontuação de acordo com a sua adequação à solução do problema, na totalização, a melhor solução é a que obtém a maior pontuação. Neste artigo são apresentados os resultados da seleção de secadores obtidos em um novo modelo de seleção proposto por ALONSO [2].When a drying step is needed, the engineer must choose the most adequate equipment, which must fit into the whole process. He must compare the advantages and disadvantages among the many available choices considering both technical and economic aspects. Some authors describe the dryer selection. Even though each author develops his or her own dryer selection, a general guideline in their dryer selection models may be identified. Every author establishes a query or a flowchart by which through its inquiry we are guided to the most appropriate equipment. From a brief review, one may notice two basic procedures for dryer selection: analytical by which a series of process decision eliminates the inappropriate equipment

  7. A new methodology for measurement of sludge residence time distribution in a paddle dryer using X-ray fluorescence analysis.

    Science.gov (United States)

    Charlou, Christophe; Milhé, Mathieu; Sauceau, Martial; Arlabosse, Patricia

    2015-02-01

    Drying is a necessary step before sewage sludge energetic valorization. Paddle dryers allow working with such a complex material. However, little is known about sludge flow in this kind of processes. This study intends to set up an original methodology for sludge residence time distribution (RTD) measurement in a continuous paddle dryer, based on the detection of mineral tracers by X-ray fluorescence. This accurate analytical technique offers a linear response to tracer concentration in dry sludge; the protocol leads to a good repeatability of RTD measurements. Its equivalence to RTD measurement by NaCl conductivity in sludge leachates is assessed. Moreover, it is shown that tracer solubility has no influence on RTD: liquid and solid phases have the same flow pattern. The application of this technique on sludge with different storage duration at 4 °C emphasizes the influence of this parameter on sludge RTD, and thus on paddle dryer performances: the mean residence time in a paddle dryer is almost doubled between 24 and 48 h of storage for identical operating conditions.

  8. Design and Performance Evaluation of a Solar Assisted Heat Pump Dryer Integrated with Biomass Furnace for Red Chilli

    Directory of Open Access Journals (Sweden)

    M. Yahya

    2016-01-01

    Full Text Available The performance of a solar assisted heat pump dryer integrated with biomass furnace has been designed and evaluated for drying red chillies, and drying kinetics of red chillies were evaluated. The red chillies were dried from 22 kg with moisture content of 4.26 db to moisture content of 0.08 db which needed 11 hours, with the average drying chamber temperature, drying chamber relative humidity, and an air mass flow rate of 70.5°C, 10.1%, and 0.124 kg/s, respectively, while the open sun drying needed 62 hours. Compared to open sun drying, this dryer yielded 82% saving in drying time. The drying rate, the specific moisture extraction rate, and thermal efficiency of the dryer were estimated in average to be about 1.57 kg/h, 0.14 kg/kWh, and 9.03%, respectively. Three mathematical models, the Newton, Henderson-Pabis, and Page models, were fitted to the experimental data on red chillies dried by solar assisted heat pump dryer integrated with biomass furnace and open sun drying. The performance of these models was evaluated by comparing the coefficient of determination (R2, mean bias error (MBE, and root mean-square error (RMSE. The Page model gave the best results for representing drying kinetics of red chillies.

  9. Energy-saving dryer that protects laundry. Thermodynamics and functional model. Final report of 1{sup st} phase; Energiesparender, waescheschonender Trockner. Thermodynamik und Funktionsmuster. Schlussbericht der 1. Phase

    Energy Technology Data Exchange (ETDEWEB)

    Friedl, M.; Weilenmann, U.

    2006-07-01

    Tumble-dryer with heat recuperation: the goal of this project is to develop a tumble-dryer with high energy efficiency (class A), which dries laundry gently and which does not cost more than normal dryers. This goal is to be achieved with a tumble-dryer with heat recuperation. Top efficiency is attainable: a thermodynamic analysis showed that with the suggested concept the efficiency of the most efficient dryers can be reached. The critical parameter thereby is the heat transfer inside of the dryer-drum. The greater this transfer is, the more efficient the dryer will be. A quantification of this heat transfer will only be possible using an operating model. Stationary computations: this report describes the thermodynamic analysis as well as the design of the operating model. The computations presented in this report are based on stationary conditions. For the interpretation of the tests with the operating model a time-dependent computation will be used. Manufacturing of the operating model in 2{sup nd} phase: in the next project phase the operating model will be manufactured. By means of various measurements and tests to be made the energy efficiency is to be demonstrated and the parameters for an optimal drying-process are to be found. (author)

  10. Using landfill gas as the primary fuel for a 200 WTPD thermal dryer[Held jointly with the 4. Canadian organic residuals and biosolids managment conference

    Energy Technology Data Exchange (ETDEWEB)

    Shulmister, D. [Manattee County, Manatee, FL (United States). Wastewater Division; Monroe, A. [McKim and Creed, Cary, NC (United States)

    2007-07-01

    Although there is no evidence of health problems, there is a growing opposition to class B land application of biosolids in many localities in the United States, resulting in less sites available to dispose of class B biosolids. Manatee County, located on the West Coast of Florida, decided to implement thermal drying of its biosolids. This produced a class A pellet that could be used without restriction as a fertilizer or soil amendment. The dryer will be located at the county's southeast water reclamation facility, adjacent to the county's Lena Road landfill. The methane gas from the landfill will be used as the primary fuel for the dryer. This paper presented how Manatee County, Florida decided to meet its long term biosolids handling and disposal needs. The paper provided background information on Manatee County, Florida. It discussed the reasons for the dryer technology selection, location of the dryer, sizing criteria as well as listing the components of the dryer. The paper also discussed dryer procurement. Other topics that were presented included fuel requirements and an analysis of landfill gas. The County expects to save approximately two million dollars per year by selecting landfill gas from its Lena Road landfill as the primary fuel for the dryer. 5 tabs.

  11. An experimentally validated simulation model for a four-stage spray dryer

    DEFF Research Database (Denmark)

    Petersen, Lars Norbert; Poulsen, Niels Kjølstad; Niemann, Hans Henrik

    2017-01-01

    is divided into four consecutive stages: a primary spray drying stage, two heated fluid bed stages, and a cooling fluid bed stage. Each of these stages in the model is assumed ideally mixed and the dynamics are described by mass- and energy balances. These balance equations are coupled with constitutive...... equations such as a thermodynamic model, the water evaporation rate, the heat transfer rates, and an equation for the stickiness of the powder (glass transition temperature). Laboratory data is used to model the equilibrium moisture content and the glass transition temperature of the powder. The resulting...... mathematical model is an index-1 differential algebraic equation (DAE) model with 12 states, 9 inputs, 8 disturbances, and 30 parameters. The parameters in the model are identified from well-excited experimental data obtained from the industrialtype spray dryer. The simulated outputs ofthe model are validated...

  12. Design and Experimentation of Collector based Solar Dryer with Recirculation for Spices

    Directory of Open Access Journals (Sweden)

    Mr. Ganesh There

    2016-02-01

    Full Text Available Sun drying system is very common method of preserving agricultural product. Solar energy is used for heating of air and to dry food substance. In open sun drying food is unprotected from rain, wind-borne dirt and dust, infestation by insects, rodents and other animal. This process is practically attractive and environmentally sound. Shell life of agricultural product is improve by drying. This paper present design and construction of active solar dryer with recirculation technique. It consists of solar collector, drying chamber with netted trays and recirculation arrangement. Air is allowed through inlet and it is heated up in collector. Then it is circulated in drying chamber where it is utilize for drying. The design based on geographical location Wardha and meteorological data were obtained for proper design specification. Locally available materials were used for construction such as polyurethane glass, mild steel metal sheet, plywood sheet and insulating material.

  13. Evaluation and comparing of natural and forced solar dryer for mint drying in Khuzestan province

    Directory of Open Access Journals (Sweden)

    J Habibi Asl

    2017-05-01

    Research Center during the years 2011-2013. Materials and Methods In this research an indirect cabinet solar dryer with three trays and grooved collector was constructed. To improve air convection, a chimney was mounted above the dryer. The dryer performance was evaluated by drying mint leaves in three levels of mass density of 2, 3, and 4 kg m-2 at two drying manners of natural and forced convection and compared with drying mint leaves in shade as the traditional method. Results and Discussion The results showed that total drying time required in different solar drier treatments was 3.5 to 15 h, while it was about 5 days in traditional method. Drying time in upper trays was more as the air flow decreased due to increase in mass density. Mean required drying time in forced convection was 29.7% less than that of natural convection. Maximum essences with 0.80% and 0.76% were belonged to "natural convection and 3kg m-2 mass density" and "forced convection and 4 kg m-2 mass density" treatments respectively, while minimum one with 0.30% was for "forced convection and 2 kg m-2 mass density" treatment. Also, the highest and lowest chlorophyll content with 8.51 and 4.18 mg ml-1 were measured in "natural convection and 3 kg m-2 mass density" and "forced convection and 4 kg m-2 mass density" treatments respectively. According to obtained results, 3 and 4 kg m-2 mass density can be suggested for natural and forced convection solar drying of mint leaves in Khuzestan condition respectively. Conclusions In order to reduce vegetable losses and increase Khuzestan vegetable producers income, indirect cabinet solar dryer for drying mint leaves in winter season, could be an appropriate option. For natural and forced convection drying methods, mass density of 3 and 4 kg m-2 is recommended respectively.

  14. Simulation of Solar Heat Pump Dryer Directly Driven by Photovoltaic Panels

    Science.gov (United States)

    Houhou, H.; Yuan, W.; Wang, G.

    2017-05-01

    This paper investigates a new type of solar heat pump dryer directly driven by photovoltaic panels. In order to design this system, a mathematical model has been established describing the whole drying process, including models of key components and phenomena of heat and mass transfer at the product layer and the air. The results of simulation at different drying air temperatures and velocities have been calculated and it indicate that the temperature of drying air is crucial external parameter compared to the velocity, with the increase of drying temperature from 45°C to 55°C, the product moisture content (Kg water/Kg dry product) decreased from 0.75 Kg/Kg to 0.3 Kg/Kg.

  15. Solar drying of West Indian ginger (Zingiber officinale Roscoe) rhizome using a wire basket dryer

    Energy Technology Data Exchange (ETDEWEB)

    Balladin, D.A.; Headley, O. [University of the West Indies (Barbados). Dept. of Chemistry; Chang Yen, I. [University of the West Indies, St. Augustine (Trinidad and Tobago). Dept. of Chemistry; McGaw, D.R. [University of the West Indies, St. Augustine (Trinidad and Tobago). Dept. of Chemical Engineering

    1996-09-01

    A wire basket dryer (1.8 m x 0.9 m x 0.2 m) was used to dry sliced (0.15 cm) West Indian ginger (Zingiber officinale Roscoe) rhizome to an acceptable moisture content of 10.2% (dry weight basis) over a 3 day period. The optimum charge size was 14.97 kg, with a packing density of 462.04 kg m{sup -3} and a specific drying rate of 0.446 h{sup -1}. The quantities (determined by high-pressure liquid chromatography) of the main pungent principles (ginerol and shogaol) extracted from fresh, non-steam-distilled solar-dried and steam-distilled solar-dried ginger rhizomes showed increases of 0.068, 0.46 and 0.67 g [per 100 g (dry weight basis)], respectively, with a decrease in the oleoresin quality (reflected in pungency profile) of the same order. (author)

  16. Adsorption isotherms of hog plum (Spondias mombin L. pulp powder obtained by spray dryer

    Directory of Open Access Journals (Sweden)

    Luís Gomes de Moura Neto

    2015-05-01

    Full Text Available Food sorption isotherms are highly important to predict drying time and storage conditions of a product. Current assay evaluates the behavior of adsorption isotherms of hog plum powder obtained by spray-dryer, through mathematical models. GAB, BET, Henderson and Oswin models were adjusted to the experimental data at 25, 30, 35 and 40ºC. The BET model best adjusted to the atomized hog plum for all temperatures tested, with an error ranging between 8.45 and 11.17%. The coefficient of determination (R2 had rates higher than 0.9900 for all the adjusted models. The behavior of hog plum powder adsorption isotherms was classified as Type III.

  17. Chitosan microspheres loaded with holmium-165 produced by spray dryer for liver cancer therapy: preliminary experiments

    Energy Technology Data Exchange (ETDEWEB)

    Miyamoto, Douglas Massao; Pires, Geovanna; Lira, Raphael A. de; Melo, Vitor H.S.; Nascimento, Nanci; Azevedo, Mariangela de Burgos M. de, E-mail: douglas.miyamoto@usp.b [Instituto de Pesquisas Energeticas e Nucleares (IPEN/CNEN-SP), Sao Paulo, SP (Brazil); Osso Junior, Joao Alberto [Instituto de Pesquisas Energeticas e Nucleares (IPEN/CNEN-SP), Sao Paulo, SP (Brazil). Centro de Radiofarmacia

    2011-07-01

    Chitosan is a biopolymer of 2-deoxy-2-amino-D-glucose that is obtained by deacetylation of chitin. It's biocompatible, biodegradable, non toxic and has antitumor activity. Chitosan has many applications, such as their microparticles that can be used to treat prostate cancer, rheumatoid arthritis, and for liver tumor brachytherapy treatment. Our group is developing different biodegradable polymer-based microspheres loaded with holmium-165 for this purpose. The Chitosan microspheres were produced loaded with holmium (III) chloride, and not loaded with it, by Mini Spray Dryer procedure. The microspheres were evaluated by scanning electron microscopy, energy dispersive spectroscopy (EDS), confocal laser scanning microscopy, thermogravimetric analysis, particle size, and X-ray diffraction. The EDS analysis confirmed the holmium chloride presence into the prepared chitosan microparticles. (author)

  18. The Development of a Spray Dryer based on a Food Industrial Viewpoint

    Science.gov (United States)

    Katoh, Fumio

    The spray dryer, which will satisfy the future demands, is developed through the engineering approach in accordance to 3A- Sanitary Standards in the food industry. The main points are as follows. 1) A High Discharge-Single Swirl Atomizer is adapted for practical use; which can mix effectively with single hot air jet. 2) An optimum jet distributer eliminates swirling components in the jet. 3) Secondary air from the periphery of the jet controls the diffusion and Coanda effect of the jet. 4) The drying chamber's wall is controlled at a temperature below the "Sticky Point" of products. 5) An optimum cooler is included in the bottom of the drying chamber. The above devices prevent undried particles from adhering to the drying chamber's wall, improve the fluidity of products as powder particles, and bring about high efficiency, stable and high quality long lasting productivity.

  19. Matrix structure selection in the microparticles of essential oil oregano produced by spray dryer.

    Science.gov (United States)

    da Costa, Joyce Maria Gomes; Borges, Soraia Vilela; Hijo, Ariel Antonio Campos Toledo; Silva, Eric Keven; Marques, Gerson Reginaldo; Cirillo, Marcelo Ângelo; de Azevedo, Viviane Machado

    2013-01-01

    The goal of this work was to select the best combination of encapsulants for the microencapsulation of oregano essential oil by spray dryer with the addition of Arabic gum (AG), modified starch (MS) and maltodextrin (MA). The simplex-centroid method was used to obtain an optimal objective function with three variables. Analytical methods for carvacrol quantification, water activity, moisture content, wettability, solubility, encapsulation efficiency (ME) and oil retention (RT) were used to evaluate the best combination of encapsulants. The use of AG as a single wall material increased ME up to 93%. Carvacrol is the major phenolic compound existent in the oregano essential oil. Carvacrol exhibits a maximum concentration of 57.8% in the microparticle with the use of 62.5% AG and 37.5% MA. A greater RT (77.39%) was obtained when 74.5% AG; MS 12.7% and 12.7% MA were applied, and ME (93%) was improved with 100% of gum.

  20. Drying operation of ceramic tile bodies in vertical dryers (second part); Le sechage des carreaux ceramiques dans les sechoirs verticaux (2. partie)

    Energy Technology Data Exchange (ETDEWEB)

    Mallol, G.; Mezquita, A.; Llorens, D.; Jarque, J.C.; Sahun, J.; Valle, F. [Universitat Jaume I., Istituto de Tecnologia Ceramica, ITC, Association de Investigacion de las Industrias Ceramicas, Castellon (Spain); Gas Natural SDF, S.A., Barcelona (Spain)

    2002-06-01

    The operation in a steady and non-steady state of a vertical dryer used for drying ceramic tile bodies and the evolution of tile body characteristics at the dryer exists were studied in the first part of this article. This second part deals with the adjustments of the burner temperature settings during stoppage, gas flow rate in the stack and recirculating gas flow rate. In addition, in some drying facilities co-generation systems are used with internal gas combustion motors. In the present study a series of modifications is proposed regarding existing facilities in order to optimise current dryer use. (authors)

  1. Performance of a Big Scale Green House Type Dryer for Coffee Drying Process

    Directory of Open Access Journals (Sweden)

    Sukrisno Widyotomo

    2014-12-01

    Full Text Available Dying is one of important steps in coffee processing to produce good quality. Greenhouse is one of artificial drying alternatives that potential for coffee drying method cause of cleans environmental friendly, renewable energy sources and chippers. Indonesian Coffee and Cocoa Research Institute has developed and testing a big scale greenhouse type dryer for fresh coffee cherries and wet parchment coffee drying process. Greenhouse has 24 m length, 18 m width, also 3 m high of the front side and 2 m high of the rear side. The maximum capacity of greenhouse is 40 tons fresh coffee cherries. Fiber Reinforced Plastic (FRP used as greenhouse roof that combined with I and C profile of steel. Fresh coffee cherries and wet parchment coffee from Robusta variety use as main materials in this research. The treatment of this research was 30 kg/m2, 60 kg/m2 and 90 kg/m2 for coffee density. String process has done by manual, two times a day in the morning and in the afternoon. As control, fresh coffee cherries and wet parchment coffee has dried by fully sun drying method. The result showed that a big scale greenhouse has heat drying efficiency between 29.9-58.2% depend on type and density of coffee treatments. On the full sunny day, greenhouse has produced maximum drying air temperature up to 52oC. In radiation cumulative level 4-5 kW-jam/m2 per day, 12.9-38.8 tons fresh coffee cherries or wet parchment coffee with 58-64% moisture content can be dried to 12% moisture content for 6 up to 14 days drying process. Slowly drying mechanism can be avoided negative effect to degradation of quality precursor compound. Capacity of the dryer can be raise and fungi can be reduce with application of controllable mechanical stirring in the greenhouse. Keywords: greenhouse, coffee, drying, quality

  2. Solar energy dryer kinetics using flat-plate finned collector and forced convection for potato drying

    Science.gov (United States)

    Batubara, Fatimah; Misran, Erni; Dina, Sari Farah; Heppy

    2017-06-01

    Research on potato drying using the indirect solar dryer with flat-plate finned collector and forced convection has been done. The research was conducted at the outdoor field of Laboratory of Institute for Research and Standardization of Industry on June 14th-23rd, 2016 from 9:00 am to 4:00 pm. This research aims to obtain the drying kinetics model of potato (Solanumtuberosum L.) using an indirect solar dryer's (ISD) with flat plate-finned collector and forced convection. The result will be compared to the open sun drying (OSD) method. Weather conditions during the drying process took place as follows; surrounding air temperature was in the range 27 to 34.7 °C, relative humidity (RH) 29.5 to 61.0% and the intensity of solar radiation 105.6 to 863.1 Watt/m2. The dried potato thicknesses were 1.0 cm, 1.5 cm and 2.0 cm, with the average initial water content of 76.46%. The average temperature in the collector chamber ranged from 42.2 to 57.4 °C and the drying chamber was at 46.2 °C. The best drying result was obtained from a sample size of 1 cm thickness using the IDS method with an average drying rate of 0.018 kg H2O per kg dry-weight.hour and the water content was constant at 5.02% in 21 hours of drying time. The most suitable kinetics model is Page model, equation MR = exp (-0.049 t1,336) for 1.0 cm thickness, exp (-0.066 t1,222) for 1.5 cm thickness and exp (-0.049 t1,221) for 2.0 cm thickness. The quality of potato drying using ISD method is better than using OSD which can be seen from the color produced.

  3. Impact of flow induced vibration acoustic loads on the design of the Laguna Verde Unit 2 steam dryer

    Energy Technology Data Exchange (ETDEWEB)

    Forsyth, D. R.; Wellstein, L. F.; Theuret, R. C.; Han, Y.; Rajakumar, C. [Westinghouse Electric Company LLC, Cranberry Township, PA 16066 (United States); Amador C, C.; Sosa F, W., E-mail: forsytdr@westinghouse.com [Comision Federal de Electricidad, Central Nucleoelectrica Laguna Verde, Km 42.5 Carretera Cardel-Nautla, 91680 Alto Lucero, Veracruz (Mexico)

    2015-09-15

    Industry experience with Boiling Water Reactors (BWRs) has shown that increasing the steam flow through the main steam lines (MSLs) to implement an extended power up rate (EPU) may lead to amplified acoustic loads on the steam dryer, which may negatively affect the structural integrity of the component. The source of these acoustic loads has been found to be acoustic resonance of the side branches on the MSLs, specifically, coupling of the vortex shedding frequency and natural acoustic frequency of safety relief valves (SRVs). The resonance that results from this coupling can contribute significant acoustic energy into the MSL system, which may propagate upstream into the reactor pressure vessel steam dome and drive structural vibration of steam dryer components. This can lead to high-cycle fatigue issues. Lock-in between the vortex shedding frequency and SRV natural frequency, as well as the ability for acoustic energy to propagate into the MSL system, are a function of many things, including the plant operating conditions, geometry of the MSL/SRV junction, and placement of SRVs with respect to each other on the MSLs. Comision Federal de Electricidad and Westinghouse designed, fabricated, and installed acoustic side branches (ASBs) on the MSLs which effectively act in the system as an energy absorber, where the acoustic standing wave generated in the side-branch is absorbed and dissipated inside the ASB. These ASBs have been very successful in reducing the amount of acoustic energy which propagates into the steam dome. In addition, modifications to the Laguna Verde Nuclear Power Plant Unit 2 steam dryer have been completed to reduce the stress levels in critical locations in the dryer. The objective of this paper is to describe the acoustic side branch concept and the design iterative processes that were undertaken at Laguna Verde Unit 2 to achieve a steam dryer design that meets the guidelines of the American Society of Mechanical Engineers, Boiler and Pressure

  4. Alterations in fruit and vegetable β-carotene and vitamin C content caused by open-sun drying, visqueen-covered and polyethylene-covered solar-dryers

    OpenAIRE

    Ndawula, J; Kabasa, JD; Byaruhanga, YB

    2004-01-01

    This study investigated the effects of three drying methods (open sun drying, visqueen-covered solar dryer and polyethylene-covered solar dryer) on b-carotene and vitamin C content of edible portions of mango fruit (Mangifera indica) and cowpea leaves (Vigna unguiculata). Commercial samples were analysed for vitamin C by titrimetry and b-carotene by spectrophotometery at 450nm. Differences in vitamin retention and loss associated with the three drying methods were assessed by analysis of vari...

  5. Heat transfer to immersed horizontal tubes in gas fluidized bed dryers

    Energy Technology Data Exchange (ETDEWEB)

    Jonassen, Ola

    1999-07-01

    The main objective of this study was to construct heat pump fluidized bed dryers of the FHT type with improved dewatering capacity for a given size of the dryer. The use of heat exchangers immersed in the fluidized bed drying chambers is an important part of the FHT (Fluidized Bed High Temperature Heat Pump Dryer) concept. A pilot plant FHT dryer was built and successfully tested on fish meal raw material and seaweed. The plant included two fluidized bed drying chambers with immersed heat exchangers. The gain in water vapor of the drying air through the chambers was increased up to four times that of adiabatic drying. The energy saving concept was retained as a SMER ratio of 3.5 to 4.7 was measured in the same tests. Therefore optimization of the immersed heat exchangers was considered the most important single objective for this work. The optimization study of the heat exchangers was confined to the actual operating conditions for the dryers using: (1) Bubbling gas fluidized beds were used, (2) air as the only type of fluidizing gas,(3) beds at atmospheric pressure, (4) bed temperatures below 100 {sup o}C, (5) fluidized particles of Geldart classes B and D, (6) horizontal tube banks for the immersed heat exchanger and the influence of radiation heat transfer was ignored. The heat transfer study was confined to the fluidized bed side of the heat exchanger surface. It was concluded early in this work that the bubbles play a major role in generating the particle circulation inside the bed and hence also in heat transfer. Publications describing the most important bubble induced mechanisms contributing to high rates of heat transfer were found to be limited. Therefore the first part of this study was aimed at establishing a method for locating and measuring the size and rise velocity of bubbles inside the bed. The method established through this work using differential pressure measurements from two static pressure probes was used later in the study of heat transfer

  6. Heat transfer to immersed horizontal tubes in gas fluidized bed dryers

    Energy Technology Data Exchange (ETDEWEB)

    Jonassen, Ola

    1999-10-01

    The main objective of this study was to construct heat pump fluidized bed dryers of the FHT type with improved dewatering capacity for a given size of the dryer. The use of heat exchangers immersed in the fluidized bed drying chambers is an important part of the FHT (Fluidized Bed High Temperature Heat Pump Dryer) concept. A pilot plant FHT dryer was built and successfully tested on fish meal raw material and seaweed. The plant included two fluidized bed drying chambers with immersed heat exchangers. The gain in water vapor of the drying air through the chambers was increased up to four times that of adiabatic drying. The energy saving concept was retained as a SMER ratio of 3.5 to 4.7 was measured in the same tests. Therefore optimization of the immersed heat exchangers was considered the most important single objective for this work. The optimization study of the heat exchangers was confined to the actual operating conditions for the dryers using: (1) Bubbling gas fluidized beds were used, (2) air as the only type of fluidising gas, (3) beds at atmospheric pressure, (4) bed temperatures below 100 {sup o}C, (5) fluidized particles of Geldart classes B and D, (6) horizontal tube banks for the immersed heat exchanger, and the influence of radiation heat transfer was ignored. The heat transfer study was confined to the fluidized bed side of the heat exchanger surface. It was concluded early in this work that the bubbles play a major role in generating the particle circulation inside the bed and hence also in heat transfer. Publications describing the most important bubble induced mechanisms contributing to high rates of heat transfer were found to be limited. Therefore the first part of this study was aimed at establishing a method for locating and measuring the size and rise velocity of bubbles inside the bed. The method established through this work using differential pressure measurements from two static pressure probes was used later in the study of heat transfer

  7. Modeling 3D conjugate heat and mass transfer for turbulent air drying of Chilean papaya in a direct contact dryer

    Science.gov (United States)

    Lemus-Mondaca, Roberto A.; Vega-Gálvez, Antonio; Zambra, Carlos E.; Moraga, Nelson O.

    2017-01-01

    A 3D model considering heat and mass transfer for food dehydration inside a direct contact dryer is studied. The k- ɛ model is used to describe turbulent air flow. The samples thermophysical properties as density, specific heat, and thermal conductivity are assumed to vary non-linearly with temperature. FVM, SIMPLE algorithm based on a FORTRAN code are used. Results unsteady velocity, temperature, moisture, kinetic energy and dissipation rate for the air flow are presented, whilst temperature and moisture values for the food also are presented. The validation procedure includes a comparison with experimental and numerical temperature and moisture content results obtained from experimental data, reaching a deviation 7-10 %. In addition, this turbulent k- ɛ model provided a better understanding of the transport phenomenon inside the dryer and sample.

  8. Modeling 3D conjugate heat and mass transfer for turbulent air drying of Chilean papaya in a direct contact dryer

    Science.gov (United States)

    Lemus-Mondaca, Roberto A.; Vega-Gálvez, Antonio; Zambra, Carlos E.; Moraga, Nelson O.

    2016-03-01

    A 3D model considering heat and mass transfer for food dehydration inside a direct contact dryer is studied. The k- ɛ model is used to describe turbulent air flow. The samples thermophysical properties as density, specific heat, and thermal conductivity are assumed to vary non-linearly with temperature. FVM, SIMPLE algorithm based on a FORTRAN code are used. Results unsteady velocity, temperature, moisture, kinetic energy and dissipation rate for the air flow are presented, whilst temperature and moisture values for the food also are presented. The validation procedure includes a comparison with experimental and numerical temperature and moisture content results obtained from experimental data, reaching a deviation 7-10 %. In addition, this turbulent k- ɛ model provided a better understanding of the transport phenomenon inside the dryer and sample.

  9. Sorbent utilization studies using a mini-pilot spray dryer. Final report, 1 September 1992--31 August 1993

    Energy Technology Data Exchange (ETDEWEB)

    Keener, T.C.; Khang, S.J.; Wang, J.; Sanders, J.F.

    1993-09-30

    The main body of the report consists of four parts: 1. additives to change process chemistry for SO{sub 2} absorption by Ca(OH){sub 2} slurry; 2. recycle tests and hydration of fly ash with Ca(OH){sub 2} to increase reactivity; 3. limestone as an alternative sorbent and additive effects; 4. physical and chemical model developments for some of the additive effects and spray dryer mathematical model application. As the concentration of SO{sub 2} in the flue gases increases, the SO{sub 2} removal efficiency will go down. Additives such as delinquent salts (NaOH, NaCl, and NaHCO{sub 3}) have been shown to improve SO{sub 2} uptake, and these additive tests have indicated that SO{sub 2} uptake may be increased by as much as 60% over baseline conditions. Other additives such as H{sub 2}O{sub 2}, sugar, and some organic acids which can change the chemical reaction processes are suggested and tested, and some promising results have been obtained. Recycle has been shown to increase sorbent utilization by allowing partially reacted sorbent to react further with the SO{sub 2} in the flue gases. Two types of Ohio coal fly ashes have been extensively studied, and improvement of utilization in spray dryer flue gas desulfurization has been demonstrated. Limestone represents an area where significant cost savings can be realized. The spray dryer tests were designed to provide some results for understanding the magnitude of the limestone performance in the spray dryer system and the additive effects. The additive effects on increasing SO{sub 2} absorption by Ca(OH){sub 2} slurry were investigated, and the chemical and physical properties of these tested additives were studied. Some models have been formed to explain the additive phenomena.

  10. Performance of A Horizontal Cylinder Type Rotary Dryer for Drying Process ofOrganic Compost from Solid Waste Cocoa Pod

    Directory of Open Access Journals (Sweden)

    Sukrisno Widyotomo

    2008-07-01

    Full Text Available Cocoa pod husk is the bigest component of cocoa pod, about 70% of total ht of mature pod, and to potentially used as organic compost source. Poten tial solid waste of cocoa pod husk from a cocoa processing centre is about 15— 22 m3/ha/year. A cocoa plantation needs about 20—30 ton/ha/year of organic matters. One of important steps in compos processing technology of cocoa pod solid waste is drying process. Organic compost with 20% moisture content is more easy in handling, application, storage and distribution. Indonesian Coffee and Cocoa Research Institute has designed and tested a horizontal cylinder type rotary dryer for drying process of organic compos from solid waste cocoa pod with kerosene burner as energy sources. The objective of this research is to study performance of a horizontal cylinder type rotary dryer using kerosene burner as energy source for drying process of organic compost from solid waste cocoa pod. The material used was solid waste cocoa pod with 70—75% moisture content (wet basis, 70% size particle larger than 4.76 mm, and 30% size particle less than 4.76 mm, 690—695 kg/m3 bulk density. Drying process temperatures treatment were 60OC, 80OC, and 100OC, and cylinder rotary speed treatments were 7 rpm, 10 rpm, dan 16 rpm. The results showed that dryer had capacity about 102—150 kg/h depend on drying temperature and cylinder rotary speed. Optimum operation condition at 100OC drying temperature, and 10 rpm cylinder rotary speed with drying time to reach final moisture content of 20% was 1,6 h, capacity 136,14 kg/ h, bulk density 410 kg/m3, porocity 45,15%, kerosene consumption as energy source was 2,57 l/h, and drying efficiency 68,34%. Key words : cocoa, drying, rotary dryer, compost, waste

  11. Study of dynamic structure and heat and mass transfer of a vertical ceramic tiles dryer using CFD simulations

    Science.gov (United States)

    Kriaa, Wassim; Bejaoui, Salma; Mhiri, Hatem; Le Palec, Georges; Bournot, Philippe

    2014-02-01

    In this study, we developed a two-dimensional Computational Fluid Dynamics (CFD) model to simulate dynamic structure and heat and mass transfer of a vertical ceramic tiles dryer (EVA 702). The carrier's motion imposed the choice of a dynamic mesh based on two methods: "spring based smoothing" and "local remeshing". The dryer airflow is considered as turbulent ( Re = 1.09 × 105 at the dryer inlet), therefore the Re-Normalization Group model with Enhanced Wall Treatment was used as a turbulence model. The resolution of the governing equation was performed with Fluent 6.3 whose capacities do not allow the direct resolution of drying problems. Thus, a user defined scalar equation was inserted in the CFD code to model moisture content diffusion into tiles. User-defined functions were implemented to define carriers' motion, thermo-physical properties… etc. We adopted also a "two-step" simulation method: in the first step, we follow the heat transfer coefficient evolution (Hc). In the second step, we determine the mass transfer coefficient (Hm) and the features fields of drying air and ceramic tiles. The found results in mixed convection mode (Fr = 5.39 at the dryer inlet) were used to describe dynamic and thermal fields of airflow and heat and mass transfer close to the ceramic tiles. The response of ceramic tiles to heat and mass transfer was studied based on Biot numbers. The evolutions of averages temperature and moisture content of ceramic tiles were analyzed. Lastly, comparison between experimental and numerical results showed a good agreement.

  12. High efficiency technical solutions for domestic tumble dryer design and modeling of a dryer - with mechanical very humic air compression; Evaluation des solutions techniques a haute efficacite energetique pour les seche-linges domestiques - conception et modelisation d'un seche-linge a re-compression mecanique d'air tres humide

    Energy Technology Data Exchange (ETDEWEB)

    Palandre, L.

    2005-12-15

    The aim of this work is to evaluate high efficiency solutions for domestic tumble dryers. A specific analysis focuses on the thermodynamic cycle with very humid air compression. The main components are designed. In a first time, two technologies of dryers are studied: evacuation dryer, and condensation dryer. Drying cycles are measured and analyzed. The energy consumption for the standard 5 kg cotton cycle is in the range of 3.3 kWh and 3.6 kWh. Two alternative solutions are proposed to reduce significantly the energy consumption: a heat pump dryer with R-134a, or an open cycle using steam or very humid air as refrigerant. In both cases, the energy consumption is cut by a factor 2. The measurement of convective heat transfer coefficients between linen and humid air has allowed to elaborate a correlation giving the Lewis function evolution with very high absolute humidity. Heat exchanges in the tumble have been characterized. A correlation giving the heat transfer coefficient in function of air mass flow rate, linen mass, and its relative humidity, is developed. An unsteady-state model is developed. It gives the drying cycle of the tumble dryer with mechanical very humid air compression. Simulations show that drying time could be reduced to 1 hour using this process compared to 2 hours with R-134a heat pump dryers. (author)

  13. Characterization of NO[sub 2] and SO[sub 2] removals in a spray dryer/baghouse system

    Energy Technology Data Exchange (ETDEWEB)

    O' Dowd, W.J.; Markussen, J.M.; Pennline, H.W. (Dept. of Energy, Pittsburgh, PA (United States)); Resnik, K.P. (Gilbert/Commonwealth, Inc., Library, PA (United States))

    1994-11-01

    Oxidation of NO to NO[sub 2] has been proposed as a method for enhancing NO[sub x] removals in conventional flue gas desulfurization (FGD) processes. This experimental investigation characterizes the removals of NO[sub 2] and SO[sub 2] in a 1.1 m[sup 3](standard)/min spray dryer/baghouse system. Flue gas was generated by burning a No. 2 fuel oil, which was subsequently spiked upstream of the spray dryer with NO[sub 2] or SO[sub 2] or both. Lime slurry was injected via a rotary atomizer into the spray dryer. Variables studied include the approach to the adiabatic saturation temperature, stoichiometric ratio, SO[sub 2] concentration, and NO[sub 2] concentration. Significant quantities of NO[sub 2] are scrubbed in this system, and over half of the total removal (at inlet NO[sub 2] > 400 ppm) occurs in the baghouse. Increasing NO[sub 2] concentrations enhance the amount of NO[sub x] removed in the system. Also, the presence of significant quantities of NO[sub 2] enhances the baghouse SO[sub 2] removal. Although up to 72% NO[sub 2] removals were obtained, concentrations of NO[sub 2] that exited the system were greater than 50 ppm for all conditions investigated.

  14. A study for the thermal treatment of dehydrated sewage sludge with gas-agitated double screw type dryer.

    Science.gov (United States)

    Kim, Hey-Suk; Shin, Mi-Soo; Jang, Dong-Soon; Na, Eun-Soo

    2005-01-01

    A specially designed dryer has been developed for the thermal treatment of dehydrated, highly viscous sewage sludge with moisture content more than 80 wt.% by an gas-agitated, double-screw type dryer system. The treatment capacity of sludge dryer was about 100 kg/h. It consists of burner, feeding hopper, hot gas supplying ducts with double screw conveyor, damper and outlets of drying gas and dried material. The sewage sludge was transported by the revolution of the cylinder conveyor together with the tumbling and mixing action of the screw and lifters. The heating of the sludge was made efficient by the combination action of conduction and convection modes together with the gas-agitation process. The conduction occurred across the surface of the combustor cylinder, the convection was made by the flue gas interaction over the sludge and the agitation action through holes of conveyor cylinder into the bottom of the sludge. The number and location of gas-agitation holes and thereby the fraction of drying gas into the agitation holes were evaluated by numerical calculation of turbulent reacting flow. To evaluate the performance of the dryer developed in this study, a series of parametric experiments were performed in terms of important variables. In general drying process occurred successfully even for the highly agglomerating municipal sewage sludge through the first lumped plastic phase to a fine granulate state when the heat and mass balance was matched by adjusting rpm of the conveyor, burner capacity, and the fraction of gas-agitation. Further the avoidance of initial sludge agglomeration was considered to be important by the combination action of screw and lifter. The weight of the sludge was reduced approximately by 60% and therefore the volume of sludge was decreased to approximately 75% of initial volume with the water content of 10-20%. Energy efficiency of dryer was evaluated in the range of 70-75% at the sludge feed rate, 100 kg/h. The results obtained show

  15. Mathematical modeling of drying of potato slices in a forced convective dryer based on important parameters.

    Science.gov (United States)

    Naderinezhad, Samira; Etesami, Nasrin; Poormalek Najafabady, Arefe; Ghasemi Falavarjani, Majid

    2016-01-01

    The effect of air temperature, air velocity, and sample shapes (circle and square with the same cross-sectional area) on kinetic drying of potato slices in a tunnel dryer was investigated experimentally and a suitable drying model was developed. The experiments of drying of potato slices were conducted at an air temperature of 45-70°C with an air velocity 1.60 and 1.81 m sec(-1). Results showed that drying temperature was the most effective parameter in the drying rate. The influence of air velocity was more profound in low temperature. The time for drying square slices was lower compared to the circle ones. Furthermore, drying data were fitted to different empirical models. Among the models, Midilli-Kucuk was the best to explain the single layer drying of potato slices. The parameters of this model were determined as functions of air velocity and temperature by multiple regression analysis for circle and square slices. Various statistical parameters were examined for evaluating the model.

  16. Design of a Low Cost Smart Dryer Temperature Measurement System for Tea Factories

    Directory of Open Access Journals (Sweden)

    Utpal SARMA

    2009-09-01

    Full Text Available This paper presents the design of a low cost smart dryer temperature measurement system for Tea Factories using K-type Thermocouple implementing linearization polynomial. The thermo emf is amplified by an instrumentation amplifier having high CMRR (106 dB and high input impedance (1012 Ohm. The analog signal is converted to digital form with the help of an SPI compatible 12-bit ADC. Data acquisition and transmission is done with an 8- bit microcontroller. As the dependence of thermo emf on temperature is not linear hence it is fitted with a polynomial. NIST data for K-type TC is taken as a standard for this fitting. The error with linear fit and polynomial fit is also presented. The digital data is corrected according to the polynomial and sent to a PC located at a remote control room for monitoring and data logging via RS232C communication. The performance of the entire system is discussed in the paper.

  17. Evaluation of convective heat transfer coefficient of various crops in cyclone type dryer

    Energy Technology Data Exchange (ETDEWEB)

    Akpinar, E. Kavak [Mechanical Engineering Department, Firat University, 23279 Elazig (Turkey)]. E-mail: eakpinar@firat.edu.tr

    2005-09-15

    In this paper, an attempt was made to evaluate the convective heat transfer coefficient during drying of various crops and to investigate the influences of drying air velocity and temperature on the convective heat transfer coefficient. Drying was conducted in a convective cyclone type dryer at drying air temperatures of 60, 70 and 80 deg. C and velocities of 1 and 1.5 m/s using rectangle shaped potato and apple slices (12.5 x 12.5 x 25 mm) and cylindrical shaped pumpkin slices (35 x 5 mm). The temperature changes of the dried crops and the temperature of the drying air were measured during the drying process. It was found that the values of convective heat transfer coefficient varied from crop to crop with a range 30.21406 and 20.65470 W/m{sup 2} C for the crops studied, and it was observed that the convective heat transfer coefficient increased in large amounts with the increase of the drying air velocity but increased in small amounts with the rise of the drying air temperature.

  18. Encapsulation of flaxseed oil using a benchtop spray dryer for legume protein-maltodextrin microcapsule preparation.

    Science.gov (United States)

    Can Karaca, Asli; Low, Nicholas; Nickerson, Michael

    2013-05-29

    Flaxseed oil was microencapsulated employing a wall material matrix of either chickpea (CPI) or lentil protein isolate (LPI) and maltodextrin using a benchtop spray dryer. Effects of emulsion formulation (oil, protein and maltodextrin levels) and protein source (CPI vs LPI) on the physicochemical characteristics, oxidative stability, and release properties of the resulting capsules were investigated. Microcapsule formulations containing higher oil levels (20% oil, 20% protein, 60% maltodextrin) were found to have higher surface oil and lower encapsulation efficiencies. Overall, LPI-maltodextrin capsules gave higher flaxseed oil encapsulation efficiencies (∼88.0%) relative to CPI-maltodextrin matrices (∼86.3%). However, both designs were found to provide encapsulated flaxseed oil protection against oxidation over a 25 d room temperature storage study relative to free oil. Overall, ∼37.6% of encapsulated flaxseed oil was released after 2 h under simulated gastric fluid, followed by the release of an additional ∼46.6% over a 3 h period under simulated intestinal fluid conditions.

  19. Controlling in situ crystallization of pharmaceutical particles within the spray dryer.

    Science.gov (United States)

    Woo, Meng Wai; Lee, May Ginn; Shakiba, Soroush; Mansouri, Shahnaz

    2016-12-20

    Simultaneous solidification and in situ crystallization (or partial crystallization) of droplets within the drying chamber are commonly encountered in the spray drying of pharmaceuticals. The crystallinity developed will determine the functionality of the powder and its stability during storage. This review discusses strategies that can be used to control the in situ crystallization process. Areas covered: The premise of the strategies discussed focuses on the manipulation of the droplet drying rate relative to the timescale of crystallization. This can be undertaken by the control of the spray drying operation, by the use of volatile materials and by the inclusion of additives. Several predictive approaches for in situ crystallization control and new spray dryer configuration strategies are further discussed. Expert opinion: Most reports, hitherto, have focused on the crystallinity of the spray dried material or the development of crystallinity during storage. More mechanistic understanding of the in situ crystallization process during spray drying is required to guide product formulation trials. The key challenge will be in adapting the mechanistic approach to the myriad possible formulations in the pharmaceutical industry.

  20. Modelling the Evaporation Rate in an Impingement Jet Dryer with Multiple Nozzles

    Directory of Open Access Journals (Sweden)

    Anna-Lena Ljung

    2017-01-01

    Full Text Available Impinging jets are often used in industry to dry, cool, or heat items. In this work, a two-dimensional Computational Fluid Dynamics model is created to model an impingement jet dryer with a total of 9 pairs of nozzles that dries sheets of metal. Different methods to model the evaporation rate are studied, as well as the influence of recirculating the outlet air. For the studied conditions, the simulations show that the difference in evaporation rate between single- and two-component treatment of moist air is only around 5%, hence indicating that drying can be predicted with a simplified model where vapor is included as a nonreacting scalar. Furthermore, the humidity of the inlet air, as determined from the degree of recirculating outlet air, has a strong effect on the water evaporation rate. Results show that the metal sheet is dry at the exit if 85% of the air is recirculated, while approximately only 60% of the water has evaporated at a recirculation of 92,5%.

  1. Effect of Selected Factors on Drying Process of Tomato in Forced Convection Solar Energy Dryer

    Directory of Open Access Journals (Sweden)

    U.S. Muhammed

    2012-09-01

    Full Text Available The effect of air velocity, slice thickness and grazing materials in drying process of tomato in forced convection solar energy dryer was evaluated. The result is to serve as an input for solar energy development for drying of vegetable and fruit products in North West Ecological zone of Nigeria. In order to evaluate the effects of the above factors in drying operation, a split-split-plot experimental design was used. Differences among the treatments and their interactions were tested with orthogonal contrast test to access their significance while further analysis were done to compare all possible pairs of treatment means using Duncan’s Multiple Range Test (DMRT. The results showed that there is no significant difference, at 95% probability level, between the means of the three glazing materials used. However, the variations in mean slice thickness and in mean air flow rate are highly significant at 99% probability level. The results further revealed that drying rate increasing with decrease in slice thickness and increase in air flow rate. Drying of 15, 20 and 25 mm slice thickness of tomato was achieved in time range of 21-24, 27-29 and 30-50 h, respectively.

  2. Investigation of drying kinetics of tomato slices dried by using a closed loop heat pump dryer

    Science.gov (United States)

    Coşkun, Salih; Doymaz, İbrahim; Tunçkal, Cüneyt; Erdoğan, Seçil

    2016-11-01

    In this study, tomato slices were dried at three different drying air temperatures (35, 40 and 45 °C) and at 1 m/s air velocities by using a closed loop heat pump dryer (HPD). To explain the drying characteristics of tomato slices, ten thin-layer drying models were applied. The drying of tomato slices at each temperature occurred in falling-rate period; no constant-rate period of drying was observed. The drying rate was significantly influenced by drying temperature. The effective moisture diffusivity varied between 8.28 × 10-11 and 1.41 × 10-10 m2/s, the activation energy was found to be 43.12 kJ/mol. Besides, at the end of drying process, the highest mean specific moisture extraction ratio and coefficient of performance of HPD system were obtained as 0.324 kg/kWh and 2.71, respectively, at the highest drying air temperature (45 °C).

  3. Investigation of drying kinetics of tomato slices dried by using a closed loop heat pump dryer

    Science.gov (United States)

    Coşkun, Salih; Doymaz, İbrahim; Tunçkal, Cüneyt; Erdoğan, Seçil

    2017-06-01

    In this study, tomato slices were dried at three different drying air temperatures (35, 40 and 45 °C) and at 1 m/s air velocities by using a closed loop heat pump dryer (HPD). To explain the drying characteristics of tomato slices, ten thin-layer drying models were applied. The drying of tomato slices at each temperature occurred in falling-rate period; no constant-rate period of drying was observed. The drying rate was significantly influenced by drying temperature. The effective moisture diffusivity varied between 8.28 × 10-11 and 1.41 × 10-10 m2/s, the activation energy was found to be 43.12 kJ/mol. Besides, at the end of drying process, the highest mean specific moisture extraction ratio and coefficient of performance of HPD system were obtained as 0.324 kg/kWh and 2.71, respectively, at the highest drying air temperature (45 °C).

  4. Thin layer modeling of tom yum herbs in vacuum heat pump dryer.

    Science.gov (United States)

    Artnaseaw, A; Theerakulpisut, S; Benjapiyaporn, C

    2010-04-01

    Thin layer vacuum heat pump drying experiments were conducted to determine drying models for Tom Yum herbs (chili, lemon grass, kaffir lime leaf and galangal slice). The drying experiments were conducted in a vacuum heat pump dryer at a constant drying pressure of 0.2 bars and drying temperatures ranging from 50 °C to 65 °C. The experimental results were fitted to a number of well-known thin layer drying models and it was found, for the range of drying temperature tested, that the Midilli model is the best model for all Tom Yum herbs. To account for the influence of drying temperature, the constants and coefficients of model were formulated as functions of the drying temperature. Statistical tests of agreement between the model and experimental results were performed by determining the coefficient of determination (R²) , reduced chi-square (χ²) and root mean square error (RMSE). It was found that the model is in very good agreement with the experimental results.

  5. Drying of oil palm frond particles in a fluidized bed dryer with inert medium

    Directory of Open Access Journals (Sweden)

    Yun May Tee

    2013-01-01

    Full Text Available Drying characteristic of oil palm frond fibres was investigated in a fluidized bed dryer with the presence of inert particles. Sand was used as inert material. Effects of air temperature (60, 70 and 80ºC, air velocity (0.79 and 0.85 m/s and mass ratio of fibres to sand (1:0, 1:1 and 1:2 on the drying curves were investigated. The results showed that the shortest drying time was obtained with the highest air temperature, air velocity and fibres to sand mass ratio. The experimental drying data were fitted to nine existing drying models namely Lewis, Page, Modified Page, Henderson and Pabis, Logarithmic, Two-term, Two-term exponential and Wang and Singh models and a proposed new model. The goodness-of-fit was determined based on the values of r2, c2 and RMSE. The results showed that the best quality of the fit was obtained using the proposed model. The new model was also validated for the superheated steam drying of oil palm empty fruit bunch from other work.

  6. Estudo de viabilidade da secagem da biomassa da banana verde em spray dryer rotativo

    Directory of Open Access Journals (Sweden)

    Ricardo Kenji Oi

    2010-01-01

    Full Text Available This paper presents a technical feasibility study for drying the biomass of green bananas at a pilot plant spray dryer with rotary atomizer. The biomass of the green banana is a component that can be used industrially in a wide variety of foods, with functional properties, especially the presence of resistant starch. The variables selected in the experimental procedure were the biomass concentration of green banana, feed flow rate and rotation of the atomizer. Responses were obtained as the mass and relative humidity of the dried product. Three levels were used in selected variables, which corresponded to the completion of 27 experiments. In experiments in which they obtained the lowest values of relative humidity, the amounts of mass were also the lowest, while in experiments where they met the higher amounts of the levels of relative humidity ranged from the highest. Considering the industrial application, whose purpose is the low humidity and increased production of the product, test 22 was the most appropriate, and found 11% moisture and 4.33 g in mass.

  7. Analysis of ginger drying inside a natural convection indirect solar dryer: An experimental study

    Directory of Open Access Journals (Sweden)

    S. K. Sansaniwal

    2015-12-01

    Full Text Available In this paper, a natural convection indirect solar cabinet dryer has been fabricated to study the drying behaviour of ginger rhizomes in terms of its convective heat transfer coefficient and moisture removing rate (% db. Various experiments were conducted during the months of March and April 2014 at Guru Jambheshwar University of Science and Technology, Hisar (29o5’5’’N, 75o45’55’’E, India. Experimental data obtained were used to evaluate the Nusselt number constants using linear regression method. Considering these constants, the average value of convective heat transfer coefficient was obtained and observed to decrease with increase in mass of ginger samples and progression of drying days with variation from 0.59 to 5.42 W/m2˚C for different mass of ginger samples. The moisture removing rate was reported to increase with increase in mass of ginger samples and decreases significantly with the progression of drying days. The average collector efficiency was also observed to vary from 14.97 to 16.14% under increasing and decreasing trends of solar radiations from morning to noon and noon to evening respectively. Modified page model was reported best for describing the drying behaviour of different mass of ginger samples. The experimental error in terms of percent uncertainty ranged from 29.19 to 46.25%.

  8. Prediction of Air Flow and Temperature Profiles Inside Convective Solar Dryer

    Directory of Open Access Journals (Sweden)

    Marian Vintilă

    2014-11-01

    Full Text Available Solar tray drying is an effective alternative for post-harvest processing of fruits and vegetables. Product quality and uniformity of the desired final moisture content are affected by the uneven air flow and temperature distribution inside the drying chamber. The purpose of this study is to numerically evaluate the operation parameters of a new indirect solar dryer having an appropriate design based on thermal uniformity inside the drying chamber, low construction costs and easy accessibility to resources needed for manufacture. The research was focused on both the investigation of different operation conditions and analysis of the influence of the damper position, which is incorporated into the chimney, on the internal cabinet temperature and air flow distribution. Numerical simulation was carried out with Comsol Multiphysics CFD commercial code using a reduced 2D domain model by neglecting any end effects from the side walls. The analysis of the coupled thermal-fluid model provided the velocity field, pressure distribution and temperature distribution in the solar collector and in the drying chamber when the damper was totally closed, half open and fully open and for different operation conditions. The predicted results were compared with measurements taken in-situ. With progressing computing power, it is conceivable that CFD will continue to provide explanations for more fluid flow, heat and mass transfer phenomena, leading to better equipment design and process control for the food industry.

  9. The effect of fan speed control system on the inlet air temperature uniformity in a solar dryer

    Directory of Open Access Journals (Sweden)

    S. F Mousavi

    2015-09-01

    Full Text Available Introduction: Drying process of agricultural products, fruits and vegetables are highly energy demanding and hence are the most expensive postharvest operation. Nowadays, the application of control systems in different area of science and engineering plays a key role and is considered as the important and inseparable parts of any industrial process. The review of literature indicates that enormous efforts have been donefor the intelligent control of solar driers and in this regard some simulation models are used through computer programming. However, because of the effect of air velocity on the inlet air temperature in dryers, efforts have been made to control the fan speed based ont he temperature of the absorber plate in this study, and the behavior of this system was compared with an ordinary dryer without such a control system. Materials and methods: In this study, acabinet type solar dryer with forced convection and 5kg capacity of fresh herbs was used. The dryer was equipped with a fan in the outlet chamber (the chimney for creating air flow through the dryer. For the purpose of research methods and automatic control of fan speed and for adjusting the temperature of the drying inlet air, a control system consisting of a series of temperature and humidity sensors and a microcontroller was designed. To evaluatethe effect of the system with fan speed control on the uniformity of air temperature in the drying chamber and hence the trend of drying process in the solar dryer, the dryer has been used with two different modes: with and without the control of fan speed, each in twodays (to minimize the errors of almost the same ambient temperature. The ambient air temperature during the four days of experiments was obtained from the regional Meteorological Office. Some fresh mint plants (Mentha longifolia directly harvested from the farm in the morning of the experiment days were used as the drying materials. Each experimental run continued for 9

  10. Explosion in a rotary dryer at a chemical factory. Eikoku kagaku koho no kaiten kansoki no bakuhatsu jiko (shiryo kenkazai no netsubunkai boso hanno)

    Energy Technology Data Exchange (ETDEWEB)

    Shioji, Y. (Nippon Oil Co. Ltd., Tokyo (Japan))

    1991-10-15

    This paper reports a dryer explosion and fire accident in the Dow Chemical {prime}s King {prime}s Lynn factory in Great Britain. Nine other accidents of dryers on the similar type are also reported to indicate the importance of advance evaluation on substances for their hazard. The subject accident occurred while a group leader was reporting a gushing sound and white smoke from the door of the dryer room at a little after 17:00 on June 27, 1976, an explosion bursted at 17:10 causing an immediate death of an operator due to a blast from the explosion. THE damage of the manufacturing equipment is estimated to have amounted to about 1.25 million pounds. The exolosion accident has occurred when the Zoalene (product name), a chicken feed additeve, has been left in a dryer in nearly a sealed condition for 27 hours after having been dried, its temperature was maintained at 120-130 {degree}C as a result of heat insulating effect of the insulators on the dryer. This caused a pyrolysis of the product, of which heat accelerated the pyrolysisand led to an explosion. One of the basic causes was that no safety evaluation technique has been established to predict danger of the drying operation. 2 refs., 5 figs.

  11. Performance Evaluation of a Solar Dryer with Finny, Perforated Absorber Plate Collector Equipped with an Air Temperature Control System for Dill Drying

    Directory of Open Access Journals (Sweden)

    M Razmipour

    2015-03-01

    Full Text Available Dill is one of the most important plants in the world because of its medicinal properties and it is widely used as a vegetable in the most parts of Iran. In the present study a new solar dryer with finny, perforated absorber plate collector was utilized to dry fresh dill. The dryer was comprised of a solar collector, a product container, a fan and a drying air temperature controller. The temperature controller was used as a control system to regulate the drying air temperature. Thermal performance of the dryer with finny, perforated solar collector was compared with that of a simple flat plate solar collector at different airflow rates. The effect of drying air temperature at three levels (45, 55 and 65 °C, the product size at three lengths (3, 5 and 7 cm and two different modes of drying (mixed and indirect on the dryer performance was investigated. The results showed that the finny, perforated absorber plate solar collector could improve the thermal efficiency about 11% in comparison with the flat plate collector and the highest thermal efficiency was achieved at the maximum airflow rate. Meanwhile, increasing the air temperature and decreasing the product size caused a significant reduction in energy consumption. Solar fraction reduced by increasing the air temperature. Finally a maximum dryer efficiency of 70% was observed at air temperature of 65 oC, product size of 3 cm with mixed mode drying.

  12. Mass transfer characteristics of eggplant slices during length of continuous band dryer

    Science.gov (United States)

    Kaveh, Mohammad; Amiri Chayjan, Reza; Nikbakht, Ali Mohammad

    2016-12-01

    This study presents a mathematical modeling of eggplant slice drying process in a continuous band dryer. The experiments for drying of eggplant slices were conducted at three air temperature levels of 45, 60, and 75 °C, inlet air velocities of 1, 1.5, and 2 m/s, and belt linear speeds of 2.5, 6.5, and 10.5 mm/s. To estimate the drying kinetics of eggplant slices, different mathematical models were utilized to fit the empirical data of thin layer drying. The models were compared based on their coefficients of determination (R 2), reduced Chi squares (χ 2) and root mean square errors (RMSE) between the experimental and predicted moisture ratios (MR). A feed and cascade forward with back-propagation algorithm was employed to predict the moisture ratio (MR) and drying rate (DR). The effective moisture diffusivity varied from 3.40 × 10-9 to 1.13 × 10-8 m2/s. The activation energy varied from 14.18 to 25.09 kJ/mol. The obtained results show that the feed forward back-propagation network with training algorithm of Levenberg-Marquardt, 4-5-5-2 topology, threshold functions of tansig-tansig-tansig can able to predict the moisture content and drying rate with R2 values of 0.9992 and 0.9726, respectively. Comparison of ANN results with mathematical models revealed that mathematical modeling yields better accuracy to predict the moisture content and drying rate of eggplant.

  13. Studi Eksperimen Karakteristik Pengeringan Batubara Dengan Variasi Beban Pengeringan Pada Cyclone Coal Dryer

    Directory of Open Access Journals (Sweden)

    Adi Krisnawan

    2013-09-01

    Full Text Available Batubara merupakan salah satu sumber bahan bakar yang digunakan pada Pembangkit Listrik Tenaga Uap. Agar didapatkan efisiensi yang tinggi pada PLTU maka batubara harus memiliki nilai kalor  tinggi. Indonesia sendiri merupakan salah satu negara penghasil batubara terbersa didunia. Namun hampir 80% batubara yang dihasilkan tergolong batubara rendah dan sedang. Untuk meningkatkan nilai kalor atas batubara perlu dilakukan pengeringan untuk mengurangi kadar air dalam batubara. Eksperimen dilakukan menggunakan batubara dengan moisture conten awal 25%. Batubara dikeringkan dalam chamber cyclone coal dryer dengan kecepatan udara dan temperature udara panas 550C. Pengambilan data dilakukan setiap 5 menit sekali dengan pengambilan sampel batubara selama 30 menit proses pengeringan. Untuk 5 menit pertama interval waktu pengambilan dilakukan selama 1 menit. Data yang diperoleh berupa relative humidity udara, temperatur, berat basah dan berat kering. Pengambilan data berat sampel kering dilakukan berdasarkan standart ASTM D5142 dengan pengeringan pada temperatur 1050C selama 3 jam. Percobaan dilakukan dengan variasi beban pengeringan 300gr,600gr,900gr. Dari hasil eksperimen diketahui bahwa pada 5 menit pertama proses pengeringan batubara memiliki drying rate paling cepat hal ini ditandai dengan penurunan moisture conten yang tajam.Temperatur udara outlet chamber untuk beban 900gr memiliki nilai paling rendah dibandingkan beban pengeringan yang lain yaitu 39.90C. Hal ini dikarenakan massa air pada beban 900 gr lebih banyak sehingga udara pengering mengalami proses pendinginan paling besar. Pada 5 menit pertama terjadi perubahan relative humidity terbesar untuk masing masing beban pengeringan, dimana untuk beban pengeringan 900 gr memiliki nilai relatie humidity terbesar pada menit pertama yaitu 35.47 %. Kenaikan Relative humidity ini dikarenakan massa air yang diilepaskan beban 900gr lebih banyak dari beban 600 gr dan 300 gr.

  14. Mass transfer characteristics of eggplant slices during length of continuous band dryer

    Science.gov (United States)

    Kaveh, Mohammad; Amiri Chayjan, Reza; Nikbakht, Ali Mohammad

    2017-06-01

    This study presents a mathematical modeling of eggplant slice drying process in a continuous band dryer. The experiments for drying of eggplant slices were conducted at three air temperature levels of 45, 60, and 75 °C, inlet air velocities of 1, 1.5, and 2 m/s, and belt linear speeds of 2.5, 6.5, and 10.5 mm/s. To estimate the drying kinetics of eggplant slices, different mathematical models were utilized to fit the empirical data of thin layer drying. The models were compared based on their coefficients of determination ( R 2), reduced Chi squares ( χ 2) and root mean square errors ( RMSE) between the experimental and predicted moisture ratios ( MR). A feed and cascade forward with back-propagation algorithm was employed to predict the moisture ratio ( MR) and drying rate ( DR). The effective moisture diffusivity varied from 3.40 × 10-9 to 1.13 × 10-8 m2/s. The activation energy varied from 14.18 to 25.09 kJ/mol. The obtained results show that the feed forward back-propagation network with training algorithm of Levenberg-Marquardt, 4-5-5-2 topology, threshold functions of tansig-tansig-tansig can able to predict the moisture content and drying rate with R2 values of 0.9992 and 0.9726, respectively. Comparison of ANN results with mathematical models revealed that mathematical modeling yields better accuracy to predict the moisture content and drying rate of eggplant.

  15. Energy analyses and drying kinetics of chamomile leaves in microwave-convective dryer

    Directory of Open Access Journals (Sweden)

    Ali Motevali

    2016-06-01

    Full Text Available Drying characteristics and energy aspects as well as mathematical modeling of thin layer drying kinetics of chamomile in a microwave-convective dryer are reported in this article. Drying experiments were carried out at 8 microwave power levels (200–900 W, air temperature of 50 °C, and air velocity of 0.5 m/s. Increasing the microwave output power from 200 to 900 W, decreased the drying time from 40 to 10 min. The drying process took place in the falling rate period. The Midilli et al. model showed the best fit to the experimental drying data. Moisture diffusivity values increase with decreasing moisture content down to 1.70 (kg water kg−1 dry matter but decrease with a further decrease in moisture content from 1.72 to 0.96 (kg water kg−1 dry matter. The average values of Deff increased with microwave power from 5.46 to 39.63 × 10−8 (m2 s−1. Energy consumption increased and energy efficiency decreased with moisture content of chamomile samples. Average specific energy consumption, energy efficiency and energy loss varied in the range 18.93–28.15 MJ kg−1 water, 8.25–13.07% and 16.79–26.01 MJ kg−1 water, respectively, while the best energy results were obtained at 400 W, 50 °C and 0.5 m s−1.

  16. Micro-Sized Particle Production of Momordicas sp Extract Using Spray Dryer

    Directory of Open Access Journals (Sweden)

    Maizirwan Mel

    2011-12-01

    Full Text Available Spray drying is the most widely used industrial process involving particle formation and drying. It is highly suited for the continuous production of dry solids in either powder, granulate or agglomerate form from liquid feed-stocks as solutions, emulsions and pump able suspensions. Therefore, spray drying is an ideal process where the end-product must comply with precise quality standards regarding particle size distribution, residual moisture content, bulk density, and particle shape. In this study, Momordica sp extract product has been successfully spray dried into micro scale of powder particle and will be used as plant-based insulin. The process optimized using Taguchi method with four factors and three levels has given a good quality of the product. The average of particle size was obtained at about 11 microns.ABSTRAK: Kering sembur digunakan secara meluas dalam proses industri yang melibatkan pembentukan zarah dan pengeringan. Ia amat sesuai dalam penghasilan pepejal kering secara beterusan dalam bentuk serbuk, butiran atau gumpalan daripada simpanan suapan bendalir sebagai larutan, emulsi dan ampaian boleh dipam. Maka, kering sembur adalah proses yang ideal apabila hasil akhir harus mematuhi piawaian kualiti yang tepat berkaitan dengan pengagihan saiz zarah, kandungan kelengsaan sisa, ketumpatan pukal dan bentuk zarah. Dalam kajian ini, produk ekstrak Momordica sp (dikenali juga sebagai peria katak telah berjaya dikering sembur menjadi serbuk zarah berskala mikro dan akan digunakan sebagai insulin berasaskan tumbuhan. Proses ini dioptimumkan dengan pengunaan kaedah Taguchi empat faktor dan tiga peringkat, agar memberikan hasil produk yang berkualiti. Kadar purata saiz zarah yang terhasil adalah lebih kurang 11 mikron.KEY WORDS: micro-sized, particle, Momordica sp, spray dryer.

  17. COMAS烘丝机整体改造与应用%Rebuilding of COMAS Cut Tobacco Dryer

    Institute of Scientific and Technical Information of China (English)

    徐伟民; 刘剑敏; 舒梦; 徐荣华

    2011-01-01

    浙江中烟工业有限责任公司下设两个生产基地,分别配备COMAS逆流式烘丝机和HAUNI顺流式烘丝机.为了克服烘丝机设备和叶丝干燥工艺差异、统一制丝生产工艺、实现不同产地产品的同质化,在对比分析了两种烘丝机工作原理和控制方式的基础上,对COMAS烘丝机进行了整体改造.内容包括:热风流向变为顺流式;风机增加变频调速功能,调节热风流量,减少能源消耗;采用HAUNI方式的热风温度与筒壁温度控制方式;在出料端安装负压传感器保持烘丝机进出风量平衡.改造后的COMAS烘丝机的热风流向、控制方式趋近于HAUNI顺流式烘丝机,各项工艺和物理指标均达到或优于改造前水平,烘丝冷却后含水率控制稳定,含水率偏差控制在0.18%以内,有效控制了干头干尾烟丝量,且减少了蒸汽消耗.%COMAS counter current cut tobacco dryer and HAUNI cocurrent cut tobacco dryer were separately used in two manufacturing facilities of China Tobacco Zhejiang Industrial Limited Corporation.In order to unify processing technology and quality of products, the working principles and control systems of the two dryers were compared and COMAS dryer was rebuilt as following; changing hot-air direction from counter current into cocurrent; adding a frequency conversion speed regulator to hot-air fan motor to adjust air volume and reduce energy consumption; the temperatures of hot-air and cylinder wall being controlled in the same way as that in HAUNI dryer; installing negative pressure sensor at output end to balance the input and output air flow.The rebuilt COMAS dryer showed better performance.The moisture content in dried cut tobacco after cooling was stable, and its deviation was under 0.18%.In addition, the amount of over-dried cut tobacco during start and finish of drying operation was effectively controlled and steam consumption was also reduced.

  18. Energy aAnalysis and Kinetics of Mint Leaves Dehydration Using Vibro-Fluidized Bed Heat Pump Dryer

    Directory of Open Access Journals (Sweden)

    S. M Ataei Ardestani

    2015-03-01

    Full Text Available Fluidized bed dryers have not yet been used for drying products such as mint leaves. This could be due to high porosity and low mechanical resistance resulting in poor quality of fluidization. Applying vibration has been recommended to overcome problems such as channeling and defluidization, and hence improving the fluidization quality. In this research, a laboratory scale vibro-fluidized bed heat pump dryer was designed and constructed for drying mint leaves. The experiments were conducted at vibration frequency of 80 Hz and amplitude of 3 mm. The velocity and temperature of the inlet air was controlled by an automatic control system. Experiments were carried out at 40, 50 and 60 °C, and two methods: heat pump drying (HPD and non-heat pump drying (NHPD. The results revealed that drying process primarily occurred in the falling rate period. Effective moisture diffusivity of the samples increased with increase in drying air temperature and varied from 4.26656×10-11 to 2.95872×10-10 m2 s-1 for the HPD method, and 3.71918×10-11 to 1.29196×10-10 m2 s-1 for the NHPD method and was within the reported range of 10-9 to 10-11 m2 s-1 for drying of food materials. The activation energy was determined to be 84 kJ mol-1 for the HPD and 54.34 kJ mol-1 for the NHPD, both have very good agreement with the results of other investigators. The coefficient of performance and specific moisture evaporation rate showed the acceptable performance of the heat pump system. Moreover, the energy consumption of the dryer for the NHPD method was more than the HPD method.

  19. Performance Analysis of Solar Assisted Fluidized Bed Dryer Integrated Biomass Furnace with and without Heat Pump for Drying of Paddy

    Directory of Open Access Journals (Sweden)

    M. Yahya

    2016-01-01

    Full Text Available The performances of a solar assisted fluidized bed dryer integrated biomass furnace (SA-FBDIBF and a solar assisted heat pump fluidized bed dryer integrated biomass furnace (SAHP-FBDIBF for drying of paddy have been evaluated, and also drying kinetics of paddy were determined. The SA-FBDIBF and the SAHP-FBDIBF were used to dry paddy from 11 kg with moisture content of 32.85% db to moisture content of 16.29% db (14% wb under an air mass flow rate of 0.1037 kg/s within 29.73 minutes and 22.95 minutes, with average temperatures and relative humidities of 80.3°C and 80.9°C and 12.28% and 8.14%, respectively. The average drying rate, specific energy consumption, and specific moisture extraction rate were 0.043 kg/minute and 0.050 kg/minute, 5.454 kWh/kg and 4.763 kWh/kg, and 0.204 kg/kWh and 0.241 kg/kWh for SA-FBDIBF and SAHP-FBDIBF, respectively. In SA-FBDIBF and SAHP-FBDIBF, the dryer thermal efficiencies were average values of 12.28% and 15.44%; in addition, the pickup efficiencies were 33.55% and 43.84% on average, whereas the average solar and biomass fractions were 10.9% and 10.6% and 36.6% and 30.4% for SA-FBDIBF and SAHP-FBDIBF, respectively. The drying of paddy occurred in the falling rate period. The experimental dimensionless moisture content data were fitted to three mathematical models. Page’s model was found best to describe the drying behaviour of paddy.

  20. Design and Performance Evaluation of a Solar Assisted Heat Pump Dryer Integrated with Biomass Furnace for Red Chilli

    OpenAIRE

    M. Yahya

    2016-01-01

    The performance of a solar assisted heat pump dryer integrated with biomass furnace has been designed and evaluated for drying red chillies, and drying kinetics of red chillies were evaluated. The red chillies were dried from 22 kg with moisture content of 4.26 db to moisture content of 0.08 db which needed 11 hours, with the average drying chamber temperature, drying chamber relative humidity, and an air mass flow rate of 70.5°C, 10.1%, and 0.124 kg/s, respectively, while the open sun drying...

  1. Design and Application of a Novel Dehumidifying System for a Fluidized Bed Dryer for the Drying of Canola Seeds

    Directory of Open Access Journals (Sweden)

    Narjes Malekjani

    2011-01-01

    Full Text Available A novel fluidized bed dryer equipped with a dehumidifying system was designed and constructed. The dehumidifying system was based on refrigeration cycle and composed of an evaporator, a compressor, a condenser an expansion valve and a damper. The drying experiments were carried out in three temperature (35, 45 and 55°C and three relative humidity (30, 50 and 70% levels. The results showed that the relative humidity of drying air has a significant effect on drying rate. The drying rates decreased as relative humidity increased at a constant temperature, and increased as temperature increased at a constant relative humidity so dehumidifying can accelerate drying and decrease drying times.

  2. Commercial Demonstration of the Manufactured Aggregate Processing Technology Utilizing Spray Dryer Ash

    Energy Technology Data Exchange (ETDEWEB)

    Milton Wu; Paul Yuran

    2006-12-31

    Universal Aggregates LLC (UA) was awarded a cost sharing Co-operative Agreement from the Department of Energy (DOE) through the Power Plant Improvement Initiative Program (PPII) to design, construct and operate a lightweight aggregate manufacturing plant at the Birchwood Power Facility in King George, Virginia in October 2001. The Agreement was signed in November 2002. The installation and start-up expenses for the Birchwood Aggregate Facility are $19.5 million. The DOE share is $7.2 million (37%) and the UA share is $12.3 million (63%). The original project team consists of UA, SynAggs, LLC, CONSOL Energy Inc. and P. J. Dick, Inc. Using 115,000 ton per year of spray dryer ash (SDA), a dry FGD by-product from the power station, UA will produce 167,000 tons of manufactured lightweight aggregate for use in production of concrete masonry units (CMU). Manufacturing aggregate from FGD by-products can provide an economical high-volume use and substantially expand market for FGD by-products. Most of the FGD by-products are currently disposed of in landfills. Construction of the Birchwood Aggregate Facility was completed in March 2004. Operation startup was begun in April 2004. Plant Integration was initiated in December 2004. Integration includes mixing, extrusion, curing, crushing and screening. Lightweight aggregates with proper size gradation and bulk density were produced from the manufacturing aggregate plant and loaded on a stockpile for shipment. The shipped aggregates were used in a commercial block plant for CMU production. However, most of the production was made at low capacity factors and for a relatively short time in 2005. Several areas were identified as important factors to improve plant capacity and availability. Equipment and process control modifications and curing vessel clean up were made to improve plant operation in the first half of 2006. About 3,000 tons of crushed aggregate was produced in August 2006. UA is continuing to work to improve plant

  3. Nanoparticle formulation by Büchi B-90 Nano Spray Dryer for oral mucoadhesion

    Directory of Open Access Journals (Sweden)

    Harsha SN

    2015-01-01

    temperature. The amount of vildagliptin retained was 1.6% within 3 hours, and in comparison with the gelatin vildagliptin nanoparticles formulation, the percentage that was retained was much higher (98.2% in 12 hours. Keywords: nanospheres, vildagliptin, Büchi Nano Spray Dryer, diabetes

  4. Characterization and drying of caja bagasse (Spondias mombin L. in a tray dryer using a factorial planning

    Directory of Open Access Journals (Sweden)

    Andréia Souto da Silva

    2012-03-01

    Full Text Available The caja (Spondias mombin L. is used in the manufacture of ice-cream, jams, pulps, beverages being also consumed in natura. One of the most important procedures in food conservation is drying, considering that most fresh fruits contain approximately 80% of water. Food drying is used to obtain two basic aspects: (1 the economic factor; in the shipping and handling of the product; (2 at the manipulation; once dried and grinded, the material is rehydrated, at desirable levels, to formulate a new product as in ice cream, jams, yoghurts and drinks and may also be added to pasta, biscuits and other industrialized products. The aim of this study was to investigate the kinetics of caja bagasse drying in a fixed-bed tray dryer, using central composite factorial planning. The following factors were evaluated: temperature (55, 65 and 75 ºC, dryer inlet air velocity (3.2, 4.6 and 6.0 m.s-1 and cake thickness (0.8, 1.2 and 1.6 cm where the response of the considered variable was caja bagasse moisture content (b.s. and the results showed that the main effects and their interactions were significant at a 95% confidence level being the best condition obtained at temperature of 75 ºC, velocity of 6.0 m.s-1 and cake thickness of 0.8 cm.

  5. Reduction of Blister Formation Time in Suction Blister Epidermal Grafting in Vitiligo Patients Using a Household Hair Dryer.

    Science.gov (United States)

    Arora, Shweta; Kar, Bikash Ranjan

    2016-01-01

    Suction blister epidermal grafting (SBEG) is a simple and effective way of surgical repigmentation in vitiligo. The major problem faced is the time taken for the formation of blisters. Temperature at the suction site is one of the factors affecting the blister formation time. To reduce the blister formation time in SBEG by increasing the surface temperature to 44°C. This is a left-right comparison study. Total seven patients with lip vitiligo involving both the angles of lips were enrolled. Suction syringes were applied on both the thighs of all the patients. On the right thigh, blisters were raised as per the procedure standardised by Gupta et al. On the left thigh, similar procedure was used, but a hair dryer was used additionally to increase the surface temperature of the skin to 44°C. The time taken for the formation of well-formed, dome-shaped, unilocular blister was noted. The mean time taken for the formation of blister on the right thigh was 121.1 ± 6.2 min and on the left thigh was 69.6 ± 5.4 min. All the seven patients were started on PUVASOL after SBEG. There was complete repigmentation of the grafted sites in all the patients after 2 months. Hair dryer is easily available, affordable and simple to use and the time saved during the procedure is quite significant.

  6. Behavior of a portable solar dryer for pineapple fiber Comportamento de um secador solar para fibras de abacaxi

    Directory of Open Access Journals (Sweden)

    Róger Moya

    2012-12-01

    Full Text Available In Costa Rica, there has been a growing interest to use pineapple fiber from plant, for which current processes need to be improved or new processes need to be developed, with emphasis on drying methods. This work presents the design and evaluation of the behavior of a prototype portable solar dryer in four sites of Costa Rica. The design describes the main parts of the dryer, as well as how they were constructed. The behavior was evaluated according to temperature and relative humidity inside e outside the chamber, and the influence of direct and indirect solar radiation. In order to achieve improved dryer efficiency, a dehumidifier was used to control relative humidity, and a heating system was implemented during the hours of low temperature, low solar radiation and high relative humidity. Based on drying time, final moisture content of fibers of pineapple leaves from plant, and the varying hours when fibers were put to dry, the evaluation of the dryer revealed that the best fiber-drying interval is from 6h00 to 14h00, and after that, it is convenient to inject hot air and use a dehumidifier in the dryer in order to increase its efficiency.Na Costa Rica, o interesse pelo uso da fibra proveniente da folha de abacaxizeiro. Tem almentado e essa atividade precisa de melhoramento ou implementação de novos processos para alcançar maior eficiência, principalmente na secagem da fibra. O presente trabalho apresenta o design e comportamento de uma protótipo portátil de secadora solar em 4 sites geográficos da Costa Rica. Estão descritas as principais partes do secador, bem como a metodologia de construção. O comportamento foi avaliado de acordo com a temperatura e umidade relativa interna e externa da câmara e a influencia da radiação direta e indireta. Com a finalidade de melhorar a eficiência da secadora, foi usado um desumidificador para controlar a umidade relativa e ainda um sistema de aquecimento durante as horas de baixa temperatura

  7. Technology and Equipment of Waste Heat Recovery in Dryer Section of Paper Machine%纸机干燥部余热回收技术与设备

    Institute of Scientific and Technical Information of China (English)

    张秀文

    2012-01-01

    Some waste heat recovery technology and equipment used in dryer section of paper machine at home and abroad were introduced in this paper.%介绍一些国际、国内余热回收技术和设备,供同行分析、研究和借鉴.

  8. Biomass equipments. Dryers. Drying, crushing, agglomeration of agro-industrial products; Materiels pour la biomasse. Les secheurs, sechage, broyage, agglomeration de produits agro-industriels

    Energy Technology Data Exchange (ETDEWEB)

    Deur, O. [Promill (France)

    1997-12-31

    This paper describes the French Promill Company activity in the design and manufacturing of complete drying-crushing-agglomerating units for agro-industrial products (pulp of beet, lucerne, etc..). The paper focusses on the thermal and mechanical efficiency of the high temperature dryer and on the pulp granulating squeezer. (J.S.)

  9. Alterations in fruit and vegetable beta-carotene and vitamin C content caused by open-sun drying, visqueen-covered and polyethylene-covered solar-dryers.

    Science.gov (United States)

    Ndawula, J; Kabasa, J D; Byaruhanga, Y B

    2004-08-01

    This study investigated the effects of three drying methods (open sun drying, visqueen-covered solar dryer and polyethylene-covered solar dryer) on b-carotene and vitamin C content of edible portions of mango fruit (Mangifera indica) and cowpea leaves (Vigna unguiculata). Commercial samples were analysed for vitamin C by titrimetry and b-carotene by spectrophotometry at 450 nm. Differences in vitamin retention and loss associated with the three drying methods were assessed by analysis of variance and least significant difference (LSD) at (pdrying. Open sun drying method caused the greatest b-carotene and vitamin C loss (58% and 84% respectively), while the visqueen-covered solar dryer caused the least loss (34.5% and 71% respectively). Blanching cowpea leaves improved b-carotene and vitamin C retention by 15% and 7.5% respectively. The b-carotene and vitamin C content of fresh ripe mango fruit was 5.9 and 164.3 mg/100g DM respectively. Similar to effects on cowpea leaves, the mango micronutrient content decreased (pdrying. The open sun drying method caused the greatest b-carotene (94.2%) and vitamin C (84.5%) loss, while the visqueen-covered solar dryer caused the least (73 and 53% respectively). These results show that the three solar drying methods cause significant loss of pro-vitamin A and vitamin C in dried fruits and vegetables. However, open sun drying causes the most loss and the visqueen-covered solar dryer the least, making the later a probable better drying technology for fruit and vegetable preservation. The drying technologies should be improved to enhance vitamin retention.

  10. Analysis of Energy Consumption of "Compression Heat" Pressure Heat Dryer%“压缩热”干燥机能耗分析

    Institute of Scientific and Technical Information of China (English)

    李申

    2015-01-01

    作为典型的热质交换设备,吸附干燥器再生能量是被吸水量锁定的。总耗能受到吸附剂本身物理性质的制约,可用“质量守恒”与“能量守恒”两大定律来解释其能耗过程。各类吸附干燥器能耗量都要通过“能量衡算”来确定。“压缩热”干燥器与其他一切加热干燥器一样采取了“长周期”工作循环制,解吸环节无效热损很大。无热再生干燥器则采用了“短周期”工作制,为实际耗气量减少留有了较大的空间。%As the typical heat and mass transfer equipment, the energy of regenerative desiccant dryers is limited by water absorption. The total energy consumption is restricted by the physical properties of the adsorbent, which can be explained through two laws of conservation of mass and energy conservation. The energy consumption in each absorption dryers should be determined by“energy balance”.“Compression heat”dryer adopts“long-period”working cycle system as other heating dryers, in which invalid heat losses are great in desorption process. However, regenerated dryer without heat adopts“short-period”working cycle system, which provides greater space for actual gas consumption reduction.

  11. A mathematical model and simulation of the drying process of thin layers of potatoes in a conveyor-belt dryer

    Directory of Open Access Journals (Sweden)

    Salemović Duško R.

    2015-01-01

    Full Text Available This paper presents a mathematical model and numerical analysis of the convective drying process of small particles of potatoes slowly moving through the flow of a drying agent - hot moist air. The drying process was analyzed in the form of a one-dimensional thin layer. The mathematical model of the drying process is a system of two ordinary nonlinear differential equations with constant coefficients and an equation with a transcendent character. The appropriate boundary conditions of the mathematical model were given. The presented model is suitable in the automated control. The presented system of differential equations was solved numerically. The analysis presented here and the obtained results could be useful in predicting the drying kinetics of potatoes and similar natural products in a conveyor-belt dryer. [Projekat Ministarstva nauke Republike, br. TR-33049, br. TR-37002 i br. TR-37008

  12. Experimental investigation on the comparison of fenugreek drying in an indirect solar dryer and under open sun

    Science.gov (United States)

    Shrivastava, Vipin; Kumar, Anil

    2016-09-01

    The convective heat transfer coefficient is an essential parameter for designing of any solar drying system. In this paper heat transfer modeling in term of convective heat transfer coefficient is performed and compared with open sun drying. The data obtained from experimentation under open sun and indirect solar drying conditions have been used to find values of the experimental constant `C' and exponent `n' by regression analysis and, consequently, convective heat transfer coefficient. From this study it is concluded that the convective heat transfer coefficient is decreasing with drying time it is due to decrease in moisture content. Results also showed that convective heat transfer coefficients are more in indirect solar dryer system than under open sun drying.

  13. Analysis and experimental study of rotatory Amaranth dryer prototype based on solar thermal energy; Analisis y estudio experimental de una secadora rotativa para granos de amaranto con aprovechamiento termico de la energia solar

    Energy Technology Data Exchange (ETDEWEB)

    Lema, A. I.; Adoro, J. A.; Fasulo, A. J.; Lara, M. A.

    2004-07-01

    The performance of a rotary Amaranth dryer prototype based on solar thermal energy is analysed in this work. Many experiments were made on this prototype in order to analyse the Amaranth seed behaviour under different drying conditions. By means of mass and energy balances, models were developed, which allow to evaluate the performance and efficiency of the rotary dryer. The thermal energy used in the drying process is provided by an air solar collector made of polyethylene and wood. The solar collector design is optimised in order to satisfy the heating requirements of the dryer, running simulations with a computational model previously developed. (Author)

  14. Optimization of the drying parameters for the short-form spray dryer producing powdered egg with 20% tapioca starch additive

    Directory of Open Access Journals (Sweden)

    Joanna Tess Masilungan-Manuel

    2015-09-01

    Full Text Available Spray drying is one of the common methods of preserving eggs. A study had shown that addition of 20% tapioca starch to liquid egg prior to drying increases the shelf-life of the powdered product. However, although the said factor has been identified, production in a larger capacity is still a problem. One way to solve this predicament is to identify the optimum drying parameter that would produce a higher yield of dried eggs but retain the quality of the desired product such as the moisture content and water activity. The key issue in optimizing the dryer operation is flow stability wherein the airflow patterns, such as velocity, temperature, and relative humidity, existing inside the drying chamber are considered as the primary factor that influences the histories of the droplets produced. In this article, the author used ANSYS-Fluent version 14.5, a computational fluid dynamics software, to analyze the flow pattern of the continuous phase and to track the particle histories of the disperse phase inside the short-form drying chamber that produces powdered egg with 20% tapioca starch additive. Simulations for the short-form dryer showed that the optimized inlet air temperature and outlet particle temperature were 438 and 385 K, respectively. Based on the results, the calculated moisture content and water activity are 4.55% and 0.02 a w , respectively. Note that the critical moisture content and water activity for powdered eggs are 5% and 0.4 a w , respectively. The values beyond these limits will cause abrupt spoilage of the dried egg.

  15. 直接加热式生物质回转干燥过程模拟%SIMULATION OF BIOMASS DRYING IN A DIRECT CONTACT ROTARY DRYER

    Institute of Scientific and Technical Information of China (English)

    奚英涛; 由长福

    2013-01-01

    通过分析回转干燥器内传热传质规律,建立生物质回转干燥过程的一维数学模型.利用基于随机颗粒轨道模型的物料体积流率公式计算干燥器内各传热面积大小,从而实现模型的求解.采用此模型预测物料温度、含水率及空气温度、湿度等在干燥器内部的轴向分布,计算结果与文献实验数据的对比结果表明该模型可用于实际生物质回转干燥过程的分析.干燥计算结果表明:物料在干燥器入口段干燥速率最大,直至物料含水率达到临界含水率后逐渐减小,物料中水分的蒸发主要发生在干燥器的前端.因此,要提高生物质物料的干燥程度,最直接有效的方法是提高物料入口段的干燥速率,可通过提高干燥空气入口温度等手段实现.%Heat and mass transfer process in a direct contact rotary dryer was analyzed, and a one-dimensional axial mathematical model of direct contact rotary drying of biomass was developed. The heat transfer areas in the rotary dryer was obtained through a formula of material volumetric flow based on a novel particulate trajectory model, thus the simulation of biomass drying in a direct contact rotary dryer was carried out. The model was used to predict the axial distribution of temperature and moisture of air and biomass in the dryer. The comparison of the simulation results and the experimental measurements showed that the model is suitable for analysis of process of biomass drying. It was shown that the drying rate of biomass is highest at the beginning of the dryer and doesn' t decrease until at the critical moisture content. Most moisture is evaporated at the beginning of the dryer. Therefore, in order to make the biomass drier, the most effective method is to improve the drying rate at the inlet section. This can be realized by increasing the temperature of inlet drying air.

  16. Use of biogas for cogeneration of heat and electricity for local application: performance evaluation of an engine power generator and a sludge thermal dryer.

    Science.gov (United States)

    Lobato, L C S; Chernicharo, C A L; Pujatti, F J P; Martins, O M; Melo, G C B; Recio, A A R

    2013-01-01

    A small unit of cogeneration of energy and heat was tested at the Centre for Research and Training on Sanitation UFMG/COPASA - CePTS, located at the Arrudas Sewage Treatment Plant, in Belo Horizonte, Minas Gerais, Brazil. The unit consisted of an engine power generator adapted to run on biogas, a thermal dryer prototype and other peripherals (compressor, biogas storage tank, air blower, etc.). The heat from engine power generator exhaust gases was directed towards the thermal dryer prototype to dry the sludge and disinfect it. The results showed that the experimental apparatus is self-sufficient in electricity, even producing a surplus, available for other uses. The tests of drying and disinfection of sludge lasted 7 h, leading to an increase in solids content from 4 to 8% (50% reduction in sludge volume). Although the drying of sludge was not possible (only thickening was achieved), the disinfection process proved very effective, enabling the complete inactivation of helminth eggs.

  17. Kneader/dryer for sludges of distillation wastes; Secador-amasador para lodos de la clarificacion, lodos de barnices y residuos de la destilacion

    Energy Technology Data Exchange (ETDEWEB)

    Schwenk, W.

    2001-07-01

    The evaporation and indirect drying of industrial and biological sludges requires equipment of heavy mechanical design that is capable to cope with sticky, pasty matter. LIST-DISCOTHERM B y LIST-ORP kneaders/dryers of closed design are able to dry difficult sludges in a single-step continuous operation without recycling of dry product. Drying of sewage sludge, paint sludges and other process wastes including solvent recovery is an important step for an ecologically safe processing of these residuals. (Author)

  18. Influência da hidrociclonagem e da secagem por spray dryer nas propriedades reológicas de argilas bentoníticas

    Directory of Open Access Journals (Sweden)

    V. C. Marques

    2015-09-01

    Full Text Available ResumoA exploração desordenada ao longo dos anos das argilas bentoníticas do município de Boa Vista, PB, resultou no esgotamento das variedades nobres. Assim, o que existe atualmente são bentonitas com elevado percentual de minerais acessórios, elementos contaminantes a exemplo do quartzo, os quais influem negativamente nas propriedades reológicas das dispersões. O presente trabalho propõe concentrar dispersões dessas argilas pouco nobres pela operação de hidrociclonagem e posterior secagem por spray dryer, visando à obtenção de amostras com valores de reologia de acordo com norma EP-1EP-00011-A da Petrobrás. Assim, preparou-se dispersões de três composições com as argilas Bofe, Chocolate, Verde-Lodo, Chocobofe e Sortida previamente selecionadas por planejamento experimental com concentrações de 4% em massa de argila para serem concentradas por hidrociclonagem. Os concentrados foram secos por spray dryer em duas condições de secagem. Os resultados evidenciaram a eficiência das operações de hidrociclonagem e secagem por spray dryer das misturas com notável melhoria nas propriedades reológicas.

  19. Closed Loop Waste Processing Dryer (DRYER) Project

    Data.gov (United States)

    National Aeronautics and Space Administration — The objective of this proposal is to develop a gravity-independent pasteurization and hot air drying process suitable for stabilization of ALS wet cabin waste,...

  20. Closed Loop Waste Processing Dryer (DRYER) Project

    Data.gov (United States)

    National Aeronautics and Space Administration — The objective of this proposal is to develop a gravity-independent pasteurization and hot air drying process suitable for stabilization of ALS wet cabin waste,...

  1. Analysis of efficiency of a solar dryer tunnel type of mango pulp; Analisis de la eficiencia de un secador solar tipo tunel para pulpa de mango

    Energy Technology Data Exchange (ETDEWEB)

    Chagoyan Serrano, Jose [Universidad Autonoma de Baja California Sur, La Paz, Baja California Sur (Mexico)

    2000-07-01

    A new method to assess the performance of a solar dryer is presented. It describes energy efficiency indicators to improve a commercial dryer design. First, a preliminary dryer design procedure is described step by step. Then, two different modes of a tunnel dryer are investigated: Batch and semi-continue operations. The results of the analysis show that, the thermal efficiency is not sufficient to rate de dryer performance. It is necessary to include the productivity of the drying process and the quality of the dried fruit. The drying process and productivity tend to go hand-in-hand but in opposite directions. That is to say, raising the thermal efficiency reduce the process productivity and conversely. The analysis also suggests that an agreement between the efficiency, productivity and the quality must be specified in the drier design. [Spanish] Se presenta un procedimiento nuevo para evaluar la operacion de un secador solar, con el cual se precisan indicadores de la eficiencia que pueden ser utiles para mejorar el diseno del equipo. Se empieza por describir los pasos de un procedimiento de diseno preliminar de un sistema de secado. Despues, se analizan cualitativamente dos secadores: uno que opera por lotes y el otro de modo semicontinuo. Los resultados del analisis muestran que, la eficiencia termica del equipo no es un criterio suficiente para evaluar su operacion; tambien se requiere tomar encuenta la productividad del proceso de secado y la calidad del producto final. Se concluye que la eficiencia termica y la productividad del proceso son conceptos encontrados. Es decir, la eficiencia termica del equipo no es un criterio suficiente para evaluar su operacion; tambien se requiere tomar en cuenta la productividad del proceso de secado y la calidad del producto final. Se concluye que la eficiencia termica y la productividad del proceso son conceptos encontrados. Es decir, la eficiencia termica solo se puede aumentar a costa de la productividad y viceversa

  2. Mathematical Modeling of Drying Kinetics of Bird’s Eye Chilies in a Convective Hot-Air Dryer

    Directory of Open Access Journals (Sweden)

    Kongdej LIMPAIBOON

    2013-12-01

    Full Text Available The drying kinetics of red bird’s eye chilies and the color of the product were investigated in a laboratory scale hot-air dryer under 3 air temperatures of 55, 60 and 65 °C. The 6 mathematical models (Lewis model; Page model; Henderson and Pabis model; Logarithmic model; Modified Page model; and Wang and Singh model were used to fit the experimental data obtained in order to estimate the moisture ratio as the function of drying time. The results showed that operating temperature enhanced the kinetics of the drying of chilies; the drying times of chilies at 55, 60 and 65 °C were 510, 360 and 330 min, respectively. The experimental drying curves obtained at all operating conditions took place in the falling rate period. Comparing the dried products, it was observed that the red bird’s eye chilies dried at a lower temperature had higher Hunter L (lightness, a* (redness and b* (yellowness values. The experimental data were fitted to different drying models. The performance of these models was investigated by comparing the determination of coefficient (R2 and root mean square error (RMSE between the observed and predicted moisture ratios. Among the 6 mathematical models, the Wang and Singh model satisfactorily described the drying kinetics of chilies.

  3. An experimental investigation of shell and tube latent heat storage for solar dryer using paraffin wax as heat storage material

    Directory of Open Access Journals (Sweden)

    Ashish Agarwal

    2016-03-01

    Full Text Available In the presented study the shell and tube type latent heat storage (LHS has been designed for solar dryer and paraffin wax is used as heat storage material. In the first part of the study, the thermal and heat transfer characteristics of the latent heat storage system have been evaluated during charging and discharging process using air as heat transfer fluid (HTF. In the last section of the study the effectiveness of the use of an LHS for drying of food product and also on the drying kinetics of a food product has been determined. A series of experiments were conducted to study the effects of flow rate and temperature of HTF on the charging and discharging process of LHS. The temperature distribution along the radial and longitudinal directions was obtained at different time during charging process to analyze the heat transfer phenomenon in the LHS. Thermal performance of the system is evaluated in terms of cumulative energy charged and discharged, during the charging and discharging process of LHS, respectively. Experimental results show that the LHS is suitable to supply the hot air for drying of food product during non-sunshine hours or when the intensity of solar energy is very low. Temperature gain of air in the range of 17 °C to 5 °C for approximately 10 hrs duration was achieved during discharging of LHS.

  4. Comportamento da beta-ciclodextrina adicionada ao leite de cabra submetido ao processo de desidratação por "spray-dryer" Beta-ciclodextrin's behavior added goat's milk submitted to the "spray-dryer" dehydration process

    Directory of Open Access Journals (Sweden)

    Adriana C. P. Diniz

    2005-06-01

    Full Text Available Este trabalho avaliou o comportamento do agente encapsulante beta -ciclodextrina ( beta-CD adicionado ao leite de cabra submetido ao processo de desidratação por "spray-dryer", através de análise termogravimétrica e de cromatografia gasosa. Após a desidratação, a amostra adicionada de beta-CD apresentou um rendimento real de 10,59% com taxa de perda de 0,04% (em relação ao valor teórico esperado 10,6% ; enquanto na amostra sem adição do agente encapsulante o rendimento real foi de 9,57%, com taxa de perda de 4,27% (valor teórico esperado 10% . Através da análise termogravimétrica (TGA, verificou-se que são volatilizados 44% e 21% dos ácidos comerciais C8 e C10 , respectivamente. Os resultados cromatográficos mostraram uma perda de aproximadamente 30% dos ácidos C8 e 20% dos ácidos C10 , nas amostras de leite de cabra sem beta -CD em relação às amostras com beta-CD. Tais porcentagens estão de acordo com os valores estimados para os ácidos comerciais. Com base nos parâmetros estudados, podemos inferir que há menor perda dos ácidos graxos C8 e C10 na amostra de leite de cabra com beta-CD, provavelmente devido ao efeito encapsulante, aumentando a estabilidade térmica dos ácidos.This work evaluated the effect of the encapsulant agent beta-cyclodextrin (beta-CD added the goat milk submitted to the "spray-dryer" dehydration process, through thermogravimetric analysis and gas cromatography. After dehydration, the sample added of beta-CD presented a real yield of 10,59%, with a loss rate of 0,04% (in relation to the expected theoretical value 10,6%; while in the sample without addition of the encapsulant agent the real yield was 9,57%, with a loss rate of 4,27% (expected theoretical value 10% . It was verified that the volatilization of 44% and 21% of the commercial acids C8 and C10 , respectively, through the thermogravimetric analysis (TGA. The cromatographic results showed losses of approximately 30% of the C8 acids and

  5. Experiments of wheat drying by bin-ventilation dryer%箱式通风干燥机小麦干燥试验研究

    Institute of Scientific and Technical Information of China (English)

    谢焕雄; 王海鸥; 胡志超; 张会娟; 颜建春; 仇春婷

    2013-01-01

    In recent years, the current sun-drying facilities in Chinese rural area are far from being able to meet the requirements of post-harvest drying of major grain crops because of the rapid development of harvesting mechanization, and grain dryers are widely demanded to reduce post-harvest losses of rural grain crops. As an economical and practical grain dryer, bin-ventilation dryer is considerably fitting for Chinese rural production practice. In order to understand the wheat ventilation drying characteristics in flat bed,experimental studies of post-harvest wheat drying were performed on SKS-480 type of bin-ventilation dryer, which involved in testing and analysis of the air field distribution upon the no-load aperture plate, the moisture distribution of materials, the temperature distribution of dry bed and the energy dissipation. The wheat dry bed was 15cm in depth, and the total drying time was set as 6 h, with air temperatures 50℃ during the first three hours and air temperature 60℃during the latter three hours. For testing temperature and moisture content of the wheat dry bed, the drying region area on horizontal plane was evenly divided into 25 unit areas, and the 15 cm-deep dry bed on vertical plane was evenly divided into upper, middle and bottom layers, respectively. It was concluded that there was evident drying speed difference among the horizontal plane and vertical plane of the dry bed, which was caused by the uneven wind field distribution and the dry bed depth. After 6 h of drying, there was very significant difference (p0.01) between the average moisture content of upper and middle layers. And the maximal difference of moisture content among the whole dry bed was more than 3%, which failed to meet the relevant industry standards and the national standards, affecting the drying efficiency and drying cost of the entire batch of materials. After 5 h of drying, average moisture content of the whole dry bed was 11.5% (w.b.) and achieved the

  6. Solar wash dryer, an environment-friendly alternative. Study of technical, architectural and societal aspects. Final report; Zonnewasdroger, een milieuvriendelijk alternatief. Onderzoek naar technische, bouwkundige en maatschappelijke aspecten. Eindrapportage

    Energy Technology Data Exchange (ETDEWEB)

    Israels, E.; Elema, K.; Bouwens, C.; Duijvestein, A.; Van der Eerden, E.; Van Putten, W.; Woltmeijer, E.

    1995-10-01

    The use of electric tumble dryers in the Netherlands increases at a great pace. Holland Energy Systems (HES) developed a prototype solar wash dryer in which the advantages of open air drying and electric drying are combined. The dryer consists of a transparent plate with an air cavity behind it. On the innerside of the air cavity is a metal dark-colored plate, the absorber. Behind this solar collector is the actual drying space, equipped with mobile racks for the laundry. If the sun does not produce enough heat the outside air will be heated electrically. The dryer also contains a flat water tank to store heat at the bottom of the drying compartment. In this report attention is paid to the architectural implementation possibilities of the solar wash dryer and the adjustments that might be made in the design of a house. Next to architectural aspects also juridical and societal aspects are discussed, in particular concerning the fitting-in of the housing construction. figs., tabs., 5 appendices, 11 refs.

  7. 旋转闪蒸干燥机的改进%Improvement and innovation of spin flash dryer

    Institute of Scientific and Technical Information of China (English)

    李宁; 孙德松; 于镇宁

    2012-01-01

    The essay optimizes barriers of the crush tank and crushing blade of the traditional machinery of spin flash dryer, improves efficiency and reduces energy consuming. Through the research of internal motion theory of the traditional spin flash dryer, two questions can be found; first, when material moving circularly in the columnar crushing chamber by airflow, the moving speed, direction of the material and crushing knife are quite close which make crushing efficiency not high; second, material is very easy to hit cylinder wall along tangential by the crushing knife with flighter in vertical plate structure and increase the extent of wall sticking, so that spinning of the crushing knife have no booster action to airflow. Through investigations, if the columnar crushing tank can be altered into polygonal, material can alter its flying direction through knock-on effects and increase frequency of exposure with crushing knife, so that working efficiency can be boosted. At the same time, if the crushing knife can be altered into fan-shaped knife tackle with oblique angle, the ascending motion of thermal current will be prompted and it will advance drying, crushing and ascending of material so that wall-sticking phenomenon of material can be improved.%针对传统结构的旋转闪蒸干燥机的粉碎室内胆和粉碎刀片所存在的欠缺进行改进优化,提高机器的工效,降低能耗.通过对物料在传统结构旋转闪蒸干燥机内部运动机理的研究发现:物料在圆筒形的粉碎室内随气流作圆周运动时,其运动速度、方向与粉碎刀的旋转速度、方向较为接近,粉碎工效不高;物料在带有刮板的垂直板式结构的粉碎刀作用下易沿切向击中筒壁,加大黏壁程度,并且粉碎刀的旋转对气流无辅助作用.如把圆筒形粉碎内胆改为多边形粉碎内胆,使物料在撞击作用下改变飞行方向,增加与粉碎刀的接触次数,可以提高工效;同时把粉碎刀改为带

  8. Modeling of Drying Process and Energy Consumption of Onion (Ex-gidankwanoSpp. Slices in a Hybrid Crop Dryer

    Directory of Open Access Journals (Sweden)

    N.R. Nwakuba

    2017-01-01

    Full Text Available High consumption of energy in the drying industry has prompted extensive research regarding various aspects of crop drying energy consumption. Specific energy consumption, moisture ratio and thermal efficiency in drying of fresh ex-gidankwano onions variety were determined using a hybrid electric-gas dryer at air temperatures of 50, 60 and 70oC, and at air velocities of 0.5, 1.0 and 1.5m/s. Thin layer models were selected by carrying out statistical analyses to fit the drying rate data to themodels. The Page drying model was found more suitable to describe the drying behaviour of onions slices based on its highest average R2 -values of 0.99 and lowest average RMSE of 3.91for all temperatures and air velocitiesirrespective of the heat source. Records of drying rates and energy consumption were made using electronic weighing balances and the Arduino microprocessor respectively. Results obtained show that the specific energy consumption decreases with increase in air temperature but increases with increase in air velocity in both heat sources. The minimum and maximum specific energies for the electric and gas heat sources were 48.73MJ/kg and 90.21MJ/kg, and 36.83MJ/kg and64.65MJ/kg of moisture evaporated respectively.The thermal efficiency of the heat sources increased proportionally with increasing drying air temperature and decreased with increase in drying air velocity with maximum values of 54.8% and 68.2% for the electric and gas heaters respectively. The gas heat source performed more efficiently in terms of energy consumption and thermal efficiency at different temperatures and air velocities.

  9. Drying Characteristics and Product Quality of Lemon Slices Dried with Hot Air Circulation Oven and Hybrid Heatpump Dryers

    Directory of Open Access Journals (Sweden)

    Yong Hong Lee

    2014-12-01

    Full Text Available In this research, drying characteristics and product quality of Coulomb-force-assisted heatpump and oven dried lemon slices were studied. Lemon slices with 3 mm thickness each, were dried using oven and Coulomb-force-assisted-heatpump dryer with and without auxiliary heater at different drying conditions. It was found that the drying rate of the lemon slices dried by all drying methods showed only falling rate states, which indicates the drying kinetics were controlled by internal moisture diffusion. Oven drying of lemon slices at 60°C showed the highest drying rate among all, followed by oven dried slices at 50°C, Coulomb-force-heater-assisted-heatpump (CF-HT-HP dried slices at 31°C, Coulomb-force-assisted-heatpump (CF-HP dried slices at 22°C, oven dried slices at 40°C and heatpump dried slices at 22°C. The average effective moisture diffusivity value for the slices dried with these drying methods was found in the range of 16.2 to 63.8´10-4 mm2min-1. In terms of quality assessment, CF-HP dried lemon slices retained the highest amount of Vitamin C as compared to the lemon slices dried by other drying methods. However, it retained relatively lower amount of total phenolic content (TPC as compared to oven dried products. Among of all, CF-HP drying method produced dried lemon slices with the highest Vitamin C (6.74 mg AA / g dry weight whereas oven dried lemon slices at 50°C preserved most of the TPC in the dried slices, which recorded as 13.76 mg GA / g dry weight.

  10. Unique concept results in 67% energy saving of dryer. Successful use of a NH3 heat pump for a McCain fried potato dryer; Uniek concept leidt tot een energiebesparing van 67% op de droger. NH3-warmtepomp succesvol toegepast op frietdroger van McCain

    Energy Technology Data Exchange (ETDEWEB)

    De Leeuw, M. [De Kleijn Energie Consulting, Druten (Netherlands)

    2013-07-15

    French fries producer McCain Foods installed in the summer of 2012 an ammonia heat pump for a fried potato dryer in Lelystad, Netherlands. After six months it appears that the installation operates without problems and with a very high efficiency [Dutch] Frietproducent McCain Foods installeerde in de zomer van 2012 een warmtepomp op de frietdroger in Lelystad. Na een half jaar kan geconstateerd worden dat de installatie zonder problemen en met een zeer hoog rendement draait.

  11. Textile drying using solarized can dryers to demonstrate the application of solar energy to industrial drying or dehydration processes, Phase II. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Mitchell, P.D.; Beesing, M.E.; Bessler, G.L.

    1979-12-01

    This program has resulted in the installation of a solar energy collection system for providing process heat to a textile drying process. The solar collection subsystem uses 700 square meters (7500 square feet) of parabolic trough, single-axis tracking, concentrating collectors to heat water in a high temperature water (HTW) loop. The solar collectors nominally generate 193/sup 0/C (380/sup 0/F) water with the HTW loop at 1.9 x 10/sup 6/ Pa (275 psi). A steam generator is fueled with the HTW and produces 450 kg/hour (1000 pounds per hour) of process steam at the nominal design point conditions. The solar-generated process steam is at 0.5 x 10/sup 6/ Pa (75 psi) and 160/sup 0/C (321/sup 0/F). It is predicted that the solar energy system will provide 1.2 x 10/sup 6/ MJ/year (1.1 x 10/sup 9/ Btu/year) to the process. This is 46 percent of the direct isolation available to the collector field during the operational hours (300 days/year of the Fairfax mill. The process being solarized is textile drying using can dryers. The can dryers are part of a slashing operation in a WestPoint Pepperell mill in Fairfax, Alabama. Over 50 percent of all woven goods are processed through slashers and dried on can dryers. The collectors were fabricated by Honeywell at a pilot production facility in Minneapolis, Minnesota, under a 3000-square-meter (32,000-square-foot) production run. The collectors and other system components were installed at the site by the Bahnson Service Company and their subcontractors, acting as the project general contractor. System checkout and start-up was conducted. Preliminary system performance was determined from data collected during start-up. System design, fabrication and installation, data analysis, operation and maintenance procedures, and specifications and drawings are presented.

  12. Energy-saving Reconstruction of Heatless Regeneration Adsorption Dryer%无热再生式干燥器节能改造

    Institute of Scientific and Technical Information of China (English)

    章罡本; 王乾虎

    2011-01-01

    This paper presents the energy-saving reconstruction of one heatless regeneration adsorption dryer based on PLC , touch screen,dew point sensor and proper hardware.With the dew point control system, the quality of compressed air is ensured and the energy cousumption is reduced.%利甩PLC可编程控制器、触摸屏、露点变送器及相关设备,组成了露点控制系统,实现了对无热再生式干燥器的节能改造,保障了压缩空气的品质,减少了能源消耗.

  13. Variation of the height of the grain bed of an indirect solar bin dryer; Variacion de la altura del lecho del grano en un secador solar indirecto

    Energy Technology Data Exchange (ETDEWEB)

    Sima, Efrain; Alvarez, Gabriela; Garcia, Saul [CENIDET, Cuernavaca, Morelos (Mexico)

    2000-07-01

    This paper presents the effect of the variation of the size of the grain bed of an indirect solar bin dryer. This solar dryer was designed and built at the Instituto Tecnologico de Zacatepec and Sima performed the thermal evaluation. The solar bin dryer consists of a bin dryer of 0.92 m diameter and 1 m height (the maximum height of the grain bed is 0.6 m). a 2 m{sup 2} solar collector, a blower and an electronic card to control the inlet air flow of the bin. A load of 36 kg, 45 kg, 52 kg and 64 kg of corn were dried. The heights of the grain were 7.5 cm, 10 cm, 12.5 cm and 17 cm respectively. Solar radiation, inlet air velocity of the solar collector, pressure drop, grain temperature and humidity, ambient temperature and humidity of the drying air were recorded. The initial grain humidity was 27.2% and the final was 11.8%. [Spanish] En este trabajo se presenta el efecto de la variacion del lecho del grano en el proceso de secado de maiz, en un prototipo de secador solar de tipo indirecto. El secador fue disenado y construido en el Tecnologico de Zacatepec y evaluado por Sima, consta de una camara de secado de 0.92 m de diametro y una altura de 1 m. (la altura del lecho maximo de grano posible es de 0.6 m.), un colector solar con un area de 2 m{sup 2}, un extractor de aire y un control electronico para el flujo de aire. El secado de maiz se llevo a cabo con cargas de maiz de 36, 45, 52 y 64 kg. Las alturas en el lecho del grano fueron 7.5, 10, 12.5 y 17 cm. Para cada altura de lecho de grano se realizo una prueba. Durante cada prueba se realizaron mediciones de: radiacion solar, velocidad del aire a la entrada, caida de presion, temperatura del grano, humedad del grano, temperatura del aire ambiente, temperatura y humedad del aire de secado a la entrada y salida del secador. La humedad inicial del grano fue alrededor de 27.2% y la final de 11.8%.

  14. Application of spin flash dryer in barium carbonate drying%旋转闪蒸干燥器在碳酸钡干燥中的应用

    Institute of Scientific and Technical Information of China (English)

    张小钦; 张风缺

    2009-01-01

    介绍了河北诺达化工设备有限公司开发生产的旋转闪蒸干燥器代替回转圆筒干燥器在碳酸钡干燥过程中的应用.通过对投资、能耗、产品质量、环保效益的详细分析得出结论:用旋转闪蒸干燥器代替回转圆筒干燥器,具有节省投资,节约能耗,提高产品质量,减小环境污染等优势,为碳酸钡的干燥提供了一种新方法.该设备也适用于碳酸锶、硫酸钡、碳酸钙等滤饼类物料的干燥,同样对于冶金、化工、医药、食品等行业的滤饼类物料的干燥也具有极高的应用价值.%Application of spin flash dryer developed and produced by Hebei Nuoda Chemical Equipment Co.,Ltd.to replace rotary cylinder dryer in drying process of barium carbonate was introduced.Through detailed analysis on investment,energy consumption,product quality,and environmental benefits,the conclusion was obtained:comparing with rotary cylinder dryer,spin flash dryer has the advantages,such as less investment,energy saving,better product quality,and smaller pollution,which provide a new drying way for barium carbonate production.Meanwhile,this equipment is suitable for drying other cake - type materials,such as strontium carbonate,barium sulfate,and calcium carbonate.It also has high application value for cake - type materials in other industries,such as metallurgical,chemical,pharmaceutical,and food.

  15. Influence of the process control on the thermal energy requirement of convection dryers in the brick industry; Einfluss der Prozessfuehrung auf den thermischen Energiebedarf von Konvektionstrocknern in der Ziegelindustrie

    Energy Technology Data Exchange (ETDEWEB)

    Tretau, Anne

    2008-06-10

    Brick manufacturing demands high amount of energy. The energy flow analysis inside the brick factory shows that the convective drying of green bricks consumes more than half of the total thermal energy required for brick manufacturing. Therefore this paper deals with the theoretical analysis and investigation for the energy requirement of green bricks. For this, a physical-based model has been developed, which describes the dependence of drying-kinetics as well as the energy-requirement interims of the process parameter like mass of the supply air. It turns out that the specific energy requirement substantially depends on temperature and humidity of the ambience air and also supply air mass flow and its temperature. Due to the continuous temperature rise of the green bricks during the second drying section the specific energy requirement increases significantly with the progressive motion of the drying in a chamber dryer. This is due to the fact that the green brick as well as the air conditioning distance more and more from the cooling limit. Just a low part of the dryer exhaust air is saturated. The exhaust air is continuously sucked out and the green bricks are pulled inside the dryer. So the exhaust air has a relatively higher water saturation. On general, continuous dryers have a lower energy requirement than chamber dryer. For the both types of dryers, the mathematical model shows that the increasing of the supply air temperature combined with a commensurate subsidence of supply air mass flow, results in a reduction of drying energy requirement. The change of other essential parameters of drying like green brick thickness, and density as well as the moisture diffusion coefficient, and the vapour diffusity which are only important in the second drying section are of comparatively negligible effect. The developed mathematical model is successfully implemented for the energy investigation in the industrial dryers. The increase in supply air temperature results

  16. 烟草CTD烘丝机出料罩的改造%Improvement of Discharging Hood of CTD Dryer

    Institute of Scientific and Technical Information of China (English)

    戴宇昕

    2013-01-01

    The problems that the stickiness of the side walls of discharging hood and the wet mass and waterlogging tobacco caused by the condensation leaks were widely encountered during the CTD dryer's use. The main reason was that the original discharging hood failed to exhaust the moisture in time and no water diversion structure was designed for the condensate water. To solve the problems, the discharging hood of CTD was improved as follows: two protruding edges were added to separate water and tobacco as well as the sieve flappers were used to divert water according to wall attachment effect; the shape of discharging hood was changed to an outward trumpet shape; additionally, a slanted toward water receiving tank was added and channels were set to exhaust moisture, etc. The results of application after improving showed that: the tobacco stuck to the side walls of discharging hood decreased by 93.4% and the dropping amount of wet mass declined by 98.8%. Moreover, there was no condensate water leakage and moisture spillover.%CTD烘丝机在使用过程中存在出料罩侧壁粘料、结露滴漏并诱发湿团及水渍烟的问题。这主要是由于原出料罩未能及时排出出口的潮气,也未对冷凝水设计导水结构所致。为此对CTD出料罩进行改造:根据附壁效应增设两重导水凸棱进行水料分离,筛网插板进行导水;改变出料罩外形为外扩喇叭状;加装斜向外侧倾斜的接水槽;设置排潮管道排气等。改造后应用效果表明,出料罩侧壁粘壁量、湿团掉落量分别降低了93.4%和98.8%,无冷凝水滴漏及潮气外溢现象,提高了产品工艺质量。

  17. Hybrid system: Heat pump-solar air dryer for grains; Sistema hibrido: bomba de calor - calentador solar de aire para el secado de productos agricolas

    Energy Technology Data Exchange (ETDEWEB)

    Soto Gomez, Willfredo [Instituto Tecnologico de Tijuana, Tijuana (Mexico); Ortega Herrera, Jose Angel [Instituto Politecnico Nacional, Mexico, D.F. (Mexico)

    2000-07-01

    Design, building, operation and evaluation energy wise of a hybrid experimental type, with heat pump, that uses no chloride, does not destroy the ozone layer. It is solar air dryer for grains. In this research we dry rice. It has tree systems: 1.- A mechanical compression heat pump, 2.- An air solar heater, and 3.- An agriculture products dryer. The drying capacity is 20 pounds of grain /day, with a median daily solar radiation. The costs is approximately U.S. $ 6 000.00. The heat pump used 22 refrigerant first, and now works with refrigerant SUVA 9000. This refrigerant will be available this year in the I.S., it is one of the ecological class that substitutes the chlorofluorocarbonates. [Spanish] Se disena, construye, opera, y evalua energeticamente, un sistema hibrido tipo experimental, con bomba de calor que utiliza refrigerante que no contiene cloro, y no destruye la capa de ozono y un calentador solar de aire, para secar granos. En este trabajo secamos arroz. Se compone de tres sistemas: 1.- Bomba de calor por compresion mecanica, 2.- Calentador solar de aire, 3.- Secador de productos agricolas. La capacidad de secado es de 10 Kilos de granos/dia promedio. Tiene un costo aproximado de $ 60 000. La bomba de calor utiliza refrigerante 22 en una primera generacion, y actualmente opera con un refrigerante SUVA 9000, en una segunda generacion, este refrigerante se comercializara en este ano, en la Union Americana, pertenece a la familia de los llamados refrigerantes ecologicos, sustitutos de los clorofluorocarbonados.

  18. Electric field and current density distributions induced in an anatomically-based model of the human head by magnetic fields from a hair dryer.

    Science.gov (United States)

    Tofani, S; Ossola, P; d'Amore, G; Gandhi, O P

    1995-01-01

    We have used the impedance method to calculate the induced electric (E) fields and current densities (J) for the spatially varying vector magnetic fields due to a hair dryer. In this method, applicable for low-frequency exposures where the quasi-static approximation may be made, the biological body or the exposed parts thereof are represented by a three-dimensional (3-D) network of impedances whose individual values are obtained from the electrical properties sigma, epsilon r for the various tissues. We have measured the 3-D variations of the 50-Hz magnetic fields from a typical hair dryer and found that the various components correlate well with those for a helical coil. The non-uniform magnetic fields thus obtained are used to calculate the induced E and J with a resolution of 1.31 cm for the model of the head and neck. The induced E values are compared with the fields endogenous to the body and the minimum detectable E-field limits based on the cellular thermal noise model proposed by Weaver and Astumian (1990, 1992).

  19. 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.

  20. Design on Mechanical Seal of Vacuum Rake Dryer%真空耙式干燥器机械密封的设计

    Institute of Scientific and Technical Information of China (English)

    朱军; 赵飞虎; 刘龙全

    2014-01-01

    The characteristics of drying process and equipment of some model vacuum rake dryer were analyzed. By tak-ing a vacuum rake dryer with shaft diameter of 320 mm as an example,the seal structure was designed,the cleaning meth-od,material selection of friction pairs,assistant seal and structural parts were explored. Trial runs were conducted on the designed sample machine by simulating practical working condition. The result shows that the structural seal has good seal-ing effect.%对真空耙式干燥工艺及设备特点进行分析,以轴径为320 mm的某型号真空耙式干燥器为例,设计其密封结构,探讨其冲洗方案及摩擦副、辅助密封和结构件的选材。模拟实际工况对设计的样机进行的运转试验,结果表明该密封结构密封效果良好。

  1. Variation of the temperature and moisture content of the coffee in horizontal dryers using firewood e GLP as fuel; Variacao da temperatura e do teor de agua do cafe em secador rotativo usando lenha e GLP como combustiveis

    Energy Technology Data Exchange (ETDEWEB)

    Reinato, Carlos H.R. [Universidade Federal de Lavras (UFLA), MG (Brazil). Curso de Ciencia dos Alimentos; Borem, Flavio M. [Universidade Federal de Lavras (UFLA), MG (Brazil). Dept. de Engenharia

    2006-05-15

    The present study was accomplished in the 'Polo de Tecnologia em Pos-Colheita de Cafe', at the 'Universidade Federal de Lavras', MG, Brazil. Its objective was to investigate the distribution of temperature and moisture content in the radial direction of the rotary dryer. For the test accomplishment, two dryers of the Pinhalense mark were used concomitantly with a 5,000 kg capacity. In a dryer, firewood was used and in the other LPG, as fuels for air heating. The air drying and coffee mass temperature were determined by means of thermocouples distributed on eighteen ends of the dryer. The readings of all the temperatures recorded on the dial were done every half an hour. Moisture content loss was followed in nine points in coffee mass. It was found that the values of temperature in the plenum presented less oscillation in the drying which used LPG. Furthermore, regardless the sort of fuel, there were found maximum temperature gradient of 20 deg C and three percents points of moisture content in the radial direction in central section, as consequence of the higher values of static pressure (637.84 Pa) in the plenum observed in this section. Regardless the kind of fuel, the temperature gradient measured in the longitudinal sense of the coffee mass was substantially less in the radial direction. (author)

  2. 纸机干燥部余热回收技术与设备(续)%Technology and Equipment of Waste Heat Recovery in Dryer Section of Paper Machine (Continuous)

    Institute of Scientific and Technical Information of China (English)

    张秀文

    2012-01-01

    Some waste heat recovery technology and equipment used in dryer section of paper machine at home and abroad were introduced in this paper.%介绍一些国际、国内余热回收技术和设备,供同行分析、研究和借鉴.

  3. Determination of stresses caused by fluctuation of acoustic load in the steam dryers of a BWR; Determinacion de esfuerzos originados por fluctuacion de carga acustica en los secadores de vapor de un reactor BWR

    Energy Technology Data Exchange (ETDEWEB)

    Centeno P, J.; Quezada G, S.; Prieto G, A.; Vazquez R, A.; Espinosa P, G. [Universidad Autonoma Metropolitana, Unidad Iztapalapa, Av. San Rafael Atlixco No. 186, Col. Vicentina, 09340 Mexico D. F. (Mexico); Nunez C, A., E-mail: javcuami26@hotmail.com [Comision Nacional de Seguridad Nuclear y Salvaguardias, Dr. Jose Ma. Barragan No. 779, Col. Narvarte, 03020 Mexico D. F. (Mexico)

    2014-10-15

    The extended power up-rate (EPU) in a nuclear power plant cause various problems in BWR components also in the steam system. This due to increased steam flow generated in the reactor and is conveyed to the turbine by the four main steam lines (MSL). One of the most serious problems is the generation of acoustic pressure loads in the metal structure of the steam dryer which eventually leads to fatigue failure and even the appearance of cracks, and in turn it causes loose parts that are entrained by the steam and transported in the MSL. This problem is due to the fluctuation of load acoustics caused by the union of the safety or relief valves (SRV) with the MSL, spreading through these to reach the reactor pressure vessel (RPV) where the effect of resonance of the acoustic wave is amplified and impacts directly in the supporting structure of the steam dryer, skirt and the panels where the mixture liquid-steam is dried, by centrifugation effect and runoff of liquid water. Efforts in the steam dryer operating conditions of EPU for two cases will be analyzed in this work, the first is before the installation of Acoustic Side Branch (ASB), and in the second case we consider the installation of said ASB in the standpipes of SRV. The analysis was performed with numerical experiments on a platform for computational fluid dynamics with virtual geometries previously designed based on the actual components of the reactor and steam system. The model to study is delimited by the top of the RPV, the steam dryer and a section of each of the four MSL with ten standpipes of SRV. With the obtained data and considering the mechanical-structural properties of the steam dryer material, we can evaluate the mechanical resistance to impacts by acoustic pressure load and its possible deformation or cracking. (Author)

  4. Análisis del Efecto de Variables de Diseño en el Comportamiento de una Secadora de Granos de Amaranto Analysis of the Effect of Design Variables on the Performance of an Amaranth Grain Dryer

    Directory of Open Access Journals (Sweden)

    A. I. Lema

    2005-01-01

    Full Text Available En este trabajo se estudia la incidencia de tres variables fundamentales en el desempeño de una secadora rotativa para amaranto: el tiempo de residencia del grano dentro del equipo, la temperatura, y el caudal de aire utilizados. Estas variables inciden directamente sobre el tiempo de secado y la humedad final del producto. Para determinar el desempeño de la secadora se utilizó como parámetro la velocidad de evaporación del agua. Se realizó primeramente un diseño estadístico de las experiencias, las que luego se implementaron en una secadora rotativa experimental construida en el Instituto de Física de Rosario. Los datos obtenidos fueron analizados utilizando técnicas de análisis de varianza. El estudio reflejó que tanto el tiempo de residencia como la temperatura del aire tienen gran incidencia en el funcionamiento de la secadora rotativa. Así, un diseño de alta eficiencia puede conseguirse optimizando estos dos parámetros.This work studies the effects of three fundamental variables related to the performance of a rotary amaranth dryer, including the residence time of the grain in the dryer, the temperature, and the flow rate of air used. These variables directly affect the drying time and moisture content of the final product. The evaporation rate of water from the grain was used to estimate the performance of the dryer. First, a statistical design of the experiments was prepared, with the experiments then carried out using an experimental rotary dryer built at the Rosario Physics Institute. The data obtained were statistically evaluated using analysis of variance. The study showed that both the residence time and the air temperature had a strong influence on the performance of the rotary dryer. A high efficiency design for this process can thus be obtained by optimizing these two parameters.

  5. 真空干燥机用真空系统的改进设计%Modified Design of Vacuum System for Vacuum Dryer

    Institute of Scientific and Technical Information of China (English)

    张勇; 周艳

    2011-01-01

    The modification on design of vacuum system of vacuum dryer in the production of PA6 chips was introduced. The mechanical pump was replaced by water jet pump, the production and maintenance work were easily, meanwhile, the repairing and energy expenses were reduced and the total production cost was cut down greatly.%介绍了锦纶6切片生产装置中真空转鼓干燥机真空系统的改进设计,利用水喷射泵代替原有的机械泵,方便了生产和维修,同时节约了维修费用,并降低了电耗,从而大大降低了生产成本.

  6. Modulating protein release profiles by incorporating hyaluronic acid into PLGA microparticles Via a spray dryer equipped with a 3-fluid nozzle

    DEFF Research Database (Denmark)

    Wan, Feng; Maltesen, Morten Jonas; Andersen, Sune Klint

    2014-01-01

    obtained. Addition of HA in inner feed solutions increased the feed viscosity, but with no influence on the surface tension. All inner feed solutions showed non-Newtonian shear thinning behavior and the rheological properties were not time dependent. The CLSM and XPS analyses suggested a core-shell like...... with or without HA were prepared using a spray dryer equipped with a 3-fluid nozzle. The effects of HA on the surface tension and the rheological behavior of the inner feed solution were investigated. The physicochemical properties of the resulting microparticles were characterized using scanning electron......: The present work demonstrates the potential of HA to modulate protein release profile from PLGA microparticle formulations produced via spray drying using 3-fluid nozzle....

  7. THE STUDY OF THE KINETICS OF DRYING FOOD RAW MATERIAL OF PLANT ORIGIN IN THE ACTIVE HYDRODYNAMIC REGIMES AND DEVELOPMENT OF DRYER ENGINEERING CALCULATION METHODS

    Directory of Open Access Journals (Sweden)

    A. N. Ostrikov

    2015-01-01

    Full Text Available Consumer properties of food raw material formed during the heat treatment. New physical, flavoring and aromatic properties of the products of plant origin, formed during drying due to substantial changes in the composition of the raw materia l occurring as a result of biochemical reactions. In the production of dried and roasted products is very important to follow the parameters that contribute to the passage of biochemical processes aimed at creating a product with high nutritional qualities, strong aroma and pleasant taste. We studied the basic kinetics of the drying process of food raw material (in terms of artichoke in a dense interspersed layer, which formed the basis for the rational choice of the drying regime with due consideration of changes in the moisture content of the product are studied. The nature of the effect of the dried product movement hydrodynamic conditions on a layer height and intensity of drying is established. As a result of food raw material drying process kinetics analysis (in terms of artichoke multistep drying regimes were chosen. Analysis of the artichoke particles drying by air, air-steam mixture and superheated steam intensity showed the presence of two parts: the horizontal one and gradually diminishing one. Kinetic laws of the artichoke drying process in a dense interspersed layer were the basis of engineering calculation of dryer with a transporting body in the form of a "traveling wave". Application of the dryer with the transporting body in the form of a "traveling wave" for food raw material drying allow to achieve uniform drying of the product due to the use of soft, gentle regimes of oversleeping while preserving to the utmost particles of the product; to improve the quality of the finished product through the use of interspersed layer that reduces clumping of product to be dried.

  8. 物理环境对人发结构特性的影响研究%Study on Influence of Electric Hair Dryer and Ultraviolet Radiation on Human Hair’s Structure Property

    Institute of Scientific and Technical Information of China (English)

    刘开达; 刘双

    2013-01-01

    In accordance with professional studies of the electric hair dryer and ultraviolet ration’s in-fluence on its morphological structures,diameter,breaking force,it is found that the electric hair dryer and ultraviolet radiation lead to serious inj ury to human hair.%研究了电吹风、紫外线照射等物理环境对人发形态结构、直径、断裂力的影响。结果表明,电吹风的吹干和紫外线长时间的照射均会对头发造成一定程度的损伤。

  9. Evaluation of a integral systems greenhouse - solar dryer for small growers; Evaluacion de un sistema integral invernadero - secadero solar para pequenos productores

    Energy Technology Data Exchange (ETDEWEB)

    Garcia, Victor O; Iriarte, Adolfo A [INENCO, Universidad Nacional de Catamarca, Catamarca (Argentina); Carabajal, Dante; Sabadzija, Gabriela; Tomalino, Luis [E.E.A. INTA, Catamarca, Catamarca (Argentina)

    2000-07-01

    Due to poor yielding capacity in the province of Catamarca, Argentina, it is necessary to improve solar drying systems in order to have a better quality final product. It is also essential to divide the costs of infrastructure with other complementary activities because of the need to make drying methods profitable. The system proposed in this work is a dryer-greenhouse with a double purposed macrotunnel greenhouse: during Winter it is used as a yielding system, and in Summer it is prepared to fulfill the functions of a solar dryer. The crops evaluated in winter were: small vegetable marrow (Curcubita maxima L), melon (Cucumis melo), ad cucumber (Cucuis sativus). Crop cycle, harvest time and tield in Kg/m were determined for each species. The assessment of the dryer was made using pepper for paprika observation of the thermal behavior of the product during drying and its final quality. The product obtained had a very good quality in color, taste and aroma with a classification of extra quality according to the Argentine Nutritional Code and the 7541 ISO Standard. Drying time decreased considerably compared to that observed in open air drying, 1995, 1996 and 1997 campaigns were economically assessed, and an evaluation of investments in five years was also conducted obtaining a positive VAN and a TIR above the cost of the best alternative for money expenditure. This integrated system is valid alternative in a sustainable production for small growers. [Spanish] Debido a las caracteristicas productivas de la Provincia de Catamarca Argentina, es necesario optimizar los procesos del secado solar teniendo en cuenta la calidad final del producto. Ademas, debido a la necesidad de rentabilizar los metodos de secado, imprescindible repartir los costos de infraestructura con otro tipo de actividad complementaria. El sistema propuesto en este trabajo es un invernadero secadero que utiliza un invernadero macrotunel que cumple una doble funcion, durante el invierno se usa como

  10. Qualidade fisiológica de sementes de sorgo coletadas em diferentes pontos de um secador Physiological quality of sorghum seeds collected at different points in the dryer

    Directory of Open Access Journals (Sweden)

    Jadir N. da Silva

    2001-12-01

    Full Text Available Neste trabalho, avaliou-se a qualidade fisiológica e se quantificaram os possíveis gradientes de umidade de sementes de sorgo BR 601, durante o armazenamento. Utilizaram-se amostras coletadas em secador de camada fixa vertical, com duto central perfurado e distribuição radial de ar. Os pontos amostrais no secador se distanciavam 0,10; 0,30 e 0,50 m em relação à lateral do duto central de ar e nas alturas de 0,85; 2,02 e 3,64 m da base do secador, com capacidade de 8 t, além de uma amostra média (M que representou os três pontos radiais, respectivamente. Armazenou-se o sorgo durante nove meses e se avaliou a germinação, vigor e umidade do produto no terceiro, sexto e nono meses de armazenamento. Não houve diferença na qualidade fisiológica das sementes nas diferentes alturas e distâncias em relação ao duto central de ar do secador, em relação à média (M durante o armazenamento, mas no decorrer deste, a queda de qualidade foi mais evidente no teste de frio, obtida no nono mês de armazenamento.The objective of this work was to evaluate the physiological quality and possible moisture gradients in seeds of sorghum BR 601, during storage. Samples from a vertical fixed-bed dryer with a perforated central duct and radial air distribution were used. In the dryer, the sample points were located at 0.10, 0.30 and 0.50 m distances in relation to the lateral of the central air duct. A composite sample was also collected and used as the control in relation to the others, at the respective heights. These sampling procedures were followed at heights of 0.85; 2.02 and 3.64 m from the dryer base. Within each height and distance relative to the air duct, the collected samples were stored during nine months and evaluated for germination and vigor. At the third, sixth and ninth months after storage, the samples were evaluated for possible differences in quality and seed moisture gradient in comparison to the composite sample. No differences

  11. 洗衣机脱水桶成型模具设计计算与参数选定%The Caculating Parameters on Designing Models of Tumble Dryer

    Institute of Scientific and Technical Information of China (English)

    张六玲

    2001-01-01

    By offering analysis to the characteristics of the plasti model of tumble dryer this paper introduces the methods for designing models and caculating the parameters.%通过对洗衣机脱水桶塑料成型件的特性分析,简要介绍了其成型模具设计和有关参数的计算方法.

  12. Application and research progress of vacuum belt dryer%真空带式干燥机的应用及研究进展

    Institute of Scientific and Technical Information of China (English)

    赵丽娟; 李建国; 潘永康

    2012-01-01

    A vacuum belt dryer (VBD) consists of drying chamber, vacuum system, dosing system, belt transport device, product crusher, CIP system, PLC system, heating and cooling system, and discharge system. The vacuum degree in drying chamber is 1 000-3 000 Pa, material temperature is 30-60 ℃. This type of dryer is suitable for drying the materials sensitive to heat and oxygen. Its heat transfer is realized by conduction-radiation. At present, a few literatures on drying characteristics, heat and mass transfer mechanism are reported to direct the design and production of industrial equipment, so the design of VBD is based on experience, which can not bring its energysaving advantage adequately. Vacuum belt drying belongs to thin layer drying. Many literatures on vacuum thin layer drying were summarized, which provides a basis for VBD drying investigation. Further study on the drying properties, heat and mass transfer of VBD drying are expected.%真空带式干燥机(VBD)由干燥室、真空系统、布料机构、履带输送装置、切料机构、CIP清洗系统、PLC控制系统、加热和冷却系统以及卸料系统组成.干燥室内真空度为1 000-3 000 Pa,物料温度为30-60℃,适用于热敏及氧敏性物料的干燥,其传热方式为传导-辐射联合传热.目前有关真空带式干燥机干燥特性及传热传质机理的研究报导较少,难以指导工业设备的设计与生产,故而真空带式干燥机的设计主要是依靠经验,这使得其节能降耗的优势不能充分体现出来.真空带式干燥属于薄层干燥,文中综述了真空薄层干燥方面的一些研究文献,为真空带式干燥机的理论研究奠定了基础,以期研究者们进一步对真空带式干燥机的干燥特性及传热传质理论进行研究.

  13. CFD simulation and optimization of airflow field in industrial tunnel dryer with different blowing designs%不同进风方案下隧道烘干窑热风流场CFD模拟和优化

    Institute of Scientific and Technical Information of China (English)

    师建芳; 吴中华; 刘清; 娄正; 赵玉强; 朱明

    2014-01-01

    隧道烘干窑内同一横截面的热风均匀性影响着物料干燥均匀性和产品质量,而烘干窑入口风速分布直接影响着窑内热风流场的均匀分布。为了解决单一风机直进风隧道烘干窑存在的风速不均匀问题,提出了多种进风结构设想,并利用计算流体力学方法对实际生产的隧道窑进风流场进行数值模拟,研究3种不同的进风方案(4风机、6风机和9风机)对隧道窑内热风流场均匀性的影响。模拟结果表明:6风机方案下隧道窑入口处进风均匀,热风扩散距离短,窑内热风流场整体均匀性较佳,综合性价比最高。研究结果为隧道窑入口进风的设计提供参考。%The tunnel dryers with direct blowing are widely applied to dry agricultural products in Chinese rural area. While in practice, the existing single fan blowing designs were found to cause a non-uniform gas velocity distribution inside the tunnel, which results in a non-homogeneous drying quality of the dried product. To address this problem, a multiple fans blowing design concept was proposed in this paper and its feasibility was evaluated by using the computational fluid dynamics (CFD) modeling method. In this paper, the CFD model was developed to simulate the cold flow field inside the tunnel dryer and thus the drying process was ignored at the present stage. The self-developed CFD model consisted of governing equations and suitable boundary conditions. The governing equations comprised of the mass, momentum conservation ones, the K-epison turbulent ones. The boundary conditions were set according to the actual operation conditions of the tunnel dryer and included the velocity inlet, pressure outlet, and non-slip boundary ones. The mathematical model was solved using a commercial CFD software-Fluent 6.3. The flow field inside an industrial tunnel dryer with a single fan blowing used for the drying of cowpeas was measured experimentally and simulated

  14. Determinación del coeficiente global de transferencia de calor en secaderos rotativos de cáscara de limón Determination of global heat transfer coefficient in lemon peel rotary dryers

    Directory of Open Access Journals (Sweden)

    Marcos A. Golato

    2005-12-01

    Full Text Available En la bibliografía consultada no se encontraron trabajos de secado de cáscara de limón en secaderos rotativos. Se realizaron ensayos de medición en secaderos rotativos de cáscara de limón en una instalación agroindustrial del noroeste argentino. Se desarrolló un modelo matemático semiempírico mediante la resolución de los balances de materia y energía. Se obtuvo una correlación estadística para la predicción de los coeficientes globales volumétricos de transferencia de calor aparentes para secaderos rotativos de cáscara de limón.No papers on lemon peel drying in rotary dryers were actually found in the sources consulted. Measurement tests were carried out in the assessment of rotary dryer systems used to dehydrate lemon peel in an agroindustrial plant of Northwestern Argentina. A semiempirical mathematic model was developed solving mass and energy balances. A statistical correlation for predicting global heat transfer coefficient in rotary dryer lemon peel dehydration was obtained.

  15. The Operation And Fault Handling Of The Qinshan Second Nuclear Power Plant's Hydrogen Gas Dryer%秦山第二核电厂氢气干燥器的运行及故障处理

    Institute of Scientific and Technical Information of China (English)

    王瑞军

    2016-01-01

    氢气湿度超标对氢冷发电机组内部部件会产生不良影响,甚至威胁到发电机组的安全可靠运行。调节氢气湿度的主要设备---氢气干燥器的运行状态好坏,直接关系到发电机运行状态的好坏。了解氢气干燥器的运行原理,及时处理氢气干燥器运行中出现的故障,是每一位电厂运行人员的必修功课。%Hydrogen humidity levels More than the standard will have an adverse influence on hydrogen-cooled generator internal components , and even threat the safe and reliable operation of the generator set. Adjust the main equipment of the hydrogen humidity.The success or failure of the operation of hydrogen gas dryer, directly relates to the stand or fall of running state of generator. Understanding of hydrogen gas dryer operation principle and in a timely manner to deal with the faults in the operation of hydrogen gas dryer ,is a compulsory lesson to every power plant operators.

  16. Functional model of an energy-saving laundry dryer - Functional model and trials - 2nd phase final report; Funktionsmuster eines energiesparenden Waeschetrockners - Funktionsmuster und Versuche - Schlussbericht der 2. Phase

    Energy Technology Data Exchange (ETDEWEB)

    Weilenmann, U.

    2008-05-15

    In this project phase, an operating model of a tumble-dryer was built and tested. It dries laundry at pressures below atmospheric pressure. The operating model was equipped with numerous sensors such that all relevant data of the process could be recorded. The measurements reported in this document show that good and promising results were obtained with the functional model. The proposed concept of the vacuum tumble-dryer with heat recovery works well and the laundry can be dried in a gentle way. The laundry experiences temperatures not higher than 60 {sup o}C. Only few fluff balls appear. This implies a process which is kind to fabrics. During the testing the drying performance reached 2 kg water per hour. The goal of 3 kg water per hour was not achieved yet. The drying duration have not been determined yet. It seems possible that the drying duration of state-of-the-art tumble-dryers can be reached. The energy efficiency of the new process has still to be determined. Due to the demonstrated process stability - also without additional heating - energy class A is surpassable considering all available results. (author)

  17. Solar drying system for tropical fruits and a model for drying bananas in a static column dryer; Sistema de secagem solar para frutos tropicais e modelagem da secagem de banana em um secador de coluna estatica

    Energy Technology Data Exchange (ETDEWEB)

    Costa, Antonio Raimundo da Silva

    2008-01-15

    An electric solar dryer consisting of a solar collector, a drying chamber, an exhaust fan and a fan to promote forced hot air convection were projected, built and tested . Banana drying experiments were also carried out in a static column dryer to model the drying and to obtain parameters that can be used as a first approximation in the modeling of an electric solar dryer, depending on the similarity of the experimental conditions between the two drying systems. From the banana drying experiments conducted in the static column dryer, we obtained food weight data as a function of aqueous concentration and temperature. Simplified mathematical models of the banana drying were made, based on Fick's and Fourier's second equations, which were tested with the experimental data. We determined and/or modeled parameters such as banana moisture content, density, thin layer drying curves, equilibrium moisture content, molecular diffusivity of the water in banana D{sub AB}, extemal mass transfer coefficient k{sub M}, specific heat C{sub p}, thermal conductivity k, latent heat of water evaporation in the food L{sub food}, time to heat food, and minimum energy and power required to heat the food and evaporate the water. When we considered the shrinkage of radius R of a banana, the calculated values of D{sub AB} and k{sub M} generally better represent the phenomenon of water diffusion in a solid. The latent heat of water evaporation in the food L{sub food} calculated by modeling is higher than the latent heat of pure water evaporation L{sub water}. The values calculated for D{sub AB} and K{sub M} that best represent the drying were obtained with the analytical model of the present paper. These values had good agreement with those assessed with a numeric model described in the literature, in which convective boundary condition and food shrinkage are considered. Using parameters such as C{sub p}, D{sub AB}, k, k{sub M} and L{sub food}, one can elaborate the preliminary

  18. Evaluation of a pilot-scaled paddle dryer for the production of ethanol from lignocellulose including inhibitor removal and high-solids enzymatic hydrolysis

    Directory of Open Access Journals (Sweden)

    Egidio Viola

    2016-03-01

    Full Text Available The advantage of using paddle dryers (PD in the production of sugars and 2nd generation ethanol from pretreated wheat straw was investigated. This machinery was employed in order to detoxify steam-exploded substrates and to mix different slurries in the hydrolysis step. The obtained hydrolysate was fermented by the yeast Saccharomyces cerevisiae. Acetic acid and furfural were reduced up to 11 and 26 fold respectively in the detoxified substrate. When fermentation was carried out at low solid suspension, the use of PD was as effective as water extraction in detoxifying exploded biomass, giving ethanol yields of 90% at 0.05 solid/liquid ratio (S/L and 80% at 0.10 S/L. Moreover, by using PD the cellulose conversion yield was significantly improved in the hydrolysis step: when operating at higher S/L (0.4, the hydrolysis efficiency was twice the one achieved by using a bioreactor with a Rushton stirrer.

  19. Discussion about Measures for Energy Conservation of Steam Jet Veneer Dryers%喷气式网带单板干燥机节能途径探讨

    Institute of Scientific and Technical Information of China (English)

    吕坤; 梅玉春; 张建平

    2015-01-01

    In order to improve the energy efficiency during the veneer drying process, the analysis of the veneer drying pro-cess is analyzed, with effective energy-saving measures taken. The utilization of the system for recovering the waste heat from veneer dryer exhaust is put forward to reduce the heat loss due to the direct discharge of exhaust, realizing energy conserva-tion by means of recovery of waste heat from exhaust;the utilization of steam cascade to recover the heat from condensate wa-ter to realize energy conservation of waste heat from condensate water.%为了提高单板干燥过程中的能源利用效率,对单板干燥过程进行了分析并提出有效的节能措施与途径。提出利用单板干燥尾气余热回收系统,以减少尾气直接排入大气时的热量损失,对尾气余热回收利用;提出蒸汽梯级利用回收冷凝水的热量,达到对冷凝水余热回收利用的目的。

  20. Thermodynamic methodology for the design of solar dryers operated with flat solar collectors; Metodologia termodinamica para el diseno de secadores operados con calentadores solares planos

    Energy Technology Data Exchange (ETDEWEB)

    Torres Reyes, Ernestina; Navarrete Gonzalez, Jose L; Ibarra Salazar, Beatriz A; Picon Nunez, Martin [Instituto de Investigaciones Cientificas, Universidad de Guanajuato, Guanjuato, Guanajuato (Mexico)

    2000-07-01

    In this paper a thermal performance analysis of solar drying process at operating varying conditions is presented. It is described semi-empirical models to thermal characterization of an experimental device. A simulator of thermal performance for operating varying conditions was developed as a part of the procedure of thermal design of solar dryers. On the other hand, it is described a simplified method to design solar collectors based on the determination of minimum entropy generation during the thermal conversion of the solar device by using the thermal analysis procedure established and the method derived of the second law of the Thermodynamics are finally presented. [Spanish] En este trabajo se presenta el analisis termico del comportamiento del sistema -colector solar camara de secado-. Se describen los modelos semi-empiricos con los que se caracterizo termicamente un secador solar experimental del tipo indirecto. Se presenta tambien un procedimiento de diseno de equipo de secado que toma en cuenta las condiciones variables de operacion que presentan los dispositivos solares. Por otro lado se describe un procedimiento simplificado de diseno, basado en un analisis derivado de la segunda ley de la Termodinamica. Esta metodologia se fundamenta en la minima generacion de entropia durante la conversion termica de la energia solar, utilizando colectores solares planos. Finalmente se presentan los resultados del diseno preliminar de equipo de secado utilizando los dos procedimientos mencionados.

  1. PVC气流干燥装置进料工艺的改进%Improvement on the feeding process of PVC pneumatic dryer

    Institute of Scientific and Technical Information of China (English)

    熊新阳; 骆雁

    2011-01-01

    Improvements on the feeding process of PVC pneumatic dryer were introduced, and thc concrete mcasures wcrc as folllows: 1 rebuilding the blades of auger convcyors; 2 adding venturis to drying tubes under the feeding position;3 changing the fceding position of auger conveyors; 4 increasing purging at the top of auger conveyors. After improvement, the problems of accumulating materials at thc bottom of pneumatic drying tubes were solved, and thc first-rate quality percentage of impurity particle number was improved.%介绍了改进PVC气流干燥进料工艺的具体措施:①改造螺旋输送器桨叶,②在进料位置下部干燥管增加缩喉,③改变螺旋输送器的进料位置,④在螺旋输送器端部增加吹扫气。改造后彻底解决了气流干燥管底部积料的问题,杂质粒子数单项优等品率有所提高。

  2. Experimental Research on Drying Technology based on Vacuum Freezing Dryer%黄瓜片真空冷冻干燥试验

    Institute of Scientific and Technical Information of China (English)

    王慧贤

    2012-01-01

    Vacuum freeze-drying technology is a new kind of food processing method which integrates with vacuum technotogy, freezing ano drying technology. The principle of vacuum freeze-drying technology, drying technology and freeze-drying equipment were briefly introduced. Cucumber drying experiment by applying vacuum freezing dryer was mainly introduced, and the cucumber vacuum freeze-drying curve was plotted, and the changes of cucumber color, shape, and weight were contrasted before and after drying, which were analyzed by the software MATLAB and electronic balance, and then the average moisture content, drying rate and surface area shrinkage rate..%为优化黄瓜真空冷冻干燥工艺,以黄瓜片为试材,采用MATLAB软件分析黄瓜片真空冷冻干燥前后的质量、色泽、形状变化。试验结果表明:黄瓜的平均含水率为96.3%;干燥后的表面收缩率为0.332471;干燥前的r、g、b色度坐标值为0.3562、0.3595、0.2842,干燥后分别为0.2835、0.4295、0.2871。

  3. Mathematical modelling for the drying method and smoothing drying rate using cubic spline for seaweed Kappaphycus Striatum variety Durian in a solar dryer

    Energy Technology Data Exchange (ETDEWEB)

    M Ali, M. K., E-mail: majidkhankhan@ymail.com, E-mail: eutoco@gmail.com; Ruslan, M. H., E-mail: majidkhankhan@ymail.com, E-mail: eutoco@gmail.com [Solar Energy Research Institute (SERI), Universiti Kebangsaan Malaysia, 43600 UKM Bangi, Selangor (Malaysia); Muthuvalu, M. S., E-mail: sudaram-@yahoo.com, E-mail: jumat@ums.edu.my; Wong, J., E-mail: sudaram-@yahoo.com, E-mail: jumat@ums.edu.my [Unit Penyelidikan Rumpai Laut (UPRL), Sekolah Sains dan Teknologi, Universiti Malaysia Sabah, 88400 Kota Kinabalu, Sabah (Malaysia); Sulaiman, J., E-mail: ysuhaimi@ums.edu.my, E-mail: hafidzruslan@eng.ukm.my; Yasir, S. Md., E-mail: ysuhaimi@ums.edu.my, E-mail: hafidzruslan@eng.ukm.my [Program Matematik dengan Ekonomi, Sekolah Sains dan Teknologi, Universiti Malaysia Sabah, 88400 Kota Kinabalu, Sabah (Malaysia)

    2014-06-19

    The solar drying experiment of seaweed using Green V-Roof Hybrid Solar Drier (GVRHSD) was conducted in Semporna, Sabah under the metrological condition in Malaysia. Drying of sample seaweed in GVRHSD reduced the moisture content from about 93.4% to 8.2% in 4 days at average solar radiation of about 600W/m{sup 2} and mass flow rate about 0.5 kg/s. Generally the plots of drying rate need more smoothing compared moisture content data. Special cares is needed at low drying rates and moisture contents. It is shown the cubic spline (CS) have been found to be effective for moisture-time curves. The idea of this method consists of an approximation of data by a CS regression having first and second derivatives. The analytical differentiation of the spline regression permits the determination of instantaneous rate. The method of minimization of the functional of average risk was used successfully to solve the problem. This method permits to obtain the instantaneous rate to be obtained directly from the experimental data. The drying kinetics was fitted with six published exponential thin layer drying models. The models were fitted using the coefficient of determination (R{sup 2}), and root mean square error (RMSE). The modeling of models using raw data tested with the possible of exponential drying method. The result showed that the model from Two Term was found to be the best models describe the drying behavior. Besides that, the drying rate smoothed using CS shows to be effective method for moisture-time curves good estimators as well as for the missing moisture content data of seaweed Kappaphycus Striatum Variety Durian in Solar Dryer under the condition tested.

  4. Mathematical modelling for the drying method and smoothing drying rate using cubic spline for seaweed Kappaphycus Striatum variety Durian in a solar dryer

    Science.gov (United States)

    M Ali, M. K.; Ruslan, M. H.; Muthuvalu, M. S.; Wong, J.; Sulaiman, J.; Yasir, S. Md.

    2014-06-01

    The solar drying experiment of seaweed using Green V-Roof Hybrid Solar Drier (GVRHSD) was conducted in Semporna, Sabah under the metrological condition in Malaysia. Drying of sample seaweed in GVRHSD reduced the moisture content from about 93.4% to 8.2% in 4 days at average solar radiation of about 600W/m2 and mass flow rate about 0.5 kg/s. Generally the plots of drying rate need more smoothing compared moisture content data. Special cares is needed at low drying rates and moisture contents. It is shown the cubic spline (CS) have been found to be effective for moisture-time curves. The idea of this method consists of an approximation of data by a CS regression having first and second derivatives. The analytical differentiation of the spline regression permits the determination of instantaneous rate. The method of minimization of the functional of average risk was used successfully to solve the problem. This method permits to obtain the instantaneous rate to be obtained directly from the experimental data. The drying kinetics was fitted with six published exponential thin layer drying models. The models were fitted using the coefficient of determination (R2), and root mean square error (RMSE). The modeling of models using raw data tested with the possible of exponential drying method. The result showed that the model from Two Term was found to be the best models describe the drying behavior. Besides that, the drying rate smoothed using CS shows to be effective method for moisture-time curves good estimators as well as for the missing moisture content data of seaweed Kappaphycus Striatum Variety Durian in Solar Dryer under the condition tested.

  5. PRELIMINARY RESULTS USING ANEW METHOD TO OPTIMIZE A SPRAY DRYER PROCESS FOR PRODUCING HIGH QUALITY MILK POWDER FROM COW, GOAT AND SHE-ASS MILK CONCENTRATES

    Directory of Open Access Journals (Sweden)

    Giuseppe Altieri

    2008-12-01

    Full Text Available As quality is a very important factor in milk powder produced by drying, the optimal process must protect both nutritional and sensorial properties. Although heat damage indices (namely the insolubility index (IINS, thermal damage (IDT, protein denaturation could be used to evaluate the correct processing of milk, they are very time-consuming. Hence a chemical marker, like vitamin C, is proposed for rapid assessment of the overall damage to the quality of the produced milk powder. Trials were carried out on milk concentrates from cow, goat and she-ass so as to optimize the process performance of the spray dryer, for each kind of milk, at three inlet temperatures (120, 150, 185 °C; the feed flow rate was set at 0.5 dm3/h with outlet air RH% in the range 10-40%; raw milk was concentrated using a low pressure evaporator until an average level of 23% dry matter was reached. As expected, the thermal damage of the milk powder increased as the inlet air temperature increased; the outlet powder RH% was 96-98% poorly correlated with the mass flow rate of the concentrate inlet. Moreover, the destruction kinetic of vitamin C was found highly correlated with the thermal damage to the milk powder. At 175 °C inlet air temperature the overall thermal treatment on the she-ass milk concentrate, which is very heat-sensitive due to its high lactose content, was “weak” (IDT<80 and the milk powder of “premium or extra” quality (IINS<1.25ml and lactic acid = 0.07% < 0.15% ADMI. The titratable acidity values are uncorrelated with the process air temperature but depend uniquely from the raw milk freshness.

  6. Technical support document: Energy conservation standards for consumer products: Dishwashers, clothes washers, and clothes dryers including: Environmental impacts; regulatory impact analysis

    Energy Technology Data Exchange (ETDEWEB)

    1990-12-01

    The Energy Policy and Conservation Act as amended (P.L. 94-163), establishes energy conservation standards for 12 of the 13 types of consumer products specifically covered by the Act. The legislation requires the Department of Energy (DOE) to consider new or amended standards for these and other types of products at specified times. This Technical Support Document presents the methodology, data and results from the analysis of the energy and economic impacts of standards on dishwashers, clothes washers, and clothes dryers. The economic impact analysis is performed in five major areas: An Engineering Analysis, which establishes technical feasibility and product attributes including costs of design options to improve appliance efficiency. A Consumer Analysis at two levels: national aggregate impacts, and impacts on individuals. The national aggregate impacts include forecasts of appliance sales, efficiencies, energy use, and consumer expenditures. The individual impacts are analyzed by Life-Cycle Cost (LCC), Payback Periods, and Cost of Conserved Energy (CCE), which evaluate the savings in operating expenses relative to increases in purchase price; A Manufacturer Analysis, which provides an estimate of manufacturers' response to the proposed standards. Their response is quantified by changes in several measures of financial performance for a firm. An Industry Impact Analysis shows financial and competitive impacts on the appliance industry. A Utility Analysis that measures the impacts of the altered energy-consumption patterns on electric utilities. A Environmental Effects analysis, which estimates changes in emissions of carbon dioxide, sulfur oxides, and nitrogen oxides, due to reduced energy consumption in the home and at the power plant. A Regulatory Impact Analysis collects the results of all the analyses into the net benefits and costs from a national perspective. 47 figs., 171 tabs. (JF)

  7. 餐厨垃圾微波干燥实验装置%An Experimental Microwave Dryer for Disposing Food Wastes

    Institute of Scientific and Technical Information of China (English)

    原一高; 王欣欣; 张肖肖

    2012-01-01

    The pollution caused by food residue is increasingly serious, which has constituted a great threat to both environment and human health. Therefore, the dispose of food wastes in an energy-saving and environmentally friendly way, and turning the wastes into a useful resource is a problem confronting the environment protection workers. In this paper, based on the microwave heating technology and the characteristics of food wastes, an experimental microwave dryer for disposing food wastes was proposed. The experimental results show that the proposed device which is easy to operate and control can meet the test requirement of food residue processing. For disposing the food wastes of high water content, a combination of the drying process consisting of ventilation microwave in the initial drying phase and vacuum microwave in the final drying stage should be used. This paper is of reference and help for the design of microwave food wastes processing equipment.%为节能、环保地达到餐厨垃圾的处理目标,基于餐厨垃圾的特点,利用微波加热技术设计了一种餐厨垃圾微波干燥装置,并进行了餐厨垃圾的微波干燥实验.结果表明,该装置操作简单,便于控制,可以满足餐厨垃圾的处理要求;对含水率很高的餐厨垃圾进行微波干燥处理,宜采用前期微波通风与后期微波真空的组合干燥方式.研究结论可为餐厨垃圾微波处理设备的设计提供参考依据.

  8. Combustion and regulations. Impacts of new regulations on medium-power thermal equipment (boilers, engines, turbines, dryers and furnaces); Combustion et reglementation. Incidences des nouvelles reglementations sur les equipements thermiques de moyenne puissance (chaudieres, moteurs, turbines, secheurs et fours)

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1997-12-31

    This conference is composed of 20 papers on the influence of French and European new pollution regulations on medium size thermal equipment such as boilers, engines, turbines, dryers and furnaces. It is discussed what is going to change with new regulations, how they will apply to existing plants, what will be the impact on future equipment costs. The evolution of energy suppliers and equipment manufacturers facing these new regulations is also examined: fuel substitution, improvements in turbines and engines with water injection and special chambers, diesel engine control, lean mixtures and electronic control for gas engines... Means for reducing SOx, NOx and ash emission levels in boilers are also examined

  9. Drying of mango pulp in a dryer of laboratory tunnel type; Secado de pulpa de mango en un secador de laboratorio tipo tunel

    Energy Technology Data Exchange (ETDEWEB)

    Pacheco Resendiz, Oscar; Chagoyan Serrano, Jose; Flores I, Alfredo; Rodriguez M, Jose A [Universidad Autonoma de Baja California Sur (Mexico)

    2000-07-01

    The result of four tests of drying of mango pulp Kent are presented, which were carried out in a dryer of the tunnel type in constant conditions of temperature, speed and absolute humidity of the air. The temperatures at which the tests were conducted were 35, 40, 45 and 50 Celsius degrees. The average speed of the drying air was 2.35 m/s. For the four tests the drying variables were measured for the purpose of controlling the process. The tests were suspended after 10 hours. The initial and final moisture contents of the samples on a wet weight basis for the test at 35 were 87.04% and 58.94% for that at 40 were 87.42% and 17.25%, for that at 45 were 87.55% and 13.29%, and for that at 50 were 87.43% and 48%. The graphs of the evolution of moisture content of the samples dried under the specified conditions are compared. [Spanish] Se presentan los resultados de cuatro pruebas de secado de pulpa de mango Kent, las cuales se realizaron en un secador tipo tunel en condiciones constantes de temperatura, velocidad y humedad absoluta del aire. Las temperaturas empleadas fueron 35, 40, 45 y 50 grados Celsius y la velocidad del aire de secado fue de 2.35 m/s. Para las cuatro pruebas se midieron las variables de secado mencionadas con el fin de controlar el proceso. Las pruebas se suspendieron al cumplirse 10 h. Las humedades inicial y final base humeda de las muestras para la prueba de 35 fueron 87.04% y 58.94%, para la de 40 fueron 87.42% y 17.25% y para la de 45 fueron de 87.55% y 13.29% y para la de 50 fueron de 87.43% y 48%. Se comparan entre si las graficas de la evolucion del contenido de humedad de las muestras que se secaron a las condiciones ya mencionadas.

  10. Calculation and optimization of the copper (II sulphate monohydrate from copper (II sulphate pentahydrate production process in a fluidized bed dryer

    Directory of Open Access Journals (Sweden)

    Kaluđerović-Radoičić Tatjana

    2015-01-01

    Pro Designer 5.1 facilitates modeling, evaluation and optimization of different industrial processes including drying. These softwares were applied for the calculation of the air flow rate, heat exchange and for the scoping of a dryer.

  11. Research of Vibration Device of Fresh Apricot Dryer based on Infrared Ray%基于红外线的鲜杏干燥机振动装置研究

    Institute of Scientific and Technical Information of China (English)

    王玉陇; 姚伟; 史增录; 张学军; 孙杰; 沈唯; 冯一洪

    2014-01-01

    The infrared radiation heat flux density of drying process is high, resulting in uneven heating of fresh apricot-sided, which af-fects the drying quality. The vibration device of fresh apricot dryer was designed. Dynamics analysis of the dryer vibration device was made and experiments were conducted to test the maximum vibration velocity of fresh apricot on the vibration device with a view of pro-viding a theoretical basis for the design and improvement of the vibration device.%针对红外辐射干燥过程中辐射的热流密度高,造成鲜杏单面受热出现阴阳面,影响干燥品质等问题,设计一种鲜杏干燥机的振动装置。通过对干燥机振动装置的动力学分析,以及鲜杏在振动装置上可承受的最大振动速度的分析与试验,为振动装置的设计及改进提供理论依据。

  12. Numerical simulation analysis of temperature and velocity field of automatic umbrella dryer%自动干伞机温度场和流场数值模拟分析

    Institute of Scientific and Technical Information of China (English)

    徐逢; 胡勇

    2014-01-01

    The working principle and design scheme of automatic umbrella dryer are introduced in this paper.The temperature field and velocity field of the inner automatic umbrella dryerare analyzed using Solidworks Flow Simulation.The results show that the tempera-ture distribution is homogeneity and the highest temperature is 40℃where the wind speed is low which is too far to hurt the umbrella. The final results show that the structure of automatic umbrella dryer is reasonable and have fine application market.%文章介绍了一种雨伞干燥装置的设计方案和工作原理。通过Solidworks Flow Simulation进行了机厢内温度场及速度场分析,表明厢内温度分布较均匀,在风速较低的局部区域温度40℃左右,远未达到伞面破坏温度,方案结构设计比较合理,具有市场推广应用价值。

  13. Design and application of a mini all-weather solar dryer%小型全天候太阳能干燥机的设计及应用

    Institute of Scientific and Technical Information of China (English)

    李汴生; 申晓曦; 刘伟涛; 阮征

    2011-01-01

    In order to solve the problems in traditional drying technology of preserved fruits, a mini all-weather solar dryer was designed and manufactured based on characteristics and requirements of preserved fruits produced in Guangdong province. The solar dryer is composed of heat-collection plate, drying chamber and blower. It can collect sun radiation to heat air and water, store heat through hot water tank. It also has an assistant heating system in water tank.Forced air convective drying, natural convective drying and greenhouse drying can be reached by the designed dryer.The experiments of drying Ganshimei (intermediate moisture salted plum) were carried out to test the dryer's performance. The working efficiency of heat-collection plate and drying chamber, the material balance and energy consumption of the drying system were calculated. And the parameters of the dryer were determined. The total drying efficiency of the forced air convective drying reached to a high level of 63.40%.Comparing with the traditional open sun drying, the drying rate of the forced air convective drying was 9.99 g/(100 g·h), which was 201.2% of the open sun drying's. And the drying time of the forced air convective drying was 12 h, much less than 50 h of the open sun drying's.Meanwhile the sugar and acid content loss of the forced air convective drying samples were less than that of the open sun drying samples.%为了解决凉果传统自然日晒干燥中存在的干燥过程耗时长,占地面积大、受天气控制和环境条件影响等问题,根据凉果的特性和干燥要求,设计研制了小型全天候太阳能干燥机.设备由集热器、干燥室和鼓风机等主要部分组成,具有集热、贮能和辅助加热等功能,可实现强制对流干燥、自然对流干燥和温室干燥等干燥模式.以干湿梅作为样品进行了干燥机的干燥性能试验,对干燥机集热器和干燥室的工作效率进行了计算、对干燥过程中的物料及能量

  14. 豇豆隧道式热风干燥特性和模型%Drying characteristics and model of cowpea in tunnel hot air dryer

    Institute of Scientific and Technical Information of China (English)

    师建芳; 吴辉煌; 娄正; 吴中华; 刘清

    2013-01-01

    Cowpea, also known as beans, black-eyed peas, is an important leguminous vegetable, which is extensively grown in China. Fresh cowpeas having relatively high moisture content must be distributed to customers or processed as quickly as possible in order to prevent microbial fermentation and thermal degradation. Cowpeas resources have great losses as which are putrescible at normal temperatures and pressures, and this severely limits the transportation, storage and process of cowpea, therefore the development of cowpea deep processing is necessary. As Asian people have the habit of eating dried vegetables such as dried cowpea, drying can not only solve the serious problem of huge losses, but also create more economic benefits for farmers;and because most of deep processing technology needs dried cowpea, drying is of great importance as a preprocessing method. The tunnel type of hot air drying technology has been widely utilized in the drying of carrots, preserved fruits, and plums etc. In this paper, hot air drying characteristics and a drying model of tunnel type of hot air drying technology was studied in drying Cowpea, in order to establish the best model to simulate and predict the water ratio and to provide a technical basis for the industrial application of the control and prediction of the drying process and the tunnel type of hot air drying for cowpea. The tunnel dryer was made by the Institute of Agricultural Product Processing, Chinese Academy of Agricultural Engineering and College of Mechanical Engineering, Tianjin University of Science and Technology. According to the pre-test results, the drying characteristics of Cowpea was investigated under different air temperatures (70℃、80℃and 90℃), air velocities (0.3、0.4 and 0.5 m/s) and material thickness (6 mm、18 mm and 30 mm). The empirical relationships between Cowpea moisture then natural logarithmic lnMR and drying time, water effective diffusion coefficient Deff and drying air temperature was

  15. Secagem de extratos de erva-mate em secador por atomização Drying of maté extract in spray dryer

    Directory of Open Access Journals (Sweden)

    Alice Teresa Valduga

    2003-08-01

    Full Text Available Efetuou-se a extração de solúveis de erva-mate, progênie Cambona 4, utilizando extrator com percolação de solvente (água. O extrato obtido apresentou uma concentração de sólidos de aproximadamente 3%. Ao extrato foi adicionada goma arábica nas concentrações de 0; 0,2; 0,4; 0,6; 0,8; 1,0; 1,5 e 2,0%, em relação aos sólidos contidos no mesmo. As misturas foram efetuadas com o objetivo de estudar a influência da goma arábica na secagem e no sabor das bebidas. Os extratos foram processados em secador por atomização nas condições operacionais médias: temperatura e vazão do ar: 190ºC e 32,1m³/h; alimentação de extrato 340mL/h. Os conteúdos de umidade do pó obtido variaram de 1,8 a 6,6%(bu. Efetuou-se análise sensorial de três formulações com concentrações: 0; 0,2 e 1,0%. Aos resultados experimentais aplicou-se tratamento estatístico e verificou-se maior preferência pela formulação contendo 0,2% de erva-mate, o que mostrou a influência do agente encapsulante na retenção de aromas.It was effected extraction of soluble of mate, lineage Cambona 4, using extracting, with percolating of solvent (water. The gotten extract presented a 3% solid concentration. The extract was used for formularization of mixtures with arabica gum in the concentrations of 0; 0.2; 0.4; 0.6; 0.8; 1.0; 1.5 and 2.0%, in relation to solids contained in the extract. The formularizations had been effected with the objective to study the volatile and aromatics substance clamping. The extracts had been processed in spray dryer in the average operational conditions: temperature and tax of air: 190ºC and 32.1m³/h; extract feed of 340mL/h. The contents of humidity of the gotten dust had varied of 1.8 to 6.6%(db. Sensorial analysis of three formularizations with concentrations was carried out: 0; 0.2 and 1.0%. A statistical analysis were carried out to experimental results and was verified bigger preference for the formularization contends 0,2% of

  16. Application of Heating Technology for Heat Transfer Oil in Veneer Dryer%导热油加热技术在单板干燥机上的应用

    Institute of Scientific and Technical Information of China (English)

    吕继文; 浦卫清; 纪建伟; 章文达

    2014-01-01

    通过BG134辊筒式单板干燥机热耗量计算、导热油炉选择、供热管线布置和换热器设计,介绍导热油加热技术在辊筒式单板干燥机上的应用,为胶合板生产技术改造和增产节能提供参考。%This article introduced the heating technology for heat transfer oils in roler veneer drying via heat consumption of roler veneer dryer BG134. This national key technology promotion project chose heat oil oven management for heating pipes and design of heat exchanger. It provided theoretical support for optimizing technology of veneer production line and increased capacity with lower consumption.

  17. 高速纸机烘缸轴承过早失效分析及改善研究%The premature failure analysis of dryer bearings for high speed paper machines and its service life improvement

    Institute of Scientific and Technical Information of China (English)

    张笑如; 朱晓广; 张辉

    2014-01-01

    Based on the fault vibration frequency spectrums got with the dynamic vibration monitoring and fault diagnosis as well as the lubricating oil characteristics, the condition of drying cylinder bearings and the bearing premature failure mechanism were studied. The results show that the lubricating requirement of the dryer bearings is more rigorous than other rolls’ bearings; the premature failure appears due to lubrication failure. Under the lubricating oil kept unchanged, increasing the temperature difference between inlet and outlet of lubricating oil, increasing the lubricating oil lfow can carry away more heat from the working bearing, which can increase the viscosity of the lubricating oil to form oil iflm comparatively and extend the service life of the dryer bearings.%利用振动监测与故障诊断技术和油品分析技术对高速纸机前干燥部烘缸轴承进行监测跟踪,并对烘缸轴承的过早失效机理进行了研究。结果表明:烘缸轴承对润滑要求非常苟刻;润滑失效可致其过早失效;在不改变润滑油型号前提下,增大烘缸轴承座进油、排油温差,增大循环润滑油流量,促进带走烘缸轴承运行产生的热量,使润滑油工作实际黏度相对增加,有利于润滑油膜形成,从而延长烘缸轴承使用寿命。

  18. Cinética e modelagem da secagem de carambola (Averrhoa carambola L. em secador de bandeja = Kinetics and modeling of star fruit (Averrhoa carambola L. drying in a tray dryer

    Directory of Open Access Journals (Sweden)

    Paulo Bonomo

    2010-07-01

    Full Text Available No presente trabalho, objetivou-se obter curvas de secagem de carambola (Averrhoa carambola L. em secador de bandejas. A partir dessas curvas foram obtidos dados de taxa de secagem e de difusividade, além do ajuste de modelos semiteóricos aos dados experimentais. As curvas de secagem foram obtidas, utilizando-se um secador de bandejas nas temperaturas de 50, 60 e 70°C e com fluxo de ar de 1,5 m s-1. Aos dados experimentais foram ajustados os modelos dePage, Henderson e Pabis e Exponencial, utilizando-se regressão não-linear. Todos os ajustes tiveram coeficiente de determinação (R2 superior a 0,96, mas o modelo de Page foi o que apresentou melhor ajuste. Observou-se que a difusividade efetiva, calculada a partir da lei de Fick, aumentou com a elevação da temperatura.In this work, drying curves were obtained for the star fruit (Averrhoa carambola L. in a tray dryer. From theses curves, drying rates and diffusivity data were also obtained and semitheoreticalmodels were adjusted. The drying curves were obtained using a tray dryer with temperatures of 50, 60 and 70°C and an air flux of 1.5 m s-1. The Page, Henderson & Pabis and Exponential models were fitted to the experimental data by non-linear regression. All fitted models presented high determination coefficients (R2. The Page model showed the best fit. It was observed that effective diffusivity, calculated by Fick’s law, increased with temperature.

  19. 间接加热式列管回转干燥机传热系数模型构建%Modeling for heat transfer coefficient in indirect-heating tube rotary dryer

    Institute of Scientific and Technical Information of China (English)

    吴静; 李选友※; 陈宝明; 王瑞雪; 马晓旭; 高玲

    2013-01-01

      传热系数是列管回转干燥机设计和热工计算所必须的至关重要的设计参数之一,其精度的高低决定了干燥机尺寸、结构设计以及操作参数的合理性。目前还没有一种能够确切描述其加热管与物料颗粒传热过程的可靠而实用的传热模型。该文在对列管回转干燥机传热机理分析的基础上,提出了列管与颗粒间换热的基本构成为:列管管壁与气体介质间对流、气体介质与颗粒间的导热以及列管管壁与颗粒间的辐射换热;通过对列管回转干燥机内料层膨胀的试验研究,分析了颗粒对列管气膜边界层的影响;在此基础上,建立了预测列管外壁与颗粒间总传热系数的数学模型,并以2 mm直径的陶瓷球为物料,在6个转速条件下测量了管壁与颗粒间的换热系数,对模型进行验证;试验结果表明,模型预测的误差小于13%,可满足工程计算的精度要求。研究结果可为列管回转干燥机传热机理的深入研究提供参考。%  Heat transfer coefficient is one of the most crucial parameters in thermal calculation and design for a tube rotary dryer. The dimension, structure and operating parameters of a suitably designed dryer rely on the accuracy of the employed heat transfer coefficient. Because of the existence of tubes, particles’ motion behavior and heat transfer mechanism in a tube rotary dryer are more complicated than in a conventional rotary dryer. So far, there is no reliable heat transfer model to describe the heat transfer process between the tubes’ surface and particles in a tube rotary dryer. As a result, the main approach of heat transfer coefficient determination is still an experimental test. The main reason is the insufficiency of understanding on the mechanism of heat transfer between heating tube’s surface and particles. Our experimental investigation showed that heat transfer between tubes’ surface and

  20. Long-Term Carbon Injection Field Test for 90% Mercury Removal for a PRB Unit a Spray Dryer and Fabric Filter

    Energy Technology Data Exchange (ETDEWEB)

    Sjostrom, Sharon; Amrhein, Jerry

    2009-04-30

    The power industry in the U.S. is faced with meeting regulations to reduce the emissions of mercury compounds from coal-fired plants. Injecting a sorbent such as powdered activated carbon (PAC) into the flue gas represents one of the simplest and most mature approaches to controlling mercury emissions from coal-fired boilers. The purpose of this test program was to evaluate the long-term mercury removal capability, long-term mercury emissions variability, and operating and maintenance (O&M) costs associated with sorbent injection on a configuration being considered for many new plants. Testing was conducted by ADA Environmental Solutions (ADA) at Rocky Mountain Power’s (RMP) Hardin Station through funding provided by DOE/NETL, RMP, and other industry partners. The Hardin Station is a new plant rated at 121 MW gross that was first brought online in April of 2006. Hardin fires a Powder River Basin (PRB) coal and is configured with selective catalytic reduction (SCR) for NOx control, a spray dryer absorber (SDA) for SO2 control, and a fabric filter (FF) for particulate control. Based upon previous testing at PRB sites with SCRs, very little additional mercury oxidation from the SCR was expected at Hardin. In addition, based upon results from DOE/NETL Phase II Round I testing at Holcomb Station and results from similarly configured sites, low native mercury removal was expected across the SDA and FF. The main goal of this project was met—sorbent injection was used to economically and effectively achieve 90% mercury control as measured from the air heater (AH) outlet to the stack for a period of ten months. This goal was achieved with DARCO® Hg-LH, Calgon FLUEPAC®-MC PLUS and ADA Power PAC PREMIUM brominated activated carbons at nominal loadings of 1.5–2.5 lb/MMacf. An economic analysis determined the twenty-year levelized cost to be 0.87 mills/kW-hr, or $15,000/lb Hg removed. No detrimental effects on other equipment or plant operations were observed. The

  1. Pemodelan Matematik Kinerja Pengering Surya Efek Rumah Kaca (ERK-Hibrid Menggunakan Rak Berputar secara Vertikal (Mathematical Modeling Performance of Greenhouse Effect (GHE-Hybrid Solar Dryer with a Vertical Rotating Rack

    Directory of Open Access Journals (Sweden)

    Sigit Triwahyudi

    2016-12-01

    Full Text Available This paper presents a performance test and mathematical modeling of greenhouse effect (GHE-Hybrid solar dryer with vertical rotating rack. The dryer consists of a greenhouse dryer (1100 × 860 × 1300 mm with eight rack and additional heating system consists of a flat plate collector (1,04 m2, a hot water storage tank (197 liters and a heat exchanger. To investigate the performance of solar greenhouse dryer, five experimental variation speed of rack were conducted (1, 4, 7, 10 rpm and without rotation. Materials used in the experiment are local cardamom (Amomum cardamomum Wild. Weight of each experiment  about  9 to 10 kg. The average temperature of the hot water storage tank varies from 50.0 to 55.0 °C, drying air  temperature between 38.9 to 45.9 °C, while the relative humidity (RH of drying chamber ranged from 32.1 to 47.4 %. Variation of rotational speed affects on the uniformity of product temperature and water content in each rack drying. At rotation 1 rpm  (experiment II, obtained  as the best conditions (temperature and moisture content are most uniform. Increasing rotational speed of rack causes increasing in standard deviation of  product temperature and moisture content. To simulate the performance of the dryer, mathematical modeling based on heat  and mass transfer and a thin layer drying  approaches were conducted. Equations solved numerically using the finite difference Euler with Visual Basic Application (VBA program on Excel. Validation was conducted by comparing the calculation results of mathematical modeling (data prediction with measurement data (data observation. Criterion validity was determined by  the value of the coefficient of determination (R2, the value of RMSD and MAPD. Mathematical models that have been developed can be described precisely the temperature of the hot water storage tank, temperature of the drying chamber, temperature of the product as well as a moisture content decrease.   ABSTRAK Makalah

  2. Long-Term Carbon Injection Field Test for 90% Mercury Removal for a PRB Unit a Spray Dryer and Fabric Filter

    Energy Technology Data Exchange (ETDEWEB)

    Sjostrom, Sharon; Amrhein, Jerry

    2009-04-30

    The power industry in the U.S. is faced with meeting regulations to reduce the emissions of mercury compounds from coal-fired plants. Injecting a sorbent such as powdered activated carbon (PAC) into the flue gas represents one of the simplest and most mature approaches to controlling mercury emissions from coal-fired boilers. The purpose of this test program was to evaluate the long-term mercury removal capability, long-term mercury emissions variability, and operating and maintenance (O&M) costs associated with sorbent injection on a configuration being considered for many new plants. Testing was conducted by ADA Environmental Solutions (ADA) at Rocky Mountain Power’s (RMP) Hardin Station through funding provided by DOE/NETL, RMP, and other industry partners. The Hardin Station is a new plant rated at 121 MW gross that was first brought online in April of 2006. Hardin fires a Powder River Basin (PRB) coal and is configured with selective catalytic reduction (SCR) for NOx control, a spray dryer absorber (SDA) for SO2 control, and a fabric filter (FF) for particulate control. Based upon previous testing at PRB sites with SCRs, very little additional mercury oxidation from the SCR was expected at Hardin. In addition, based upon results from DOE/NETL Phase II Round I testing at Holcomb Station and results from similarly configured sites, low native mercury removal was expected across the SDA and FF. The main goal of this project was met—sorbent injection was used to economically and effectively achieve 90% mercury control as measured from the air heater (AH) outlet to the stack for a period of ten months. This goal was achieved with DARCO® Hg-LH, Calgon FLUEPAC®-MC PLUS and ADA Power PAC PREMIUM brominated activated carbons at nominal loadings of 1.5–2.5 lb/MMacf. An economic analysis determined the twenty-year levelized cost to be 0.87 mills/kW-hr, or $15,000/lb Hg removed. No detrimental effects on other equipment or plant operations were observed. The

  3. CO2充入量对小型热泵干燥机性能的影响%Effect of CO2 filling amount on performance of small heat pump dryer

    Institute of Scientific and Technical Information of China (English)

    杨道龙; 李娟玲; 姬长英; 何艳东

    2016-01-01

    【目的】探究CO2充入量与热泵干燥机系统功率、干燥室内温度、系统性能系数的关系,获得CO2最佳充入量。【方法】根据实际生产要求分析热泵干燥机的工作原理,搭建CO2热泵干燥试验平台;使用PLC采集数据和设计监测系统;进行CO2充入量试验。【结果】当CO2充入量为2.5 kg时,该系统功率达1200 W,干燥室内温度较高,达70℃,系统的能耗比(COP)为3.89,单位时间除湿量为1.636 kg·h-1。此时冷却器和蒸发器压力适宜,进出口温差较大。【结论】该系统能源利用率高,性能优。%Objective] To explore the relationship between CO2 filling amount and the performances of the heat pump dryer system including the system power, the drying chamber temperature and the system performance coefficient, and to determine the optimal CO2 filling amount.[Method]The working princi-ples of the heat pump dryer were analyzed according to the actual production requirements. The CO2 heat pump drying experimental platform was established. Data collection and monitoring system design were conducted by PLC. CO2 filling experiments were performed.[Result]When the CO2 filling amount was 2. 5 kg, the system power reached 1 200 W, the drying chamber temperature reached 70 ℃, the energy consumption rate (COP) was 3. 89, the dehumidification rate was 1. 636 kg·h-1, the pressures of the cooler and evaporator were suitable, and the temperature difference between inlet and outlet was relatively large.[Conclusion]This system has high energy efficiency and excellent performance.

  4. Secagem do Polissacarídeo l-Carragena Usando um Leito de Jorro Fluidizado Bidimensional Drying of l-Carrageenan Using a Two Dimensional Spouted Fluidized Bed Dryer

    Directory of Open Access Journals (Sweden)

    Héctor José Ciro Velásquez

    2012-06-01

    Full Text Available Resumo. Suspensões de l-carragena foram secas usando um secador de leito de jorro fluidizado bidimensional com partículas inertesplásticas de ABS (acrilonitrilo-butadieno-estireno. O desempenho do secador (produção de pó e retenção de sólidos e qualidade do produto seco obtido (propriedades reológicas e teor de umidade foi avaliado. Os resultados mostraram que a eficiência de produção média de pó foi de 23% com uma retenção média de 71%. A variável mais relevante na secagem das suspensões foi a vazão de alimentação, sendo que um aumento desta variável produziu um baixo rendimento de pó e aumentou a retenção de sólidos dentro do leito. O produto reconstituído de l-carragena obtido nas condições otimizadas de secagem formou suspensões de natureza altamente pseudoplástica, porém com propriedades viscoelásticas características de suspensões altamente diluídas (G''>G', mostrando valores de viscosidade, módulos elástico (G' e de perda (G'' menores que o produto comercial.Abstract. l-carrageenan suspensions were dried using a two dimensional spouted fluidized bed dryer with inert particles of ABS (acrylonitrile butadine styrene. The dryer performance (powder production and solid retention and quality properties of final product (rheological properties and moisture content were evaluated. According to results the mean powder production of l-carrageenan using ABS as inert particle was of 23% with a solid retention of 71%. The most significant variable in the drying of suspension was the feed mass flow rate, as its increase produced a diminishing of the powder production and increasing of the solids retention in the bed. The reconstituted suspensions of l-carrageenan obtained from optimized conditions of drying formed highly pseudoplastic suspensions with viscoelastic properties of highly diluted (G''>G' systems. In addition, the rheological characteristics as viscosity, storage (G' and loss moduli (G'' were lower

  5. NIR spectroscopic method for the in-line moisture assessment during drying in a six-segmented fluid bed dryer of a continuous tablet production line: Validation of quantifying abilities and uncertainty assessment.

    Science.gov (United States)

    Fonteyne, Margot; Arruabarrena, Julen; de Beer, Jacques; Hellings, Mario; Van Den Kerkhof, Tom; Burggraeve, Anneleen; Vervaet, Chris; Remon, Jean Paul; De Beer, Thomas

    2014-11-01

    This study focuses on the thorough validation of an in-line NIR based moisture quantification method in the six-segmented fluid bed dryer of a continuous from-powder-to-tablet manufacturing line (ConsiGma™ 25, GEA Pharma Systems nv, Wommelgem, Belgium). The moisture assessment ability of an FT-NIR spectrometer (Matrix™-F Duplex, Bruker Optics Ltd, UK) equipped with a fiber-optic Lighthouse Probe™ (LHP, GEA Pharma Systems nv, Wommelgem, Belgium) was investigated. Although NIR spectroscopy is a widely used technique for in-process moisture determination, a minority of NIR spectroscopy methods is thoroughly validated. A moisture quantification PLS model was developed. Twenty calibration experiments were conducted, during which spectra were collected at-line and then regressed versus the corresponding residual moisture values obtained via Karl Fischer measurements. The developed NIR moisture quantification model was then validated by calculating the accuracy profiles on the basis of the analysis results of independent in-line validation experiments. Furthermore, as the aim of the NIR method is to replace the destructive, time-consuming Karl Fischer titration, it was statistically demonstrated that the new NIR method performs at least as good as the Karl Fischer reference method.

  6. Caracterização e processamento de leite bubalino em pó em secador por nebulização Characterization and processing of powdered buffalo milk by spray dryer

    Directory of Open Access Journals (Sweden)

    Roberta B. Guerra

    2005-09-01

    Full Text Available Avaliou-se o processo de secagem por nebulização em "spray dryer" para a obtenção de leite bubalino em pó. Foram realizadas análises físico-químicas no leite in natura e no leite desidratado, para averiguar perdas de macronutrientes ocorridas durante a secagem; análises microbiológicas para assegurar a qualidade higiênico-sanitária do processo e produto e análises sensoriais para estabelecer a aceitabilidade do produto. Foram obtidas isotermas de adsorção e dessorção de umidade a 25°C, para o produto em pó, visando observar o seu comportamento higroscópico. O leite bubalino em pó obtido apresentou como características físicoquímicas: 3,4% de umidade, 23,2% de proteínas, 46,1% de gordura, 4,2% de cinzas, 0,5% de lecitina de soja e 22,6% de carboidratos totais. De acordo com os exames microbiológicos está apto para o consumo humano. O produto foi caracterizado como integral por não ter sofrido qualquer padronização. As perdas ocorridas para a maioria dos macronutrientes durante o processamento, foram inferiores a 5% e apenas o teor de proteínas apresentou variação superior a 15%, devido à desnaturação da caseína em temperatura superior a 80°C. O produto apresentou isotermas de adsorção do tipo III, mesmo comportamento apresentado pelo leite bovino. Através da isoterma de dessorção determinou-se o valor de umidade equivalente à monocamada, obtendo-se o valor médio de 4,4g H2 O/100g b.s., o que validou o processo utilizado. O comportamento de histerese apresentado pelo produto foi similar ao do leite em pó integral, sendo a sua aceitabilidade de 74%, muito próxima a 80% obtido para um leite em pó integral comercial.This work aims to show the process development based on the spray dryer for the obtaining of powdered buffalo milk. For that, physiochemical analyses were made in the milk in natura and later in the powdered product, which was also submitted to microbiological analysis to be sure that it

  7. Study of response surface optimization design of tube plate type dryer process%管板式烘丝机工艺参数对卷烟香气的影响

    Institute of Scientific and Technical Information of China (English)

    韦小玲; 康金岭

    2012-01-01

    In order to use cigarette aroma sensory quality evaluation scores as a indicators, based on the result of single factor study, four factors and three levels of response surface analysis in cigarette production process pipe plate dryer drying parameters were researched on the cigarette aroma and the effect of optimum parameter configuration. The result showed that, the temperature of the tube wall, the tide discharging opening, ( drying cylinder ) entrance temperature on cigarette aroma significantly, the establishment of two regression e-quations, significant and effective model, optimal production process were: the cylinder wall temperature of 142 ℃ , the hot air temperature of 95 ℃ , the entrance temperature of 81 ℃ , the humidity of discharging opening 50%. In this condition, the cigarette aroma sensory quality evaluation scores was the hightest than others.%以卷烟香气感官质量评分为指标,在单因素试验的基础上,运用四因素三水平的响应曲面分析法,研究卷烟生产过程中管板式烘丝机烘丝工艺参数对卷烟香气的影响.结果表明,筒壁温度、排潮开度、(烘丝筒)入口温度对卷烟香气影响显著,建立二次回归方程,模型显著且有效,最佳生产工艺为筒壁温度142℃,热风温度95℃,入口温度81℃,排湖开度50%,该条件下,卷烟香气感官质量评价得分最高.

  8. Automatización de un Secador Convectivo de Aire Caliente para fines de Docencia en Ingeniería de Alimentos Automation of a Convective Hot Air Dryer for Teaching in Food Engineering

    Directory of Open Access Journals (Sweden)

    Jorge A Saavedra

    2008-01-01

    Full Text Available El presente trabajo describe el diseño y montaje de un dispositivo experimental para la automatización de un secador de aire caliente con flujo paralelo en co-corriente para realizar estudios de secado. El desarrollo del trabajo se dividió en dos actividades principales: (i diseño del sistema de automatización y (ii la validación de los datos entregados por el equipo. Se obtuvo un dispositivo capaz de registrar las variables del proceso de secado y de la imagen de la muestra deshidratada en tiempo real, como así mismo transmitir dicha información a través de Internet. Los datos procesados por el sistema automático comparados con experiencias manuales tradicionales (no automatizadas se validaron estadísticamente. Se concluye finalmente que la propuesta es viable, fiable y atractiva para el usuario por lo que facilita el proceso de enseñanza-aprendizaje en un área de especial importancia en Ingeniería de Alimentos.This paper describes the design and installation of an automated experimental device applied to a parallel co-current hot air dryer to perform drying studies in the field of food engineering. The development of this work was divided into two main activities: (i design of the automation system and (ii validation of automatically collected data. A device capable of collecting and registering real time data and images from drying processes, and transmitting them through Internet was obtained. The data processed by the automatic device was statistically validated. It is concluded that the proposed automation device is feasible, reliable and attractive for the users, facilitating the teaching-learning process in an important area of Food Engineering.

  9. First test results of the pilot plant for the pressure loaded vapour loaded fluidized bed drying process (DDWT) of brown coals. A pilot plant for 5 t/h dry coal and till 6 bar dryer pressure; Erste Testergebnisse von der Versuchsanlage zur Druckaufgeladenen Dampfwirbelschicht-Trocknung (DDWT) von Braunkohlen. Versuchsanlage fuer 5 t/h Trockenkohle und bis 6 bar Trocknerdruck

    Energy Technology Data Exchange (ETDEWEB)

    Porsche, T.; Thannhaeuser, L.; Hoehne, O.; Martin, J.S. [Vattenfall Europe Generation AG, Cottbus (Germany)

    2009-07-01

    Apart from other promising possibilities for the improvement of the efficiency of fossil fuelled power stations such as the improvement of the steam parameters and optimization of the equipment technology the preliminary drying of coal possesses a very high potential. This results from a more effective combustion of the dried coal in the power station boiler and from the energetic use of the condensation enthalpy of the coal water vapour during processing the power station. Especially, if the vapour steam is on a high level of pressure, the applied evaporation enthalpy completely can be led back into the power station process. Thereby, improvements of the net efficiency of power stations of about 4 to 5 % are attainable. Starting from October 2008, Vattenfall Europe AG (Berlin, Federal Republic of Germany) established a pilot plant for a vapour loaded fluidized bed drying process (DDWT) of brown coals at the site Schwarze Pumpe. The plant is laid out for a dryer performance of 5 t/h dry brown coal. This plant enables tests with a dryer system pressure between 1 and 6 bar. After start-up in the third quarter 2008, the operation of the pilot plant begun. Extensive tests of the plant and components were accomplished, and the procedure proof for DDWT of Lausitz brown coals was furnished. So far, up to 4 t/h dry coal were produced with the accomplished test campaigns. A dryer system pressure of up to 4.5 bar started. The target is to transfer the results and experiences from the test operation into planning and construction of a 250 MW{sub e}l Oxyfuel demonstration power station with upstream coal pressure drying process which is established by Vattenfall Europe AG at the location Jaenschwalde until 2015.

  10. DRUM DRYER FOR DRYING THE PARTICULATE PRODUCTS

    Directory of Open Access Journals (Sweden)

    I. S. Iurova

    2014-01-01

    Full Text Available Summary. For raise effectiveness drying process drum-type installation in which drum the mechanism of creation of various zones providing a necessary temperature and hydrodynamic regime of process of drying in process of product passage on a drum and changes in it of a relationship of various forms of communication of a moisture, and also a process intensification at last stage of drying by creation разряжения in a continuous technological stream of drying is provided is offered. The drum provides formation of a zone of separation of heat-transfer agent by means of the dissector, zones of intensive drying by disposing lobate nozzles in chessboard order with a dividing ring, zones of separation of the completed heat-transfer agent from жома as a result of separator installation in which the elliptic disk having cuts on a straight line from edge to the centre places, with formation of the triangular slot for passage dried pulp and heat-transfer agent, and also zones the final drying by performance of a section of a drum matching to a zone perforated on which length are had spring-loaded lobate nozzles representing the blades connected bow-shaped rod with metal plates, had with outer side of a drum and under the form repeating its contour, thus the bow-shaped rod from the interior of a drum which ends are supplied by springs rest against overhead and bottom persistent screw nuts, and blades and metal plates are installed with possibility of twirl concerning a fastening place on a drum and supplied by reinforcing ribs.

  11. 吹风机%Hair Dryers

    Institute of Scientific and Technical Information of China (English)

    2006-01-01

    据卖场导购员介绍,在往年,夏季对于吹风机来说应该是个淡季,很少有消费者购买吹风机。可是现在虽然天气越来越热.但是还是有很多消费者前来购买吹风机。当问及原因时,导购员说:以前的吹风机完全就是一个散热器.吹出来的风都是热风.在炎热的夏季很少有消费者愿意拿它来吹干头发。随着科技的飞速发展,现在的吹风机采用了许多人性化的设计,不会出现烫伤头皮的现象。

  12. 吹风机%Hair Dryers

    Institute of Scientific and Technical Information of China (English)

    2006-01-01

    现在的天气逐渐转凉,吹风机的销量比起前段时间有一定的提高,而且它向着多功能的方向发展。高级的都带有负离子发生器,防磁屏蔽罩等,设计更加人性化。各个产品的价格相差不大,功能多的当然更受欢迎。建议选择护发效果好的产品,这样对自己的头发更健康。从产品的用途来看,可分为三类:家居型、旅行型和专业型。其中旅行型产品功率800W左右,特点是携带方便;家居型产品功率普遍在800—1200W之间,适合一般的家庭使用;专业型功率在1600-2000W之间,主要销售对象为专业美发店。

  13. 吹风机%Hair Dryers

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    目前仍有不少女性对使用电吹风有一定疑虑,认为电吹风会损害发质,为了避免发质受损,宁愿等上两、三小时,让头发自然风干,而实际上,这样做我们所要付出的代价可能更大,因为头发外层自然干了,但发根依旧潮湿,易使头皮滋生细菌,产生头屑。

  14. Open-loop heat-recovery dryer

    Science.gov (United States)

    TeGrotenhuis, Ward Evan

    2013-11-05

    A drying apparatus is disclosed that includes a drum and an open-loop airflow pathway originating at an ambient air inlet, passing through the drum, and terminating at an exhaust outlet. A passive heat exchanger is included for passively transferring heat from air flowing from the drum toward the exhaust outlet to air flowing from the ambient air inlet toward the drum. A heat pump is also included for actively transferring heat from air flowing from the passive heat exchanger toward the exhaust outlet to air flowing from the passive heat exchanger toward the drum. A heating element is also included for further heating air flowing from the heat pump toward the drum.

  15. New tools to optimise spray dryers

    NARCIS (Netherlands)

    Verschueren, M.; Straatsma, J.; Schutyser, M.A.I.; Akkerman, C.; Jong, de P.

    2007-01-01

    Spray drying is an essential unit operation for the manufacture of many products with specific powder properties. It is characterised by atomisation of a solution or suspension into droplets, followed by subsequent drying of these droplets by evaporation of water or other solvents. Spray drying is u

  16. 丝状颗粒在滚筒横向截面中的传热传质特性%Heat and mass transfer characteristics of filamentous particles in transverse section of rotary dryer

    Institute of Scientific and Technical Information of China (English)

    朱立平; 秦霞; 袁竹林; 闫亚明; 罗登山; 李斌

    2014-01-01

    针对丝状物料在滚筒内干燥不均等问题,从干燥机理出发,建立了一种基于离散单元法的丝状颗粒传热传质数学模型。利用该模型对滚筒横向截面中丝状物料的温度和含水率的变化过程进行了分析计算,并通过实验验证了数学模型的有效性。研究结果表明:筒壁温度的变化对丝状颗粒传热传质特性有着直接且重要的影响;在干燥的初始阶段,颗粒彼此间温度的不均匀性迅速增大,但随着干燥的进行,颗粒之间的温度差别又呈现出逐渐缩小的趋势。颗粒间含水率的不均匀性在干燥的初始阶段同样迅速增大,当满足一定的干燥条件或一定的干燥时间,筒体内部丝状颗粒的干燥程度将会越来越均匀;丝状颗粒在滚筒中所获取的热量主要来自于与高温壁面(特别是与筒体之间)的接触导热;与升举式抄板相比,均布式抄板可使颗粒在滚筒横截面上的分布及颗粒间的温度和含水率更加均匀。%On account of drying inequality problem of filamentous materials in the rotary, a mathe-matical model for heat and mass transfer of filamentous particles based on the discrete element meth-od was proposed according to drying mechanisms, and then it was used to numerically study the tem-perature and moisture content evolution of filamentous materials in the transverse section of a rotary dryer.The effectivity of this model was verified by experiments.The results show that the change of the temperature of the cylinder wall has a direct and significant impact on the heat and mass transfer characteristics of filamentous particles.At the initial stage of drying, the standard deviation of the particles temperature increases rapidly, but then it reduces gradually with the dying time.And the standard deviation of the moisture content also increases rapidly at the initial stage of drying.When the certain drying conditions or the drying time is met

  17. OPTIMIZACIÓN DEL AISLAMIENTO TÉRMICO DE UNA CUBIERTA TRANSPARENTE DE UN SECADOR HÍBRIDO DE Guadua angustifolia OTIMIZAÇÃO DE ISOLAMENTO TÉRMICO DE UMA TAMPA TRANSPARENTE DE SECADOR HÍBRIDO DE Guadua angustifolia THERMAL INSULATION OPTIMIZATION OF A TRANSPARENT COVER FROM HYBRID DRYER OF Guadua angustifolia

    Directory of Open Access Journals (Sweden)

    Carlos Alberto Orozco

    2011-12-01

    Full Text Available El principal problema que tiene un secador solar híbrido (solar asistido con gas o electricidad son sus costos de operación por consumo de energía. Para ello se determinó el espesor óptimo de aire confinado en la cubierta plástica el cual actúa como aislamiento térmico, se calculó el coeficiente global de transferencia de calor 'U', se estimó la potencia de la fuente externa la cual fue de 1,8 kW y se encontró que el consumo de energía es aproximadamente 5,35 veces menos que la potencia del secador híbrido con cubierta sencilla. El concepto es aplicable a cualquier tipo de secador solar, solar-asistido o cualquier invernadero para el sector agroindustrial.0 principal problema con um secador solar híbrido (solar-gás assistido ou com electricidade são os custos operacionais para o consumo de energia. Para este fim a pesquisa determinou a espessura ideal de ar confinado na tampa de plástico (duas carnadas que atua como isolamento térmico, foi calculada a taxa global de transferencia de calor 'U' e estimada pela alimentação externa de 1,8 kW e descobriu que o consumo de energía é de cerca de 5,35 vezes menor do que a potência do secador revestido híbrido simples. 0 conceito é aplicável a qualquer tipo de secador solar, solar assistida ou qualquer tampa plástica no seitor agrícola.In a solar hybrid dryer (solar assisted gas or electricity its main problem is to minimize its operational costs due to energy consumption. For this, was determined the optimum thickness of air confined in the plastic cover as thermal isolation, was calculated overall coefficient of heat transfer 'U', and was estimated the power of the external source which was of 1,8 kW and found that energy consumption is approximately 5,35 times less than the power of the hybrid dryer with single plastic deck. The concept is applicable to any type of solar dryer, solar-assisted or any greenhouse in agroindustrial area.

  18. The Delta dryer: Theoretical and technological development of an energy-efficient dryer for sludge

    NARCIS (Netherlands)

    Van Gemert, G.W.

    2009-01-01

    The annual production of watery waste streams is significant. Considerable fractions are contaminated and cannot simply be disposed off. They must be stored or further treated. The latter option usually involves a thermal drying step, which renders the residue suitable as a resource: 1. Sludge with

  19. 热泵冷风干燥鲢鱼的挥发性盐基氮和脂质氧化品质模型%Modeling of total volatile basic nitrogen and thiobarbituric acid of silver carp dried in cold-air dryer with heat pump

    Institute of Scientific and Technical Information of China (English)

    高瑞昌; 袁丽; 刘伟民; 于茂帅; 周存山; 马海乐

    2013-01-01

    The quality and flavor of dried fish products tend to be affected by dry conditions. A high drying temperature will lead to the propagation of microorganisms, the oxidation of fat, and the increase of the content of total volatile basic nitrogen (TVB-N) in fish. A cold-air dryer with a heat pump can be used to keep the quality and flavor of dried fish stable, and to reduce drying energy consumption, in which the lower temperature source is used to heat the drying air with the help of a compressor. The drying medium of air in this technique is not in contact with the outside environment, so that the oxidation of nutrients and propagation of microorganisms are effectively avoided To realize the characteristics of fish products dried by cold air in a dryer with a heat pump, and determine the effects of the cold wind drying process parameters on the dried fish quality, silver carp was used as the drying material and tested by a uniform design of experiments of U10*(103). TVB-N and the value of thiobarbituric acid (TBA) for oxidation of fat was investigated as the criteria of quality of dried silver carp in the conditions of different cold air drying process parameters. The drying air temperature(x1) was 8, 11, 14, 17, 20, 23, 26, 29, 32, and 35℃, the by-pass air ratio (x2) was 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, and 1.0, and the air velocity (x3) was 0.3, 0.45, 0.6, 0.75, 0.9, 1.05, 1.2, 1.35, 1.5, and 1.65 m/s, respectively. The value of TVB-N of 10 experiments was 36.12, 34.72, 34.44, 31.64, 47.04, 35.28, 42.00, 52.92, 97.44, and 85.40 mg/100g, and the value of TBA was 4.32, 4.65, 3.68, 3.36, 4.74, 3.59, 6.67, 6.53, 7.96, and 10.58 mg/kg respectively. By SPSS analysis, the regression equations of TVB-N (mg/100g) and TBA value (mg/kg) was Y1=80.364-4.629x1+0.150x12-11.813x3, Y2=7.854-0.535x1+0.017 x12, respectively. The results show that the fit of the regression equations are good. The drying temperature was the main factor that had an effect on TVB-N and

  20. Regenerative Gas Dryer for In-Situ Propellant Production

    Science.gov (United States)

    Paz, Aaron

    2017-01-01

    Rocket propellant can be produced anywhere that water is found by splitting it into hydrogen and oxygen, potentially saving several tons of mass per mission and enabling the long term presence of humans in space beyond LEO. When water is split into hydrogen and oxygen, the gaseous products can be very humid (several thousand ppm). Propellant-grade gases need to be extremely dry before being converted into cryogenic liquids (less than 26 ppm water for grade B Oxygen). The primary objective of this project is to design, build and test a regenerative gas drying system that can take humid gas from a water electrolysis system and provide dry gas (less than 26ppm water) to the inlet of a liquefaction system for long durations. State of the art work in this area attempted to use vacuum as a means to regenerate desiccant, but it was observed that water would migrate to the dry zone without a sweep gas present to direct the desorbed vapor. Further work attempted to use CO2 as a sweep gas, but this resulted in a corrosive carbonic acid. In order for in-situ propellant production to work, we need a way to continuously dry humid gas that addresses these issues.

  1. Fabrication and evaluation of a Solar Grain Dryer

    Directory of Open Access Journals (Sweden)

    Yanoy Morejón Mesa

    2011-01-01

    Full Text Available El proceso de secado es una actividad principal en las operaciones de postcosecha en los granos; para economizar en Fuentes de energía y reducir la contaminación del medio ambiente es posible desarrollar secadoras solares de granos. Por esta razón se realizo la fabricación y la prueba de funcionamiento de una secadora solar de granos. Los principales resultados obtenidos fueron los siguientes, el contenido medio de humedad antes del secado en la superficie fue 22,51% y después del proceso de secado fue 11,6%, y en el fondo el contenido medio de humedad antes del secado fue 22,78% y después de secado fue 13,2%, por lo tanto el promedio de la tasa de reducción de humedad fue 0,84%/h, también antes del secado la masa de arroz cascara fue de 120,28 kg y después de secado fue 105,40 kg, por lo tanto 14,88 kg de agua fueron separados y el consumo de combustible del motor diesel durante 12 horas de operación fue de 2,75 L. Los resultados obtenidos fueron impresionantes; por lo tanto este prototipo ayudaría a los Productores de pequeña escala a mejorar la calidad del grano durante las operaciones de postcosecha.

  2. Large Optic Drying Station: Summary of Dryer Certification Tests

    Energy Technology Data Exchange (ETDEWEB)

    Barbee, T W; Ayers, S L; Ayers, M J

    2009-08-28

    The purpose of this document is to outline the methodology used to baseline and maintain the cleanliness status of the newly built and installed Large Optic Cleaning Station (LOCS). The station has currently been in use for eleven months; and after many cleaning studies and implementation of resulting improvements appears to be cleaning optics to a level that is acceptable for the fabrication of Nano-Laminates.

  3. Behavior of a portable solar dryer for pineapple fiber

    National Research Council Canada - National Science Library

    Moya, Róger; Solano, Marco

    2012-01-01

    In Costa Rica, there has been a growing interest to use pineapple fiber from plant, for which current processes need to be improved or new processes need to be developed, with emphasis on drying methods...

  4. Inert Welding/Brazing Gas Filters and Dryers

    Science.gov (United States)

    Goudy, Jerry

    2009-01-01

    The use of hybridized carbon/silicon carbide (C/SiC) fabric to reinforce ceramic matrix composite face sheets and the integration of such face sheets with a foam core creates a sandwich structure capable of withstanding high-heat-flux environments (150 W/sq cm) in which the core provides a temperature drop of 1,000 C between the surface and the back face without cracking or delamination of the structure. The composite face sheet exhibits a bilinear response, which results from the SiC matrix not being cracked on fabrication. In addition, the structure exhibits damage tolerance under impact with projectiles, showing no penetration to the back face sheet. These attributes make the composite ideal for leading-edge structures and control surfaces in aerospace vehicles, as well as for acreage thermal protection systems and in high-temperature, lightweight stiffened structures. By tailoring the coefficient of thermal expansion (CTE) of a carbon fiber containing ceramic matrix composite (CMC) face sheet to match that of a ceramic foam core, the face sheet and the core can be integrally fabricated without any delamination. Carbon and SiC are woven together in the reinforcing fabric. Integral densification of the CMC and the foam core is accomplished with chemical vapor deposition, eliminating the need for bond-line adhesive. This means there is no need to separately fabricate the core and the face sheet, or to bond the two elements together, risking edge delamination during use. Fibers of two or more types are woven together on a loom. The carbon and ceramic fibers are pulled into the same "pick" location during the weaving process. Tow spacing may be varied to accommodate the increased volume of the combined fiber tows while maintaining a target fiber volume fraction in the composite. Foam pore size, strut thickness, and ratio of face sheet to core thickness can be used to tailor thermal and mechanical properties. The anticipated CTE for the hybridized composite is managed by the choice of constituents, varying fiber tow sizes and constituent part ratios. This structural concept provides high strength and stiffness at low density 1.06 g/cu cm in panels tested. Varieties of face sheet constructions are possible, including variations in fiber type and weave geometry. The integrated structures possible with this composite could eliminate the need for non-load-bearing thermal protection systems on top of a structural component. The back sheet can readily be integrated to substructures through the incorporation of ribs. This would eliminate weight and cost for aerospace missions.

  5. performance evaluation of a pebble bed solar crop dryer abstract

    African Journals Online (AJOL)

    Dr Obe

    Department of Agricultural Engineering. University of ... bed solar heat storage unit/solar collector and crop drying chamber measuring 67 cm x 110 cm ... artificial methods of food drying in Nigeria, .... the solar collector when in operation.

  6. Boosting spray dryer performance without compromising powder quality

    NARCIS (Netherlands)

    Schutyser, M.A.I.; Straatsma, M.; Jong, de P.

    2008-01-01

    Abstract The role of NIZO food research in the design of the optimal spray drying processes is discussed. NIZO offers various analysis and modeling techniques that are successfully applied for the optimization and design of drying installations. Heat processing and drying of food is beneficial to ma

  7. Pulse Dryer Technology for Developing Nations Its Application to Sludge

    Energy Technology Data Exchange (ETDEWEB)

    Rogan, F.; Duncan, S. G.

    2003-02-24

    This paper describes a simple but efficient process for converting sludge and other miscellaneous liquid/solid mixtures into a very dry powder form. Its simplicity lends itself to ease of use, mobility and cost effectiveness. The operation of this process does not present any unreviewed or new environmental issues and accommodates Best Available Treatment requirements. The process provides an opportunity for the treatment of small or large quantities of sludge and other existing hazardous wastes to create a dry product that is more easily handled, disposed of or otherwise dispositioned.

  8. Energy balance for steam generation system with biomass dryer

    Energy Technology Data Exchange (ETDEWEB)

    Ramos, Pedro A.R. [Instituto Superior Politecnico Jose Antonio Echeverria (CUJAE), Ciudad de La Habana (Cuba). Facultad Ingenieria Mecanica]. E-mail: pedro@economia.cujae.edu.cu; Lombardi, Geraldo; Santos, Antonio Moreira dos [Universidade de Sao Paulo (USP), Sao Carlos, SP (Brazil). Escola de Engenharia]. E-mails: lombardi@sc.usp.br; asantos@sc.usp.br

    2008-07-01

    Water content is a major drainer of the energy available in the biomass, which justifies the proposal of a drying system with the potential to increase 80% of the biomass low heating value, also increasing the production of steam in the boiler and cogeneration of electricity. An example of biomass is the sugar cane bagasse of an alcohol mill producing 120,000 liters of alcohol per day, whose humidity from the extraction section is usually 50%. The present paper determines the increases in the mass flow rates of steam in the boiler, in the cogeneration of electricity and in the pay back time of the drying system and of the alcohol mill, as a consequence of the bagasse drying from 50 to 35%, considering 30% of air excess over the stoichiometric value admitted in the boiler for the bagasse burning. It also provides subsidies for the development and deployment of a drying system for the current boilers. (author)

  9. Fabrication and evaluation of a Solar Grain Dryer

    OpenAIRE

    Yanoy Morejón Mesa; Toshiyuki Tsujimoto; Tadashi Watahiki

    2011-01-01

    El proceso de secado es una actividad principal en las operaciones de postcosecha en los granos; para economizar en Fuentes de energía y reducir la contaminación del medio ambiente es posible desarrollar secadoras solares de granos. Por esta razón se realizo la fabricación y la prueba de funcionamiento de una secadora solar de granos. Los principales resultados obtenidos fueron los siguientes, el contenido medio de humedad antes del secado en la superficie fue 22,51% y después del proceso de ...

  10. Learning Sustainability by Developing a Solar Dryer for Microalgae Retrieval

    Science.gov (United States)

    Malheiro, Benedita; Ribeiro, Cristina; Silva, Manuel F.; Caetano, Nídia; Paulo Ferreira,; Guedes, Pedro

    2015-01-01

    The development of nations depends on energy consumption, which is generally based on fossil fuels. This dependency produces irreversible and dramatic effects on the environment, e.g. large greenhouse gas emissions, which in turn cause global warming and climate changes, responsible for the rise of the sea level, floods, and other extreme weather…

  11. Preservation of Food Items Using Solar Dryers: A Review

    Directory of Open Access Journals (Sweden)

    Manish Joshi

    2016-07-01

    Full Text Available In order to conserve the food products like chillies, grapes, potatoes & other agricultural products, for a longer period of time & with same the quality they need to be dried by using any form of energy, for example heat energy from fossil fuels or solar energy etc. This is done to reduce the moisture content to a predetermined level which prevents the growth & reproduction of micro organisms like bacteria, yeasts etc. that causes many moisture mediated deterioration reactions. One of the drying methods involves drying the produce with the help of direct sun light by spreading them in an open space. This process is labor intensive & requires a large area for spreading the produced to dry out. The disadvantage of this method involves uneven heating, loss of produce due to birds, animals, bad weather etc. Another method of drying involves artificial mechanical drying which is an energy intensive, expensive and costly method. Green house drying or solar drying gives the best results as it does not compromise the product quality, aesthetic etc. Moreover it makes the transportation process easy as the volume of dried product reduces. This paper reviews the solar drying process & gives complete in depth of all the elements involve in solar drying.

  12. Water adsorption isotherms and isosteric sorption heat of spray-dried and freeze-dried dehydrated passion fruit pulp with additives and skimmed milk Isotermas de adsorção e calor isostérico de sorção de polpa de maracujá desidratada por spray dryer e liofilizador com aditivos e leite desnatado

    Directory of Open Access Journals (Sweden)

    Kelly Tafari Catelam

    2011-12-01

    Full Text Available Moisture equilibrium data of passion fruit pulp powders with maltodextrin and gum arabic were obtained by two different drying methods (spray drying and freeze drying and determined at 20, 30, 40 and 50º C. Skimmed milk was used to substitute part of these additives in the samples. One formulation using passion fruit pulp/maltodextrin/skimmed milk (PMS was prepared, and another using passion fruit pulp/gum arabic/skimmed milk (PGS. The behavior of curves was type III, according to Brunauer's classification. GAB models were fitted to experimental equilibrium data. The parameters obtained from GAB models was affected by the presence of additives. The behavior of the sorption isotherms for different temperatures are similar, noting only a small effect of temperature. There were little differences between both drying methods and additives used in relation to equilibrium moisture content. The parameters obtained with the addition of the skimmed milk were considered satisfactory (Xm values ranged from 0,04084 to 0,06488 in dry basis, demonstrating that it is an effective and cheap alternative for regular additives. A progressive increase in the heat of sorption in relation to decreasing moisture content was observed and the heat of sorption values of different samples are all similar, comparing the relative equilibrium moisture content.Dados de umidade de equilíbrio da polpa de maracujá em pó com maltodextrina e goma arábica obtidas por dois diferentes processos de secagem (spray dryer e liofilizador foram determinados a 20, 30, 40 e 50° C. Leite desnatado foi utilizado nas amostras em substituição a uma parte desses dois aditivos. Prepararou-se uma formulação, usando polpa de maracujá/maltodextrina/leite desnatado (PMS e outra com polpa de maracujá/goma arábica/leite desnatado (PGS. Os comportamentos das isotermas obedeceram ao tipo III, de acordo com a classificação de Brunauer e utilizou-se o modelo de GAB para ajuste dos dados de

  13. Cashew-nut (Anacardium occidentale L.) Drying Study Using a Solar Dryer with Direct Radiation

    OpenAIRE

    Machado, Antônio V.; Oliveira,Edson L. de; Santos, Everaldo S.; Jackson A de Oliveira

    2010-01-01

    MACHADO, Antônio V. et al. Estudio del Secado de Anacardo (Anacardium occidentale L.) mediante Secador Solar de Radiación Directa. Información Tecnológica, v. 21, n. 1, p. 31-37, 2010. Resumen: Se presentan ensayos de secado con radiación solar directa y su modelado matemático, para evaluar la cinética de secado del anacardo (Anacardium occidentale L.) y comparar su eficiencia en relación al secado solar natural en tablero. Los experimentos fueron realizados con rodajas de fruta de 1 cm. y...

  14. Numerical and experimental investigation of direct solar crop dryer for farmers

    Science.gov (United States)

    Kareem, M. W.; Habib, Khairul; Sulaiman, S. A.

    2015-07-01

    This article presents a theoretical and experimental investigation on effects of weather on direct solar crop drying technique. The SIMULINK tool was employed to analyze the energy balance equations of the transient system model. A prototype of the drying system was made and data were collected between the months of June and July in Perak, Malaysia. The contribution of intense sunny days was encouraging despite the wet season, and the wind velocity was dynamic during the period of investigation. However, high percentage of relative humidity was observed. This constitutes a hindrance to efficient drying process. The reported studies were silent on the effect of thick atmospheric moisture content on drying rate of agricultural products in tropic climate. This finding has revealed the mean values of insolation, wind speed, moisturized air, system performance efficiency and chili microscopy image morphology. The predicted and measured results were compared with good agreement.

  15. Drying and dryer from the aspect of renewable energy and sustainable development

    OpenAIRE

    Topić Radivoj; Božović Milan; Topić Goran

    2017-01-01

    Sustainable development, energy efficiency, renewable energy and environmental protection are the most pressing questions at the beginning of a new, 21st, century. The most important role of renewable energy in reducing greenhouse gases, increasing energy security and creation through small and medium enterprises. The paper gives a brief overview of renewable energy sources in terms of sustainable development, energy efficiency and environmental protection and the role of the drying process t...

  16. Studi Eksperimen Pengaruh Ukuran Partikel Batubara Pada Swirling Fluidized Bed Dryer Terhadap Karakteristik Pengeringan Batubara

    Directory of Open Access Journals (Sweden)

    Zainal Fanani

    2014-03-01

    Full Text Available Desain suatu PLTU salah satunya dibuat berdasarkan kualitas batubara yang akan digunakan sebagai bahan bakar. Pada PLTU batubara dibakar didalam boiler, didalam boiler terdapat pulverizer yang berfungsi untuk menghaluskan batubara dan menambah pasokan batubara kedalam boiler jika batubara didalam boiler memiliki nilai heating value rendah. Dengan menggunakan batubara dengan kualitas rendah maka suplai batubara yang dibutuhkan untuk memanaskan boiler  akan semakin banyak, hal ini bisa mengakibatkan kerja dari pulverizer akan semakin berat. Indonesia sendiri merupakan salah satu negara penghasil batubara terbersa didunia. Namun hampir 80% batubara yang dihasilkan tergolong batubara rendah dan sedang [1] . Untuk meningkatkan nilai kalor batubara perlu dilakukan pengeringan untuk mengurangi kadar air dalam batubara. Eksperimen dilakukan dengan mengeringkan batubara didalam chamber dengan temperature udara 550C, sudut blade 200 dan massa pengeringan sebanyak 600gram, variasi ukuran partikel batubara 5mm, 10mm, 15mm. Pengambilan data dilakukan dengan menimbang berat batubara setiap satu menit sebanyak 5 kali  , dua menit sebanyak 3 kali, dan lima menit sebanyak 4 kali. Data yang diperoleh berupa relative humidity udara, temperature udara, berat sampel basah dan berat sampel kering. Pengambilan data berat sampel kering dilakukan berdasarkan standart ASTM D5142 dengan pengeringan pada temperatur 1050C selama 3 jam. Dari hasil eksperimen didapat bahwa proses pelepasan massa uap air paling banyak terjadi pada lima menit pertama yang ditandai dengan penurunan moisture content paling besar. Pada partikel batubara ukuran 5mm,10mm,15mm didapat moisture content terendah berturut-turut sebesar  6,48 %, 7,66 %, 7,47 %. Untuk laju pengeringan didapat nilai terendah berturut-turut sebesar 0,062 gram/menit, 0,104 gram/menit, 0,023 gram/menit,  sedangkan selisih humidity ratio ( ɷ2-ɷ1 didapat nilai terendah berturut turut sebesar 0,0072gram/kg dry air, 0,0713 gram/kg dry air, 0,1372 gram/kgdry air.

  17. From Yeast to Hair Dryers: Effective Activities for Teaching Environmental Sciences.

    Science.gov (United States)

    Nolan, Kathleen A.

    2001-01-01

    Reports on four experiments and/or activities that were used to stimulate student interest in environmental science. Makes the case that varying classroom activities in the environmental science classroom makes the teaching and learning experience more alive and vital to both instructor and student. (Author/MM)

  18. Hair dryer use to optimize pulsed dye laser treatment in rosacea patients.

    Science.gov (United States)

    Kashlan, Lana; Graber, Emmy M; Arndt, Kenneth A

    2012-06-01

    Rosacea is a common chronic inflammatory condition characterized by erythema, telangiectasias, papules, and pustules. While there are many effective treatment options for the papulopustular type, laser therapy remains the most effective modality to treat erythematotelangiectatic rosacea. Erythema and flushing associated with rosacea remains an uncomfortable and socially embarrassing problem for patients. Unfortunately, patients often do not have significant erythema or flushing when they present for laser treatment. With this in mind, we propose a novel technique aimed at enhancing the response of rosacea patients being treated for erythema with pulsed dye laser. Specifically, we present a split-face example of our clinical observation that pre-treatment with forced heated air prior to pulsed-dye laser leads to a greater response in rosacea patients with erythema and flushing.

  19. In Vitro Protein Digestibility and Physical Properties of Instant Teh Talua Dried by Spray Dryer

    Directory of Open Access Journals (Sweden)

    Rina Yenrina

    2016-02-01

    Full Text Available Abstract—This study aims to learn the effect of the addition of different concentrations of tea on protein digestibility and physical properties of the  product. This study has been completed from February to July 2014. This study begins with the process of making instant teh talua, then continue with prodct analysis. This study used a completely randomized design (CRD with 5 treatments and 3 replications. Data were analyzed statistically by F test and if significantly different, followed by Duncan's test New Multiple Range Test (DNMRT at 5% level. The treatment in this study include A (Without Tea Extract, B (5 g of Tea Extract in 100 ml of water, C (10 g of Tea Extract in 100 ml of water, D (15 g of Tea Extract in 100 ml of water, and E (20 g of Tea Extract in 100 ml of water. The results of this study showed that the addition of treatment between different tea extract gives significant effect on protein content, water-soluble portion, protein digestibility, and no significant effect on moisture content and water activities.

  20. Thermodynamic analysis of an industrial dryer in a ceramic production: an application

    Energy Technology Data Exchange (ETDEWEB)

    Utlu, Zafer [Mechanical Engineering Department, Faculty of Engineering and Architecture, Istanbul Aydin University (Turkey)], E-mail: zaferutlu@aydin.edu.tr, email: zafer_utlu@yahoo.com; Hepbasli, Arif [Department of Mechanical Engineering, College of Engineering, King Saud University (Saudi Arabia)], email: ahepbasli.c@ksu.edu.sa, email: arifhepbasli@gmail.com

    2011-07-01

    The drying industry always aims to reduce the amount of moisture from production and to reach this goal using the minimum amount of energy and at minimum cost. The purpose of this paper is to give the energy and exergy analysis of a ceramic plant and to determine the energy and exergy utilization efficiencies of this plant's drying process. Exergy analysis has been widely used for various thermal systems and drying is a significant element of these systems and is an energy intensive operation. In this study, the exergy analysis method was applied to a drying system on a ceramic production line. This process was divided into three stages with the aim of calculating the values for exergy destruction and efficiency of the system in reference (dead state) temperature. Mass, elemental, and heat losses were also studied by means of the actual plant operational data and conclusions were drawn from this that are listed in this paper.

  1. 76 FR 52854 - Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and...

    Science.gov (United States)

    2011-08-24

    ... Equipment Price Forecasting in Energy Conservation Standards Analysis (76 FR 9696, Feb. 22, 2011), has not... innovations for production of gas from tight shales. AGA recommended that DOE conduct its analysis using the.... Equipment Price Forecasting AHAM expressed concern regarding the use of experience curves in equipment...

  2. Use of an artisan Solar Grain Dryer to dry soybeans and black beans grains

    Directory of Open Access Journals (Sweden)

    Yanoy Morejón Mesa

    2014-01-01

    Full Text Available El proceso de secado de granos es una actividad principal en las operaciones de poscosecha, con el objetivo de economizar en fuentes de energía y reducir la contaminación del medio ambiente es posible desarrollar secadoras solares de granos. Por esta razón se fabri- có y evaluó un prototipo para el secado solar de granos. Los principales resultados obtenidos para granos de soya y frijol negro fueron los siguientes: el contenido medio de humedad antes del secado de la soya fue 15% y después del proceso fue 10,24%, en el caso del frijol negro el contenido medio de humedad antes del secado fue 16% y después fue 12,15%, siendo la tasa de reducción de humedad 1,58%/ h y 0,54%/ h para ambos granos respectivamente, antes del secado la masa de soya fue de 116 kg y después fue 104 kg, por lo tanto fueron separados 12 kg de agua; en el caso del frijol negro la masa inicial fue de 150 kg y después fue 142 kg, por lo tanto se separaron 8 kg de agua; el consumo de combustible fósil fue nulo, así como la emisión de gases productos de la combustión; este prototipo resiste las cargas a las que se somete y las leyes de transferencia de calor validan que el mismo cumple con las características que deben tener las máquinas secadoras, también se determinó el costo de explotación el cual fue de 2,71 peso/h.

  3. Desalination of salty water using vacuum spray dryer driven by solar energy

    KAUST Repository

    Hamawand, Ihsan

    2016-11-18

    This paper addresses evaporation under vacuum condition with the aid from solar energy and the recovered waste heat from the vacuum pump. It is a preliminary attempt to design an innovative solar-based evaporation system under vacuum. The design details, equipment required, theoretical background and work methodology are covered in this article. Theoretically, based on the energy provided by the sun during the day, the production rate of pure water can be around 15 kg/m2/day. Assumptions were made for the worst case scenario where only 30% of the latent heat of evaporation is recycled and the ability of the dark droplet to absorb sun energy is around 50%. Both the waste heat from the pump and the heat collected from the photovoltaic (PV) panels are proposed to raise the temperature of the inlet water to the system to its boiling point at the selected reduced pressure.

  4. Drying characteristics of pumpkin ( Cucurbita moschata) slices in convective and freeze dryer

    Science.gov (United States)

    Caliskan, Gulsah; Dirim, Safiye Nur

    2017-06-01

    This study was intended to determine the drying and rehydration kinetics of convective and freeze dried pumpkin slices (0.5 × 3.5 × 0.5 cm). A pilot scale tray drier (at 80 ± 2 °C inlet temperature, 1 m s-1 air velocity) and freeze drier (13.33 kPa absolute pressure, condenser temperature of -48 ± 2 °C) were used for the drying experiments. Drying curves were fitted to six well-known thin layer drying models. Nonlinear regression analysis was used to evaluate the parameters of the selected models by using statistical software SPSS 16.0 (SPSS Inc., USA). For the convective and freeze drying processes of pumpkin slices, the highest R2 values, and the lowest RMSE as well as χ2 values were obtained from Page model. The effective moisture diffusivity (Deff) of the convective and freeze dried pumpkin slices were obtained from the Fick's diffusion model, and they were found to be 2.233 × 10-7 and 3.040 × 10-9 m2s-1, respectively. Specific moisture extraction rate, moisture extraction rate, and specific energy consumption values were almost twice in freeze drying process. Depending on the results, moisture contents and water activity values of pumpkin slices were in acceptable limits for safe storage of products. The rehydration behaviour of [at 18 ± 2 and 100 ± 2 °C for 1:25, 1:50, 1:75, 1:100, and 1:125 solid:liquid ratios (w:w)] dried pumpkin slices was determined by Peleg's model with the highest R2. The highest total soluble solid loss of pumpkin slices was observed for the rehydration experiment which performed at 1:25 solid: liquid ratio (w:w). Rehydration ratio of freeze dried slices was found 2-3 times higher than convective dried slices.

  5. Cold Vacuum Dryer (CVD) Facility Fire Protection System Design Description (SYS 24)

    Energy Technology Data Exchange (ETDEWEB)

    SINGH, G.

    2000-10-17

    This system design description (SDD) addresses the Cold Vacuum Drying (CVD) Facility fire protection system (FPS). The primary features of the FPS for the CVD are a fire alarm and detection system, automatic sprinklers, and fire hydrants. The FPS also includes fire extinguishers located throughout the facility and fire hydrants to assist in manual firefighting efforts. In addition, a fire barrier separates the operations support (administrative) area from the process bays and process bay support areas. Administrative controls to limit combustible materials have been established and are a part of the overall fire protection program. The FPS is augmented by assistance from the Hanford Fire Department (HED) and by interface systems including service water, electrical power, drains, instrumentation and controls. This SDD, when used in conjunction with the other elements of the definitive design package, provides a complete picture of the FPS for the CVD Facility.

  6. Economic Optimization of Spray Dryer Operation using Nonlinear Model Predictive Control

    DEFF Research Database (Denmark)

    Petersen, Lars Norbert; Poulsen, Niels Kjølstad; Niemann, Hans Henrik

    2014-01-01

    In this paper we investigate an economically optimizing Nonlinear Model Predictive Control (E-NMPC) for a spray drying process. By simulation we evaluate the economic potential of this E-NMPC compared to a conventional PID based control strategy. Spray drying is the preferred process to reduce......-shooting method combined with a quasi-Newton Sequential Quadratic Programming (SQP) algorithm and the adjoint method for computation of gradients. The E-NMPC improves the cost of spray drying by 26.7% compared to conventional PI control in our simulations....

  7. Economic Optimization of Spray Dryer Operation using Nonlinear Model Predictive Control with State Estimation

    DEFF Research Database (Denmark)

    Petersen, Lars Norbert; Jørgensen, John Bagterp; Rawlings, James B.

    2015-01-01

    In this paper, we develop an economically optimizing Nonlinear Model Predictive Controller (E-NMPC) for a complete spray drying plant with multiple stages. In the E-NMPC the initial state is estimated by an extended Kalman Filter (EKF) with noise covariances estimated by an autocovariance least...... squares method (ALS). We present a model for the spray drying plant and use this model for simulation as well as for prediction in the E-NMPC. The open-loop optimal control problem in the E-NMPC is solved using the single-shooting method combined with a quasi-Newton Sequential Quadratic programming (SQP...

  8. Design of energy systems for gas-heated through air dryers

    Energy Technology Data Exchange (ETDEWEB)

    Weineisen, Henrik; Stenstroem, Stig [Lund Univ. (Sweden). Dept. of Chemical Engineering

    2006-04-15

    The aim of the work has been to acquire a better understanding for the through-drying process and to use this knowledge to improve the energy efficiency of the process. In order to learn more about the mechanisms involved in through-drying, the process has been studied by experiments and by mathematical modelling. The work has been focused on the following areas: A. Review of the existing literature on through-drying B. Initial computer modelling of the through-drying process and comparison with experimental data from the literature C. Study of the overall energy balances of the through-drying system D. Experimental work with the aim of acquiring data at conditions comparable to industrial intensities (The work was performed at the Metso Paper research facility, Biddeford, Maine, USA.) E. Modelling of through-drying at high intensity and comparison with experimental data (ongoing). Short reports of stages A-C and a detailed report from stage D are presented in this publication.

  9. Research of Seed Cotton Dryer Technology%籽棉烘干机技术研究

    Institute of Scientific and Technical Information of China (English)

    刘同策; 温浩军

    2016-01-01

    我国夏季高温多雨,秋冬多霜雪,特别在北部地区,下半年气候潮湿,不利于棉花收获. 伴随棉花产量的增加,晾晒条件的不理想及对棉花等级要求的提高,籽棉烘干技术在棉花加工过程中扮演着不可缺少的作用.近些年,我国机采棉发展势头强劲,然而机采棉的回潮率远大于手摘棉,严重影响了棉花加工生产各个环节的质量. 为此,阐述了籽棉烘干技术的研究现状及发展趋势.%China has high temperature and a lot of rain in summer , has a lot of frost and snow in autumn and winter , es-pecially in the north .The damp climate is not conducive to the cotton harvest in the second half of a year .Along with the increase of cotton production, not ideal drying conditions, as well as the improvement of cotton quality , seed cotton' s drying technology plays an indispensable role in cotton production .In recent years , the development of cotton-picking machine is huge in China ,however ,cotton moisture regain is more than hand picking cotton .In the same time , the quality of cotton production ' s each part has been affected seriously .In order to improve the economic benefit , seed cotton ' s dr-ying technology has been promoted greatly .

  10. Drying performance of fermented cassava (fercaf) using a convective multiple flash dryer

    Science.gov (United States)

    Handojo, Lienda A.; Zefanya, Samuel; Christanto, Yohanes

    2017-05-01

    Fermented cassava (fercaf) is a tropical versatile carbohydrate source flour which is produced by modifying the characteristics of cassava. Drying process is one of the processes that could influence the quality of fercaf. In general, for food application, convective and vacuum drying were used, however recently another advanced method using combination of both convective and vacuum, i.e. convective multiple flash drying (CMFD), was proposed. This method is conducted by repeating cycles of convective and vacuum drying in intermittent manner. Cassava chips with thickness of 0.1-0.2 cm were fermented for 24 hours at room condition. Then, the drying process was conducted by using 3 techniques, i.e. convective, vacuum, and combined method (CMFD), with operation temperatures between 50 and 70°C for 10 hours or until fermented cassava reached a moisture content of less than 20%. The study shows that CMFD was the fastest drying method with only 5-6 hours period compared to 8-10 hours using vacuum and more than 10 hours using convective method. CMFD also produces harder fercaf chips than those of vacuum and convective methods. Moreover, this research also proves that the operating pressure and temperature influence the moisture content.

  11. 76 FR 26656 - Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and...

    Science.gov (United States)

    2011-05-09

    ... U.S.C. 6295(o) or other applicable law. If the Secretary makes such a determination, DOE must..., Arcelik, Fisher & Paykel, Scotsman Ice, Indesit, Kuppersbusch, Kelon, and DeLonghi); energy and... Water Efficiency (AWE), Northwest Power and Conservation Council (NPCC), and Northeast Energy...

  12. 30 CFR 77.307 - Thermal dryers; location and installation; general.

    Science.gov (United States)

    2010-07-01

    ... where the heat, sparks, flames, or coal dust from the system might cause a fire or explosion. (b... structures of heavy construction with explosion pressure release devices (such as hinged wall panels,...

  13. 76 FR 22324 - Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and...

    Science.gov (United States)

    2011-04-21

    ...; ] DEPARTMENT OF ENERGY 10 CFR Part 430 RIN 1904-AA89 Energy Conservation Program: Energy Conservation Standards... Renewable Energy, Department of Energy. ACTION: Proposed rule. SUMMARY: The Energy Policy and Conservation Act (EPCA) prescribes energy conservation standards for various consumer products and......

  14. 76 FR 22453 - Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and...

    Science.gov (United States)

    2011-04-21

    ... April 21, 2011 Part II Department of Energy 10 CFR Part 430 Energy Conservation Program: Energy... 10 CFR Part 430 RIN 1904-AA89 Energy Conservation Program: Energy Conservation Standards for..., Department of Energy. ACTION: Direct final rule. SUMMARY: The Energy Policy and Conservation Act...

  15. 78 FR 20842 - Energy Conservation Program: Energy Conservation Standards for Residential Clothes Dryers and...

    Science.gov (United States)

    2013-04-08

    ... Part 430 RIN 1904-AC98 Energy Conservation Program: Energy Conservation Standards for Residential... conservation standards for room air conditioners. In the direct final rule establishing amended energy... May 8, 2013. ADDRESSES: Any comments submitted must identify the proposed rule for Energy...

  16. Drying characteristics of pumpkin (Cucurbita moschata) slices in convective and freeze dryer

    Science.gov (United States)

    Caliskan, Gulsah; Dirim, Safiye Nur

    2017-01-01

    This study was intended to determine the drying and rehydration kinetics of convective and freeze dried pumpkin slices (0.5 × 3.5 × 0.5 cm). A pilot scale tray drier (at 80 ± 2 °C inlet temperature, 1 m s-1 air velocity) and freeze drier (13.33 kPa absolute pressure, condenser temperature of -48 ± 2 °C) were used for the drying experiments. Drying curves were fitted to six well-known thin layer drying models. Nonlinear regression analysis was used to evaluate the parameters of the selected models by using statistical software SPSS 16.0 (SPSS Inc., USA). For the convective and freeze drying processes of pumpkin slices, the highest R2 values, and the lowest RMSE as well as χ2 values were obtained from Page model. The effective moisture diffusivity (Deff) of the convective and freeze dried pumpkin slices were obtained from the Fick's diffusion model, and they were found to be 2.233 × 10-7 and 3.040 × 10-9 m2s-1, respectively. Specific moisture extraction rate, moisture extraction rate, and specific energy consumption values were almost twice in freeze drying process. Depending on the results, moisture contents and water activity values of pumpkin slices were in acceptable limits for safe storage of products. The rehydration behaviour of [at 18 ± 2 and 100 ± 2 °C for 1:25, 1:50, 1:75, 1:100, and 1:125 solid:liquid ratios (w:w)] dried pumpkin slices was determined by Peleg's model with the highest R2. The highest total soluble solid loss of pumpkin slices was observed for the rehydration experiment which performed at 1:25 solid: liquid ratio (w:w). Rehydration ratio of freeze dried slices was found 2-3 times higher than convective dried slices.

  17. COMMERCIAL DEMONSTRATION OF THE MANUFACTURED AGGREGATE PROCESSING TECHNOLOGY UTILIZING SPRAY DRYER ASH

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol

    2003-07-01

    This quarterly report covers the period from April 1st, 2003 through June 30th, 2003. It covers; technical development, permitting status, engineering status, construction status, operations summary and marketing support activities for this period.

  18. Commercial Demonstration of the Manufactured Aggregate Processing Technology Utilizing Spray Dryer Ash

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol

    2005-05-01

    This quarterly report covers the period from January 1, 2005 through March 31, 2005. It covers: technical development, permitting status, engineering status, construction status, operations summary and marketing support activities for this period. Plant startup is still continuing. Testing of admixtures to enhance extrusion and SDA wetting is continuing. Efforts are underway to improve plant availability.

  19. Commercial Demonstration of the Manufactured Aggregate Processing Technology Utilizing Spray Dryer Ash

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol

    2004-11-01

    This quarterly report covers the period from July 1st, 2004 through September 30th, 2004. It covers: technical development, permitting status, engineering status, construction status, operations summary and marketing support activities for this period. Plant startup, including equipment and system debugging, is underway. Minor adjustments to the SDA feed system, pug mill, and extruder were completed. Testing of admixtures to prevent the wetted SDA from sticking is continuing. The power plant is implementing a lime optimization program to reduce the calcium hydroxide values in the ash.

  20. COMMERCIAL DEMONSTRATION OF THE MANUFACTURED AGGREGATE PROCESSING TECHNOLOGY UTILIZING SPRAY DRYER ASH

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol

    2003-10-01

    This quarterly report covers the period from July 1st, 2003 through September 30th, 2003. It covers; technical development, permitting status, engineering status, construction status, operations summary and marketing support activities for this period.

  1. COMMERCIAL DEMONSTRATION OF THE MANUFACTURED AGGREGATE PROCESSING TECHNOLOGY UTILIZING SPRAY DRYER ASH

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol, P.E.

    2003-06-01

    This quarterly report covers the period from January 1st, 2003 through March 31st, 2003. It covers; technical development, permitting status, engineering status, construction status, operations summary and marketing support activities for this period.

  2. COMMERCIAL DEMONSTRATION OF THE MANUFACTURED AGGREGATE PROCESSING TECHNOLOGY UTILIZING SPRAY DRYER ASH

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol

    2004-01-01

    This quarterly report covers the period from October 1st, 2003 through December 31st, 2003. It covers: technical development, permitting status, engineering status, construction status, operations summary and marketing support activities for this period.

  3. COMMERCIAL DEMONSTRATION OF THE MANUFACTURED AGGREGATE PROCESSING TECHNOLOGY UTILIZING SPRAY DRYER ASH

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol, P.E.

    2003-06-01

    This quarterly report covers the period from November 14th, 2002 through December 31st, 2002. It covers; mix design development, permitting status, engineering status, construction status, and marketing support activities for this period.

  4. Commercial Demonstration of the Manufactured Aggregate Processing Technology Utilizing Spray Dryer Ash

    Energy Technology Data Exchange (ETDEWEB)

    Roy Scandrol

    2005-02-01

    This quarterly report covers the period from October 1st, 2004 through December 31st, 2004. It covers: technical development, permitting status, engineering status, construction status, operations summary and marketing support activities for this period. Plant startup is still continuing. Testing of admixtures to enhance extrusion and SDA wetting is continuing. Green extrudates and embedding material were loaded into the curing vessel on October 14th. The whole plant was integrated on December 16th. Efforts are underway to improve plant availability.

  5. Hydrodynamics study on drying of pepper in swirling fluidized bed dryer (SFBD)

    Science.gov (United States)

    Syaif Haron, Nazrul; Hazri Zakaria, Jamal; Faizal Mohideen Batcha, Mohd

    2017-08-01

    Malaysia is one of the pepper producer with exports quantity reaching more than 90000 tonnes between 2010 until 2016. Drying of pepper is mandatory before their export and at present, pepper was dried by sun drying to reduce cost. This conventional drying method was time consuming and may take four days during rainy season, which retards the production of pepper. This paper proposes the swirling fluidized bed drying (SFBD) method, which was known to have high mixing ability and improved solid-gas contact to shorten the drying time of products. A lab scale SFBD system was constructed to carry out this study. Hydrodynamic study was conducted for three beds loadings of 1.0 kg, 1.4 kg at a drying temperature of 90°C. The SFBD has shown excellent potential to dry the pepper with a relatively short drying time compared to the conventional method. Batch drying for the bed loads studied only took 3 hours of drying time only. It was found that bed higher bed loading of wet pepper requires longer drying time due to higher amount of moisture content in the bed. Four distinct regimes of operation were found during drying in the SFBD and these regimes offer flexibility of operation. The total bed pressure drop was relatively low during drying.

  6. Two-dimensional mathematical model of a packed bed dryer and experimentation

    Energy Technology Data Exchange (ETDEWEB)

    Basirat-Tabrizi, H.; Saffar-Avval, M.; Assarie, M.R. [Amirkabir University of Technology, Tehran (Iran). Dept. of Mechanical Engineering

    2002-04-01

    A comprehensive heat and mass transfer model, based on the Eulerian two fluid model (TFM), developed for a packed-bed-drying process. The temperature and moisture content in a particle was considered with the conjugate effects between the gas and particles in a packed bed. Numerical study of the model was carried out on two-dimensional, axi-symmetrical cylindrical coordinates in order to investigate the effects of the different parameters such as particle size, variation of inlet gas temperature on the moisture content, and temperature of solid and gas outlet. For experimental observations, an experimental apparatus was designed and utilized. The theoretical results were then compared to the experimental data, which indicated good agreement. (author)

  7. Study of the Drying Kinetics of “Granny Smith” Apple in Fluid Bed Dryer

    Directory of Open Access Journals (Sweden)

    Darko Velić

    2007-12-01

    Full Text Available The drying characteristics of “Granny Smith” apple were investigated using a bench-scale fluidised bed drier at different temperatures and using blanching in hot water as pre treatment. Temperatures of fluidisation for non-treated and treated samples were 50, 60, 70 and 80 oC and airflow velocity 3.50 m s-1. The aim of the experiment was to get apples with approximately 9% water content, with good texture, rehydration capability and colour quality. The effect of temperatures and pre-treatment on the quality of dried apple samples was determined on the basis of colour and volume changes and reconstitution characteristics. Th e kinetic equations were estimated using logarithmic model. The results of the estimation have exhibited correspondence to experimental results. As a result of drying of non-treated apple at higher temperatures, drying time shortens, while rehydration properties improve. On the other hand, with the increase of the drying temperature, overall colour changes (ΔE of non-treated samples increase. The best results, shorter drying time and better rehydration properties, were obtained when samples were pre-treated by blanching in hot water.

  8. Cost analysis in support of minimum energy standards for clothes washers and dryers

    Energy Technology Data Exchange (ETDEWEB)

    1979-02-02

    The results of the cost analysis of energy conservation design options for laundry products are presented. The analysis was conducted using two approaches. The first, is directed toward the development of industrial engineering cost estimates of each energy conservation option. This approach results in the estimation of manufacturers costs. The second approach is directed toward determining the market price differential of energy conservation features. The results of this approach are shown. The market cost represents the cost to the consumer. It is the final cost, and therefore includes distribution costs as well as manufacturing costs.

  9. Dehydration of Traditional Dried Instant Noodle (Mee Siput) Using Controlled Temperature & Humidity Dryer

    Science.gov (United States)

    Mamat, K. A.; Yusof, M. S.; Yusoff, Wan Fauziah Wan; Zulafif Rahim, M.; Hassan, S.; Rahman, M. Qusyairi. A.; Karim, M. A. Abd

    2017-05-01

    Drying process is an essential step to produce instant noodles. Yet, the industries especially Small and Medium Enterprises (SMEs), is seeking for an efficient method to dry the noodles. This paper discusses the performance of an invented drying system which employed heating and humidifying process. The drying system was tested using 30 kilogram of the raw noodle known as “Mee Siput”. Temperature controlled system were used in the study to control the temperature of the drying process and prevent the dried noodles from damage by maintaining the temperature of lower than 80°C. The analysis shows that the system was drastically decreased the humidity from 80% to 40% just after 200 minutes of the drying process. The complete dehydration time of noodle has also decreased to only 4 hours from 16 hours when using traditional drying system without sacrificed the good quality of the dried noodle. In overall, the invented system believed to increase the production capacity of the noodle, reduce cost of production which would highly beneficial for Small Medium Industries (SMEs) in Malaysia.

  10. A low-cost ultrasonic spray dryer to produce spherical microparticles from polymeric matrices

    OpenAIRE

    2007-01-01

    The spray-drying technique has been widely used for drying heat-sensitive foods, pharmaceuticals, and other substances, because it leads to rapid solvent evaporation from droplets. This method involves the transformation of a feed from a fluid state into a dried particulate, by spraying the feed into a hot medium. Despite being most often considered a dehydration process, spray drying can also be used as an encapsulation method. Therefore, this work proposes the use of a simple and low-cost u...

  11. Improving the Sun Drying of Apricots (Prunus armeniaca) with Photo-Selective Dryer Cabinet Materials.

    Science.gov (United States)

    Milczarek, Rebecca R; Avena-Mascareno, Roberto; Alonzo, Jérôme; Fichot, Mélissa I

    2016-10-01

    Photo-selective materials have been studied for their effects on the preharvest quality of horticultural crops, but little work has been done on potential postharvest processing effects. The aim of this work was to characterize the effects of 5 different photo-selective acrylic materials (used as the lid to a single-layer sun drying cabinet) on the drying rate and quality of apricots (Prunus armeniaca). Photo-selective cabinet materials that transmit light in the visible portion of the solar spectrum accelerate the apricots' drying rate in both the early period of drying and the course of drying as a whole. These materials do not significantly affect the measured quality metrics during the first day of sun drying. However, when drying is taken to completion, some minor but significant quality differences are observed. Infrared-blocking material produces dried apricot with lower red color, compared to clear, opaque black, and ultraviolet-blocking materials. Clear material produced dried apricot with significantly lower antioxidant activity, compared to black and infrared-blocking materials. Using appropriate photo-selective drying cabinet materials can reduce the required sun drying time for apricots by 1 to 2 d, compared with fully shaded drying. Ultraviolet-blocking material is recommended to maximize drying rate and minimize quality degradation.

  12. 家用滚筒干衣机、滚筒洗干一体机性能认证技术规范%Technical Specification for Household tumble dryer,washer-dryer performance Certification

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ 大中城市消费者购买使用滚筒干衣机、特别是洗干一体机的比例明显上升,家庭占有率大幅度提高,但是产品性能质量参差不齐.如果产品设计的不甚合理,就会导致干燥效率下降,甚至无法将衣物彻底烘干,给国家的能源造成了巨大的浪费.

  13. 用旋风分离器干燥甘蔗渣%Cyclone as a Sugar Cane Bagasse Dryer

    Institute of Scientific and Technical Information of China (English)

    Jefferson Luiz Gomes Corr(e)a; Daniel Rezende Graminho; Maria Aparecida Silva; Silvia Azucena Nebra

    2004-01-01

    Drying of sugar cane bagasse was theoretically and experimentally studied in a cyclone. The experiments were carried out using hot air as drying agent. The influence of the cyclone conical part was studied. It was shown that the conical part has a great influence on the particle residence time and, consequently, on moisture reduction.Experimental results were alike industrial ones. CFX 4.4坰 from AEA Technology was used to simulate some experiments. Simulated and experimental results were close and showed that the presented model leads to a good prediction.

  14. 发梳式电吹风机的设计%Design of comb-type hair dryer

    Institute of Scientific and Technical Information of China (English)

    陈凯哲; 姚浩钢; 郑坤; 李孝禄

    2016-01-01

    本文介绍了一种将梳子与电吹风结合的发梳式电吹风机,运用温度/湿度控制,实现对头发的有效保护.包括发热模块、智能控制模块以及发梳式电吹风结构本体.控制芯片将可根据温度与湿度实时调整风力的大小,对头发智能吹风.本设计具有节能、护发等特点.

  15. Design of the Injection Mould for Hair Dryer Shell%风筒注塑模设计

    Institute of Scientific and Technical Information of China (English)

    林海雄; 康俊远

    2009-01-01

    通过对风筒外壳产吕结构和注塑成型存在的工艺问题进行了分析,选择苯乙烯-丁二烯-丙烯晴共聚物(ABS)的成型工艺参数,确定了该塑件的注塑模结构为一模两腔.设计了内外滑块侧抽芯机构、浇注系统和温度控制系统.结果表明:内滑块机构解决了内部空间较小倒扣塑件成型问题.

  16. Behavior of a portable solar dryer for pineapple fiber Comportamento de um secador solar para fibras de abacaxi

    National Research Council Canada - National Science Library

    Róger Moya; Marco Solano

    2012-01-01

    In Costa Rica, there has been a growing interest to use pineapple fiber from plant, for which current processes need to be improved or new processes need to be developed, with emphasis on drying methods...

  17. Energetic evaluation of a mechanical dryer (flex) to familiar agriculture; Avaliacao energetica de um secador mecanico (FLEX) para cafeicultura familiar

    Energy Technology Data Exchange (ETDEWEB)

    Donzeles, Sergio M.L. [Empresa de Pesquisa Agropecuaria de Minas Gerais (CTZM/EPAMIG), Vicosa, MG (Brazil). Centro Tecnologico da Zona da Mata], E-mail: slopes@ufv.br; Silva, Juarez S.; Martin, Samuel; Nogueira, R.M.; Silva, Jadir N.; Zanata, Fabio L. [Universidade Federal de Vicosa (DEA/UFV), MG (Brazil). Dept. de Engenharia Agricola], Emails: juarez@ufv.br, jadir@ufv.br, samuel.martin@ufv.br

    2009-07-01

    Actually, the coffee is one of the most important exportation crops of the country. The utilization of obsolete or unsuitable processes, specifically related to the coffee drying, it can to damage the final quality of the product, besides to result in a low profitability of the coffee growing. In this work a mechanical drier (flex) was built, for the familiar coffee growing, being subsequently evaluated, to the drying of peeled cherry coffee, by the realization of two tests: one with heating of the air using vegetable coal and other combining the use of solar heater with vegetable coal. Basing on the results, it was possible to conclude that the drying of coffee in the mechanical drier Flex can be carried out using vegetable coal as fuel as well as associating the use of the vegetable coal with the solar collector, to save energy. (author)

  18. Method of aeration disinfecting and drying grain in bulk and pretreating seeds and a transverse blow silo grain dryer therefor

    Science.gov (United States)

    Danchenko, Vitaliy G [Dnipropetrovsk, UA; Noyes, Ronald T [Stillwater, OK; Potapovych, Larysa P [Dnipropetrovsk, UA

    2012-02-28

    Aeration drying and disinfecting grain crops in bulk and pretreating seeds includes passing through a bulk of grain crops and seeds disinfecting and drying agents including an ozone and air mixture and surrounding air, subdividing the disinfecting and drying agents into a plurality of streams spaced from one another in a vertical direction, and passing the streams at different heights through levels located at corresponding heights of the bulk of grain crops and seeds transversely in a substantially horizontal direction.

  19. Analysis and Modeling of Wangqing Oil Shale Drying Characteristics in a Novel Fluidized Bed Dryer with Asynchronous Rotating Air Distributor

    Institute of Scientific and Technical Information of China (English)

    Yang Ning; Zhou Yunlong; Miao Yanan

    2016-01-01

    In order to replace the conventional distributor, a novel asynchronous rotating air distributor, which can optimize the drying ability of lfuidized bed and strengthen the drying performance of oil shale particles, is creatively designed in this study. The rotating speed of the asynchronous rotating air distributor with an embedded center disk and an encircling disk is regulated to achieve the different air supply conditions. The impacts of different drying conditions on the drying characteristic of Wangqing oil shale particles are studied with the help of electronic scales. The dynamics of experimental data is analyzed with 9 common drying models. The results indicate that the particles distribution in lfuidized bed can be improved and the drying time can be reduced by decreasing the rotating speed of the embedded center disk and increasing the rotating speed of the encircling disk. The drying process of oil shale particles involves a rising drying rate period, a constant drying rate period and a falling drying rate period. Regulating the air distributor rotating speed reasonably will accelerate the shift of particles from the rising drying rate period to the falling drying rate period directly. The two-term model ifts properly the oil shale particles drying simulation among 9 drying models at different air supply conditions. Yet the air absorbed in the particles’ pores is diffused along with the moisture evaporation, and a small amount of moisture remains on the wall of lfuidized bed in each experiment, thus, the values of drying simulation are less than the experimental values.

  20. Gene expression programming approach for the estimation of moisture ratio in herbal plants drying with vacuum heat pump dryer

    Science.gov (United States)

    Dikmen, Erkan; Ayaz, Mahir; Gül, Doğan; Şahin, Arzu Şencan

    2017-07-01

    The determination of drying behavior of herbal plants is a complex process. In this study, gene expression programming (GEP) model was used to determine drying behavior of herbal plants as fresh sweet basil, parsley and dill leaves. Time and drying temperatures are input parameters for the estimation of moisture ratio of herbal plants. The results of the GEP model are compared with experimental drying data. The statistical values as mean absolute percentage error, root-mean-squared error and R-square are used to calculate the difference between values predicted by the GEP model and the values actually observed from the experimental study. It was found that the results of the GEP model and experimental study are in moderately well agreement. The results have shown that the GEP model can be considered as an efficient modelling technique for the prediction of moisture ratio of herbal plants.

  1. Gene expression programming approach for the estimation of moisture ratio in herbal plants drying with vacuum heat pump dryer

    Science.gov (United States)

    Dikmen, Erkan; Ayaz, Mahir; Gül, Doğan; Şahin, Arzu Şencan

    2017-02-01

    The determination of drying behavior of herbal plants is a complex process. In this study, gene expression programming (GEP) model was used to determine drying behavior of herbal plants as fresh sweet basil, parsley and dill leaves. Time and drying temperatures are input parameters for the estimation of moisture ratio of herbal plants. The results of the GEP model are compared with experimental drying data. The statistical values as mean absolute percentage error, root-mean-squared error and R-square are used to calculate the difference between values predicted by the GEP model and the values actually observed from the experimental study. It was found that the results of the GEP model and experimental study are in moderately well agreement. The results have shown that the GEP model can be considered as an efficient modelling technique for the prediction of moisture ratio of herbal plants.

  2. Dehydration studies using a novel multichamber microscale fluid bed dryer with in-line near-infrared measurement

    DEFF Research Database (Denmark)

    Räsänen, Eetu; Rantanen, Jukka; Mannermaa, Jukka-Pekka

    2003-01-01

    of solid materials. The temperature and the moisture content of the process air were demonstrated to be significant factors for the solid-state stability of theophylline. The presented setup is a material and cost-saving approach for studying the influence of different process parameters on dehydration....... The materials studied were disodium hydrogen phosphates with three different levels of hydrate water and wet theophylline granules. Measured process parameters of fluid bed drying were logged, including in-line NIR signals. Off-line analyses consisted of X-ray powder diffraction patterns, Fourier transform NIR...

  3. 40 CFR 63.2251 - What are the requirements for the routine control device maintenance exemption?

    Science.gov (United States)

    2010-07-01

    ... maintenance exemption from the EPA Administrator for routine maintenance events such as control device... device is used to control a green rotary dryer, tube dryer, rotary strand dryer, or pressurized...

  4. Development Application of Multiple Stage Spray Granulating Dryer%多级喷雾造粒干燥器的开发及应用

    Institute of Scientific and Technical Information of China (English)

    翁颐庆

    2002-01-01

    本文主要介绍一种新型造粒干燥设备,它是将我们熟悉的喷雾与流态化技术相结合的造粒、干燥设备.其生产简单,操作控制方便,适用范围广.特别对一些热敏性物料,及需要加入喷涂剂如香精、卵磷脂、润滑剂、防尘剂、缓蚀剂等物料的造粒工艺更有其优越性.

  5. 混联式太阳能果蔬烘干机的研制%Design of hybrid type mixed-mode solar dryer for fruits and vegetables

    Institute of Scientific and Technical Information of China (English)

    马洪江; 王海; 王颉

    2009-01-01

    为了解决新疆地区传统果蔬干制工艺存在的问题,提高农产品加工质量,根据该地区的气候特点及农产品特点,确定了混联式太阳能果蔬烘干机的总体结构方案,完成了集热、控制和烘干等丰要系统设计计算、参数设定,成功进行了葡萄烘干试验,通过葡萄烘干试验表明,比传统干燥方式缩短时间66.7%,绿级品率由低于35%提高到79.19%,该设备可提高新疆农产品的干制效率,促进该地区农业的发展.

  6. 膨胀干燥机螺杆轴断裂分析%Fracture analysis of screw shaft in extruder-dryer

    Institute of Scientific and Technical Information of China (English)

    陈珏; 潘红良; 唐世华

    2009-01-01

    膨胀干燥机螺杆轴在实际使用中经常发生断裂事故,为了保证膨胀干燥机的正常运行,就螺杆轴的断裂原因进行了分析.结果表明:螺杆轴断裂的主要原因是轴材存在明显的质量问题,热处理和机械性能均未达到预期要求,造成应力腐蚀疲劳断裂.就轴的使用要求提出一些建议.

  7. 螺旋式碎片干燥机排潮系统的改进%Improvement of Exhaust System in Screw Type Scrap Dryer

    Institute of Scientific and Technical Information of China (English)

    陶智麟

    2007-01-01

    螺旋式碎片干燥设备的排潮系统由于设计不合理,经常造成干燥后碎片含水率偏高且不稳定,为此对其排潮系统进行了改进.将原来的自然排潮改为机械排潮,改进后螺旋式碎片干燥机加工后碎片,日平均含水率、日最高含水率、日最低含水率全部符合工艺规范要求(11%~13%),且日含水率极差均不超过1.2%.机械排潮方式提高了螺旋式碎片干燥设备的排潮能力,且不受外界条件变化的影响,提高了碎片的干燥质量.

  8. Breakage and maintenance of dryer journal of 3400mm paper machine%3400mm纸机烘缸轴颈磨损与维修

    Institute of Scientific and Technical Information of China (English)

    王乐伟

    2001-01-01

    @@2000年10月6日,山东太阳纸业股份有限公司二分厂3400mm纸机烘缸传动侧发生一起因轴承毁坏而把烘缸轴颈磨损的恶性事故,造成较大经济损失,对此事故的原因做了如下分析及探讨。

  9. Design of the hair dryer cover based on reverse engineering%基于逆向工程的吹风机后盖造型设计

    Institute of Scientific and Technical Information of China (English)

    赵让乾; 马宗正

    2013-01-01

    利用三维光学面扫描系统对吹风机后盖扫描获得其点云数据并进行优化,完成后将点云保存为.igs格式的文件.将此文件导入UG NX6.0软件中进行曲线和曲面的二次重构,改进了吹风机后盖的通风造型,实现了产品性能的快速改造设计和制造,提高了产品的设计效率和投放市场的速度.

  10. NC Machining of the Concave Moulds for Electric Hair Dryer Based on MasterCAM%基于MasterCAM电吹风凹模的数控加工

    Institute of Scientific and Technical Information of China (English)

    陈丽华

    2013-01-01

    以曲面加工中非常典型的电吹风凹模零件加工为例,以MasterCAM系统为加工平台,对零件特点进行分析,对加工难点提出了策略,规划了加工工艺,解决了复杂曲面的加工,取得了良好的加工效果.

  11. NC Machining of Hair Dryer Shell Punch Based on MasterCAM%基于MasterCAM的电吹风外壳凸模数控加工

    Institute of Scientific and Technical Information of China (English)

    宋卫东

    2010-01-01

    为了提高模具加工的质量和效率,以电吹风外壳西模为例,介绍了用MasterCAM软件进行数控编程的基本方法,重点论述了电吹风外壳凸模加工工艺方案的合理性,并对电吹风外壳凸模进行了仿真模拟加工.

  12. 关于电吹风的减振与降噪研究%Study on Reduction of Vibration and Noise of Hair Dryer

    Institute of Scientific and Technical Information of China (English)

    石趁义; 李黎; 战嘉恺; 宁和

    2000-01-01

    电吹风是小家电产品之一。优质电吹风的设计、制造是属于低噪声、大风量、微型风 机的设计问题。在电吹风产生噪声的问题中,气流噪声是主要的,解决好降低噪声和电热丝不呈 红色之间的矛盾是复杂、艰难而又重要的问题。本文介绍了降低电吹风噪声的三项有效研究措 施。%Hair dryer is one of small household electrical appliances. Designing a superior hair dryer is concern of some questions including  low noise、density of wind、micro-motor and so on.The problem of noise  creating in hair dryer mainly focus on the air current noise.To solve  the contradiction between low noise and cool the heatproof wire in order  to keep it from heat-red is a complex、diffcult and very important duty .Three efficient methods in reducing hair dryer noise are introduced.

  13. 小巧型电吹风检测常见不合格项分析%Disqualification analysis of minitype hair dryer

    Institute of Scientific and Technical Information of China (English)

    王乐涛; 邹苗章; 李建祥

    2005-01-01

    本论文介绍了小巧型电吹风两种基本的工作原理,并给出了一种类型的电吹风的完整电路,分析其在安规试验中常见的几种不合格项,主要有非正常试验不合格,爬电距离、电气间隙不合格.具体的整改措施有:选用合适自复位热断路器、外壳用耐火耐热型塑料、合理布置导线、电源线连接改进设计等.

  14. Design of Injection Molds for Hair Dryer Shell Based on UG%基于UG的吹风机外壳注塑模具设计

    Institute of Scientific and Technical Information of China (English)

    潘祖聪; 何芳

    2015-01-01

    UG NX(简称UG)是一款强大的CAD/CAM集成软件,MoldWizard是UG应用的一个模块,专门用于注塑模具设计.以吹风机外壳为例,阐述了基于UG的注塑模具设计的过程和方法.

  15. Optimization Design of Injection Mold Gate for Hair Dryer%吹风机注塑模具浇口的优化设计

    Institute of Scientific and Technical Information of China (English)

    吕迅; 金杨福; 厉淦

    2008-01-01

    浇口位置在注塑成型过程中起关键性作用.介绍专业注塑模分析软件MPI在吹风机注塑模具浇口位置设计的应用,从产品的填充时间、充模压力、流动前沿温度和熔接痕等方面对不同的浇口设计方案进行对比.分析表明,两浇口位置方案具有注射压力、锁模力小,熔接痕和气穴数量少的优点,是较佳的浇口位置方案.

  16. Equipment for biomass. Dryers. Drying, crushing, aggregating of agro-industrial products; Materiels pour la biomasse, les secheurs, sechage, broyage, agglomeration de produits agro-industriels

    Energy Technology Data Exchange (ETDEWEB)

    Deur, O. [Promill, 28 - Serville (France)

    1997-12-31

    The French society Promill has developed complete units for the drying, crushing and aggregating of agro-industrial products (beet roots, agricultural wastes, lucerne, maize, etc.). Drying is conducted in a three-pass drum, using any type of fuel (fuel oil, gas, electric power, coal), and ensuring a thermal yield of 680 kCal/kg and ash emission rates complying with French and European legislation. Granulation is conducted with vapour addition, with a granulate flowrate reaching 15 T/h. Crushing is carried out in a hammer mill

  17. Effect of openings collectors and solar irradiance on the thermal efficiency of flat plate-finned collector for indirect-type passive solar dryer

    Science.gov (United States)

    Batubara, Fatimah; Dina, Sari Farah; Klaudia Kathryn Y., M.; Turmuzi, M.; Siregar, Fitri; Panjaitan, Nora

    2017-06-01

    Research on the effect of openings solar collector and solar irradiance to thermal efficiency has been done. Solar collector by flat plate-finned type consists of 3 ply insulator namely wood, Styrofoam and Rockwool with thickness respectively are 10 mm, 25 mm and 50 mm. Absorber plate made of aluminum sheet with thickness of 0.30 mm, painted by black-doff. Installation of 19 units fins (length x height x thickness: 1000x20x10 mm) on the collector will increase surface area of absorber so it can receive much more solar energy. The solar collector cover is made of glass (thickness of 5 mm). During the research, the solar irradiance and temperature of collector are measured and recorded every five minutes. Temperature measurement performed on the surface of the absorber plate, inside of collector, surface cover and the outer side insulator (plywood). This data is used to calculate the heat loss due to conduction, convection and radiation on the collector. Openings of collectors vary as follows: 100%, 75%, 15% and 0% (total enclosed). The data collecting was conducted from 09.00 am to 17.00 pm and triplicates. The collector thermal efficiency calculated based on the ratio of the amount of heat received to the solar irradiance absorbed. The results show that each of openings solar collector has different solar irradiance (because it was done on a different day) which is in units of W/m2: 390 (100% open), 376 (75% open), 429 (15% open), and 359 (totally enclosed). The highest thermal efficiency is in openings variation of 15% opened. These results indicate that the efficiency of the collector is influenced by the solar irradiance received by the collector and the temperature on the collector plate. The highest thermal efficiency is in variation of openings 15%. These indicate that the efficiency of the collector was influenced by solar irradiance received by the collector and openings of the collector plate.

  18. MATHEMATICAL MODELING AND EXPERIMENTAL STUDY ON THIN LAYER HALOGEN DRYER OF STRAWBERRY AND STUDY IT’S EFFECT ON ANTIOXIDANT ACTIVITY

    Directory of Open Access Journals (Sweden)

    Asaad Rehman Saeed Al-Hilphy

    2013-01-01

    Full Text Available The halogen drying characteristics of strawberry (Fragaria ananassa Duch slices were investigated. Drying experiments were carried out a three different drying temperatures (60, 70 and 80°C. The effect of drying temperature on the drying rate, drying coefficient, efficiency, effective diffusivity of the strawberry and antioxidant activity were evaluated. The best model for describing the halogen drying process was chosen by fitting nine commonly used drying models. The effective moisture diffusivity and activation energy were calculated using an infinite series solution of Fick’s diffusion equation. The results showed that increasing drying temperature accelerate the halogen drying process. As well as, increasing of drying rate, drying rate constant, drying coefficient and effective diffusivity. All drying experiments had only falling rate period. The goodness of fit tests indicated that the proposed modified page model gave the best fit to experimental results at 70 and 80°C, but page model gave the best fit to experiment results at temperature of 60°C. The effective diffusivity varied from 7.53×10-9 -2.52×10-8 m2/sec. Effective diffusivity was satisfactorily by an Arrhenius type relationship with activation energy with in 60-80°C temperature range. The ability of reducing power of the ferrous ion can taken as an indicator for the ability or antioxidant power for strawberry extracted.

  19. The economy analysis of new energy saving technique of spaying dryer%喷雾干燥器节能新技术及经济分析

    Institute of Scientific and Technical Information of China (English)

    康智勇; 杜夏芳; 刘纯

    2006-01-01

    陶瓷工业是一个高能耗产业,喷雾干燥器又是陶瓷行业能耗较高的设备之一(喷雾干燥器消耗能量占陶瓷砖生产能耗的30%左右),所以节能降耗是陶瓷企业追求的目标。特别是目前随着能源日益紧张及市场竞争的日益激烈,降低喷雾干燥器的能耗,节约能源及降低生产成本,对提高企业的经济效益,促进陶瓷工业的可持续发展具有深远而重要的意义。

  20. SKIM MILK POWDER, WHEY POWDER AND MILK AND WHEY MIXTURES IN POWDER PRODUCED IN MINISPRAY DRYER:ISOTHERM ANALYSIS AND APPLICATION OF THE BET MODEL

    OpenAIRE

    Perrone, Ítalo Tuler; Carvalho, Antônio Fernandes de; Pereira, João Pablo Fortes; Stringueta, Paulo César; Silva, Paulo Henrique Fonseca da

    2013-01-01

    In this study whey powders and skim milk powder were produced in laboratory scale. Water vapor sorption for each powder was measured gravimetrically. The results of the isothermal adsorption were in agreement with the BET model and the quantities of water in the monolayer, obtained by the model, were less than the total quant ities of water in the powder s. Laboratory scale production of milk and whey powders showed that increasing whey percentage in the mixture of milk and whey before drying...

  1. Multi-criteria optimization of dryers: use of neural networks and genetical algorithms; Optimisation multi-criteres de sechoirs: utilisation des reseaux de neurones et algorithmes genetiques

    Energy Technology Data Exchange (ETDEWEB)

    Hugget, A.; Nadeau, J.P.; Sabastian, P. [Ecole Nationale Superieure des Arts et Metiers, 33 - Talence (France)

    1997-12-31

    Drying remains a complex process to model and thus to optimize. In this paper a new approach is proposed which allows to perform a compression in the drying model in order to integrate it using neural networks. The simulation times become very small and allow to test a great number of configurations. This decisive advantage allows to perform a multi-criteria optimization using hybrid genetical algorithms based on technical-economical criteria like drying cost, production or final product quality. (J.S.) 10 refs.

  2. 太阳能热带牧草干燥机的设计与试验%Design and Experiment of Solar Dryer for Tropical Forage

    Institute of Scientific and Technical Information of China (English)

    张浩栋; 王娟; 朱永超

    2014-01-01

    The drying methods of tropical forage are mainly natural drying method and energy -consuming drying physico-chemical method .The drying technology is backward , which can lead to larger energy consumption, losing nutrient and lower efficiency .Based on stylosanthes cv .Reyan 2 design , a solar tropical forage drier can be invented .We can make full use of abundant solar energy in Hainan Province .Forage uniform drying can be achieved after using the three-layer mesh transmission apparatus of grass and air uniform temperature control system .The average operating temperature of this drier on the experiment is 58 centidegrade;the maximum temperature of the hothouse is 67 centidegrade;the efficiency of the solar collector reaches 57.2 percent;the efficiency of forage drying is 0.52 t/d, the wet basis moisture content af-ter drying is 17 percent or less .Compared with natural drying method ,the nutrient of forage dried by solar tropical forage drier can be generally better saved , which can meet the production need of tropical forage drying .%热带牧草的干燥方式主要是自然晾晒和利用物理化学方法的耗能干燥,干燥技术落后,耗能大,营养损失较大,效率较低。针对热研2号柱花草设计研制出一种太阳能热带牧草干燥机,利用海南丰富的太阳能资源,采用3层网状输草装置和匀风控温系统,实现牧草均匀干燥加工。该干燥机试验时段平均工作温度为58℃,干燥室最高温度为67℃,太阳能集热器效率达到57.2%,牧草干燥效率为0.52t/d,干燥后湿基含水率≤17%。牧草营养成分与自然晒干相比总体保留较好,满足热带牧草干燥的生产要求。

  3. 77 FR 8575 - National Emissions Standards for Hazardous Air Pollutants: Secondary Aluminum Production

    Science.gov (United States)

    2012-02-14

    ... scrap shredders, thermal chip dryers, scrap dryers/delacquering kilns/decoating kilns, group 1 furnaces... following affected sources: aluminum scrap shredders (subject to PM standards), thermal chip dryers (subject... scrap shredders; afterburners for control of THC and D/F from thermal chip dryers; afterburners...

  4. 40 CFR 63.2241 - What are the work practice requirements and how must I meet them?

    Science.gov (United States)

    2010-07-01

    ... SOURCE CATEGORIES National Emission Standards for Hazardous Air Pollutants: Plywood and Composite Wood... rotary dryers instead of the work practices for dry rotary dryers. If you have a hardwood veneer dryer or veneer redryer, you may choose to designate your hardwood veneer dryer or veneer redryer as a...

  5. 40 CFR 60.733 - Reconstruction.

    Science.gov (United States)

    2010-07-01

    ... PERFORMANCE FOR NEW STATIONARY SOURCES Standards of Performance for Calciners and Dryers in Mineral Industries... facility” under § 60.15. Calciner and dryer equipment subject to high temperatures and abrasion are:...

  6. Non-aerated burner reduces drying costs; Diffusiebrander maakt drogen goedkoper

    Energy Technology Data Exchange (ETDEWEB)

    Koopman, F.P. [Gasunie Research, Groningen (Netherlands)

    1998-10-01

    Gas-fired tumble dryers are more expensive than electric dryers. However, consumers appear to be more satisfied about the drying results of gas-fired tumble dryers. Since premix burner lead to higher natural gas conversion costs, Gasunie Research developed a non-aerated burner, featuring a simple design and a limited number of parts. Moreover, it can be manufactured at low cost, which should improve the competitiveness of the gas-fired tumble dryer

  7. 16 CFR Appendix A to Part 423 - Glossary of Standard Terms

    Science.gov (United States)

    2010-01-01

    ... clean with damp cloth or sponge. 3. Drying, All Methods: a. “Tumble dry”—use machine dryer. When no temperature setting is given, machine drying at a hot setting may be regularly used. b. “Medium”—set dryer at medium heat. c. “Low”—set dryer at low heat. d. “Durable press” or “Permanent press”—set dryer...

  8. 40 CFR 63.9652 - What definitions apply to this subpart?

    Science.gov (United States)

    2010-07-01

    ... existing ore crushing and handling operation, ore dryer, indurating furnace, or finished pellet handling... water, such as wet milling and wet magnetic separation. Ore dryer means a rotary dryer that repeatedly tumbles wet taconite ore concentrate through a heated air stream to reduce the amount of...

  9. 40 CFR 60.734 - Monitoring of emissions and operations.

    Science.gov (United States)

    2010-07-01

    ... operator of an affected facility subject to the provisions of this subpart who uses a dry control device to... clay vibrating grate dryer, a bentonite rotary dryer, a diatomite flash dryer, a diatomite rotary... section. (d) The owner or operator of an affected facility subject to the provisions of this subpart...

  10. 76 FR 19087 - Energy Conservation Program for Consumer Products: Publication of the Petition for Waiver and...

    Science.gov (United States)

    2011-04-06

    ... Electric (75 FR 13122, Mar. 18, 2010). BSH claims that its condenser clothes dryers cannot be tested... washing machines, clothes dryers, refrigerator-freezers, ovens, microwave ovens, dishwashers, and vacuum... the effects on space heating and cooling requirements are considered. The air lost from dryer...

  11. 40 CFR 63.605 - Monitoring requirements.

    Science.gov (United States)

    2010-07-01

    ... rock dryer or phosphate rock calciner subject to the provisions of this subpart shall install... either the mass flow of phosphorus-bearing feed material to the dryer or calciner, or the mass flow of product from the dryer or calciner. The monitoring system shall have an accuracy of ±5 percent over...

  12. 40 CFR 60.403 - Monitoring of emissions and operations.

    Science.gov (United States)

    2010-07-01

    ... of the gases discharged into the atmosphere from any phosphate rock dryer, calciner, or grinder. The... operate a device for measuring the phosphate rock feed to any affected dryer, calciner, or grinder. The... phosphate rock dryer, calciner, or grinder subject to paragraph (a) of this section exceeds the...

  13. 40 CFR Table 3 to Subpart Dddd of... - Work Practice Requirements

    Science.gov (United States)

    2010-07-01

    ... Standards for Hazardous Air Pollutants: Plywood and Composite Wood Products Pt. 63, Subpt. DDDD, Table 3... veneer dryers Process less than 30 volume percent softwood species on an annual basis. (3) Softwood veneer dryers Minimize fugitive emissions from the dryer doors through (proper maintenance...

  14. Designing of the Spin-flash Dryer Used to Dry Pesticide%农药干燥用旋转闪蒸干燥机的工艺设计

    Institute of Scientific and Technical Information of China (English)

    常桂霞

    2007-01-01

    介绍了用于干燥农药滤饼的旋转闪蒸干燥机的设计方法.旋转闪蒸干燥机结构紧凑,集干燥、粉碎、分级为一体,是流化技术、旋流技术、粉碎分级技术、喷动技术及对流传热技术的优化组合,简化了生产工艺流程,节省了设备投资和运转费用.

  15. Design and Experiment of the 5HRE-6 Hert Solar Dryer for Fruit%5HRT—8型果蔬全自动太阳能热泵组合干燥设备研制与试验

    Institute of Scientific and Technical Information of China (English)

    沈卫强; 刘小龙; 田翔; 刘娜; 张杰

    2011-01-01

    为了充分利用太阳能和空气热能,加快新疆果品产后制干加工的发展,研制了一种太阳能与空气源热泵组合干燥设备,该机利用太阳能和空气热能为热源,可完成果品和蔬菜的干燥加工.介绍了该机的工作原理、主要工作部件结构特点,并进行了无核紫葡萄的干燥试验.

  16. Design and Experimental Studies of the GTG-6 Type Solar Dryer for Fruit%GTG-6型果品太阳能干燥器研制与试验

    Institute of Scientific and Technical Information of China (English)

    沈卫强; 杨军; 马月虹; 刘娜; 江英

    2009-01-01

    为了充分利用太阳能,加快新疆果品产后制干加工的发展,研制了一种温室-集热器型果品太阳能干燥设备.该机利用太阳能为热源,在常规风机辅助下,可完成杏等果品的干燥加工.为此,介绍了该机的工作原理和主要工作部件的结构特点,并进行了杏的太阳能干燥试验研究.

  17. 新型烟道气蔗渣干燥器的试验研究%Experimental Investigation on a Novel Screw-conveying Bagasse Experimental Investigation on a Novel Screw-Conveying Bagasse Dryer with Flue Gas

    Institute of Scientific and Technical Information of China (English)

    周少基; 梁勇; 梁卫

    2010-01-01

    开发了新型螺旋输送烟道气蔗渣干燥器.建立螺旋输送烟道气蔗渣干燥器实验装置,通过改变进风方式,风量、蔗渣处理量、烟气温度,实验研究干燥器的阻力特性和干燥效果.实验结果表明:当螺旋输送机采用最佳进气方式,蔗渣宅气比为0.24 kg/m3及烟气温度约为150℃时,蔗渣脱水率达22.5%;在适用的风速范围内,干燥器的阻力小于400 Pa.该蔗渣干燥器具有设备紧凑、操作稳定性和安全率高等特点,具有良好的工业应用前景.

  18. Hair Dryer Punch Processing based on MasterCAM X4 Simulation%基于MasterCAMX4的吹风简凸模模拟加工

    Institute of Scientific and Technical Information of China (English)

    刘汉华

    2014-01-01

    阐述了用MasterCAMX4软件编制吹风筒凸模数控编程的基本加工工艺过程及模拟加工,设计了比较合理的加工方式和优化了相关参数的设置,整个模拟过程可设置毛坯的形状和大小,进行刀具路径安全检查,确保加工更加安全可靠,在保证加工质量的前提下提高零件加工的效率,显著提高了生产效率和经济效益.

  19. CAE-based design of injection mould for casing cover of hair dryer%基于CAE分析的风筒壳后盖注射模设计

    Institute of Scientific and Technical Information of China (English)

    戚春晓; 南雷英; 李万里

    2009-01-01

    分析了风筒壳后盖的结构特点.用Moldflow软件对塑件的注射成型过程进行了CAE模拟分析,确定了模具的浇注系统、冷却系统.在模拟分析的基础上运用UG NX4.0软件完成了模具设计.模具采用潜伏式浇口、斜导柱侧抽芯及斜顶抽芯机构及合理的冷却系统,模具结构设计合理.

  20. 电吹风火灾残留物中电热丝的鉴定技术%Appraisal Technology of Heating Wire in Fire Remains for Hair Dryer

    Institute of Scientific and Technical Information of China (English)

    张辉; 邹红

    2010-01-01

    模拟电吹风正常使用、通电过热、正常使用后受火灾作用和通电过热后受火灾作用,获得在不同试验条件下的电吹风火灾残留物.用扫描电子显微镜对电吹风火灾残留物中的电热丝显微形貌进行观察.结果表明:在不同试验条件下,电热丝的显微形貌有明显的不同.因此,利用扫描电子显微镜观察电吹风电热丝的显微形貌,可以直观、快速地鉴别电吹风在火灾前所处的状态,为电吹风火灾事故的认定提供了一种新的技术方法.

  1. 基于Pro/E和Moldflow的电吹风制品注射成型工艺分析%Analysis of Injection Molding Technology of Hair Dryer Products Based on Pro/E and Moldflow

    Institute of Scientific and Technical Information of China (English)

    董中宁; 林伟; 李延鑫; 曹弥

    2013-01-01

    采用逆向工程技术对电吹风外壳进行实物采集、数据测量,然后采用Pro/E三维设计软件对电吹风的外壳进行实体设计,生成组装图和爆炸图;以电吹风的手柄为例,采用Moldflow模拟软件对该塑料制品进行注塑成型工艺模拟分析.重点进行最佳浇口位置、冷却质量、流动质量以及成型条件分析.结果表明:Moldflow软件能够分析结果并指出存在的问题,使电吹风手柄的成型质量得以提高,减少了缺陷的产生,从而达到降低生产成本、缩短生产周期的目的.

  2. Uso de plasma suíno desidratado por Spray-Dryer na dieta de leitões desmamados precocemente The use of Spray-Dried porcine plasma in early-weaned pig diets

    Directory of Open Access Journals (Sweden)

    Eduardo Afonso F. Butolo

    1999-04-01

    Full Text Available O objetivo deste trabalho foi avaliar o uso do plasma suíno desidratado (PSD, na dieta de leitões desmamados aos 21 dias de idade. Cento e vinte leitões, com peso médio inicial de 5,75 kg, foram usados para testar os níveis de inclusão de 0; 2,5; 5,0; e 7,5% de plasma na fase 1 (0 a 14 dias e o seu efeito na fase 2 (14 a 28 dias. À exceção dos leitões mantidos em dieta controle, o restante foi alimentado com ração inicial com 2,5% PSD e 2,5% de hemácias desidratadas no período 15 a 28 dias pós-desmama. As dietas foram formuladas para conter nas fases 1 e 2, respectivamente, 1,40 e 1,20% de lisina, 0,54 e 0,41% de metionina e 15 e 8% de lactose. Foi usado delineamento experimental em blocos casualizados, com cinco repetições por tratamento e seis animais por unidade experimental. O consumo médio diário de ração aumentou linearmente, nas fases 1 e 2, com o aumento de PSD na ração. No período de 0 a 28 dias, houve resposta linear para o consumo médio diário de ração para os níveis de PSD da fase 1. O plasma estimulou maior consumo de ração pré-inicial, nas duas semanas subseqüentes ao desmame. Este efeito foi mantido durante a segunda fase (15 a 28 dias pós-desmame, quando foi usada na ração inicial combinação de 2,5% de plasma e 2,5% de hemácias desidratada.The objective of this work was to evaluate the spray-dried porcine plasma (SDPP in the diet of 21 day-weaned pig. One hundred and twenty piglets averaging 5.75 kg of initial weight were used to test the inclusion levels of 0, 2.5, 5.0, and 7.5% of porcine plasma on phase 1 (from 0 to 14 days and its effects on phase 2 (from 15 to 28 days. Except for the piglets in the control diet, all other animals were fed a starter diet with 2.5% of SDPP and 2.5% of spray-dried red blood cell (SDBC during 15 to 28-day-post weaning period. The diets were formulated to contain in the phases 1 and 2, respectively, 1.4 and 1.2% of lysine, .54 and .42% of methionine, and 15 and 8% of lactose. A randomized block design with five replications and six animals per experimental unit was used. Average daily feed intake increased linearly in the phases 1 and 2, with the increasing level of SDPP. For overall period (from 0 to 28 days, there was linear response of average daily feed intake to the SDPP levels in the phase 1.The SDPP stimulated higher daily feed intake during the two weeks after weaning. This effect was maintained during the second phase (15 to 28 days post weaning, when a combination of 2.5% SDPP and 2.5% SDBC was used.

  3. Evaluation of Ohio fly ash/hydrated lime slurries and Type 1 cement sorbent slurries in the U.C. Pilot spray dryer facility. Final report, September 1, 1993--August 31, 1994

    Energy Technology Data Exchange (ETDEWEB)

    Keener, T.C.; Khang, S.J.; Meyers, G.R. [Cincinnati Univ., OH (United States)

    1995-02-01

    The objectives of this year`s work included an evaluation of the performance of fly ash/hydrated lime as well as hydrated cement sorbents for spray drying adsorption (SDA) of SO{sub 2} from a simulated high-sulfur flue gas. These sorbents were evaluated for several different hydration methods, and under different SDA operating conditions. In addition, the physical properties of surface area and porosity of the sorbents was determined. The most reactive fly ash/hydrated lime sorbent studied was prepared at room temperature with milled fly ash. Milling fly ash prior to hydration with lime did have a beneficial effect on calcium utilization. No benefit in utilization was experienced either by hydrating the slurries at a temperature of 90{degrees}C as compared to hydration at room temperature, or by increasing hydration time. While the surface areas varied greatly from sorbent to sorbent, the pore size distributions indicated ``ink bottle`` pores with surface porosity on the order of 0.5 microns. No correlation could be drawn between the surface area of the sorbents and calcium utilization. These results suggest that the composition of the resulting sorbent might be more important than its surface area. The most effective sorbent studied this year was produced by hydrating cement for 3 days at room temperature. This sorbent provided a removal efficiency and a calcium utilization over 25 percent higher than baseline results at an approach to saturation temperature of 30{degrees}F and a stoichiometric ratio of 0.9. A maximum SO{sub 2} removal efficiency of about 90 percent was experienced with this sorbent at an approach to saturation temperature of 20{degrees}F.

  4. Improvement on electric controller circuit of JKG series dual-tower air dryer%JKG系列双塔空气干燥器电控器电路改进

    Institute of Scientific and Technical Information of China (English)

    潘朝晖

    2005-01-01

    针对JKG系列双塔空气干燥器失效,影响机车制动系统工作可靠性的故障现象,分析了原因,并对双塔空气干燥器电控器电路作了改进.改进后的干燥器在SS7型机车上得到运用,经受了考验.

  5. 核桃气体射流冲击干燥特性及干燥模型%Drying Characteristics and Model of Walnut in Air-Impingement Jet Dryer

    Institute of Scientific and Technical Information of China (English)

    赵珂; 肖旭霖

    2015-01-01

    [Objective] In order to improve the dried walnut quality, shorten the drying time, the effects of different conditions on the walnut air-impingement jet drying were studied and the activation energy for drying was obtained and the optimum drying model was selected.[Method] Using the method of energy saving technology of dry heat pipe combined with a self-made gas jet impingement equipment, in 9 groups of an experiment, effects of different jet air temperatures (40℃, 50℃ and 60℃) and air velocities (11, 12 and 13 m·s-1) on the drying characteristics of materials, effective moisture diffusion coefficient and activation energy were studied, at the same time, through the statistical data selection for the fitting drying models, 5 drying kinetics models were established. The 5 models are the Page model, the Modified Page model, the Logarithmic model, the Herdenson and Pabis model, and the Lemus model. The data were processed by using the DPS, after finishing the fitting, a parametric equation was obtained the final generalMR andt.[Result] Compared to the most results of food material drying test, air-impingement jet drying of walnut mainly occurred in the falling rate drying period, and there was no constant drying rate stage. Air temperature had large influence on each stage of walnut air impingement. With the increase of the air temperature values, the drying rate was rising and the MR was decreased. The air velocity almost had no influence on the drying time, but had a certain influence on the rate of surface water vaporizing stage by increasing the drying time. The air velocity almost had no influence on the drying rate of internal moisture transfer stage had almost no influence, and by employing this feature, a method of changing the wind temperature and wind speed could be used in different periods, so not only the drying time was shortened, but also the purpose of energy saving was achieved. Overall, for shortening the drying time, the order of the influence was air temperature>wind speed. The drying rate of the air-impingement jet drying of walnut increased with the increase of air temperature, while had no effect by the air velocity increasing. Fick’s second law was used to calculate the effective moisture diffusivity of walnut in drying process and the values were in the range of 0.9674×10-11 to 2.2231×10-11m2·s-1. Because of its shell structure so that the effective moisture diffusion coefficient was 1-3 orders of magnitude lower than other food materials. The activation energy was increased with the increase of the air velocity and the lowest activation energy was 27.644 kJ·mol-1. The five models had a higher fitting degree, and could better describe the walnut air impingement drying. The Modified Page model gave the highest coefficient of determination (R2), the lowest chi-square (χ2) and root mean square (RMSE). Based on the Modified Page model, regression analysis by using the DPS, a parameter equation was established between generally applicable moisture ratio (MR) for walnut air impingement drying and time (t) in the circumstance where the temperature of wind is 40-60℃ and the speed of wind is 11-13 m·s-1.[Conclusion] Air temperature and air velocity had influence on the drying curve, the drying rate curve, effective moisture diffusion coefficient and activation energy. According to the fitting result of the fitted values and the observated values under different conditions, the optimal drying condition was that the air temperature is 50℃ and the wind speed was 13 m·s-1. The Modified Page and Page models could properly describe the air-impingement jet drying behavior of walnut and could be used when the drying air temperature between 40 to 60℃, air velocities between 11 to 13 m·s-1. The Modified Page model fitting degree higher, it is the optimal model of the walnut air impingement drying.%【目的】研究不同条件对核桃气体射流冲击干燥的影响,提高核桃干制品质、缩短干燥时间,得到干燥所需活化能并筛选出最适干燥模型。【方法】

  6. SECAGEM DE SEMENTES DE SOJA EM SILO COM DISTRIBUIÇÃO RADIAL DO FLUXO DE AR: I. MONITORAMENTO FÍSICO DRYING OF SOYBEAN SEEDS IN A RADIAL AIR FLOW DRYER: I. PHYSICAL MONITORING

    Directory of Open Access Journals (Sweden)

    LUIZ CARLOS MIRANDA

    1999-11-01

    Full Text Available O trabalho foi desenvolvido com o objetivo de avaliar a evolução física do processo de remoção de água das sementes em secador estacionário, com cilindro central perfurado e distribuição radical de ar. A pesquisa foi conduzida com sementes de soja, variando o fluxo (26,9, 28,4 e 33,2 m³/minuto/t e a temperatura do ar insuflado (42, 46 e 50ºC, considerando a posição das sementes (17, 34 e 51 cm em relação ao cilindro de insuflação e o tempo de secagem (zero a doze horas, com intervalos de duas horas. Foram caracterizados o ar ambiente, o ar insuflado, as temperaturas e os teores de água da massa, as velocidades e curvas de secagem. As avaliações realizadas destacaram vantagens físicas operacionais da combinação de 28,4 m³/minuto/t com 46ºC e o contrário, com a combinação de 26,9 m³/minuto/t com 42ºC.The purpose of this research was to study several physical parameters of soybean seed drying submitted to stationary process with radial air distribution by combining different air flows (26.9, 28.4 and 33.2 m³/minute/ton and temperatures (42, 46 and 50ºC, considering seed positions in the seed mass (17, 34 and 51 cm in relation to the insuflation cylinder and drying periods (zero to twelve hours with two-hour intervals. Environmental air, insuflation air, seed temperatures, moisture content of seeds, drying speed and drying curves were characterized. Considering the evaluated parameters during the drying process, the physical advantages of the combination of 28.4 m³/minute/ton with 46ºC, and the desadvantage of the combination of 26.9 m³/minute/ton with 42ºC were observed.

  7. LEITE EM PÓ DESNATADO, SORO EM PÓ E MISTURAS DE LEITE E SORO EM PÓ OBTIDOS EM MINISPRAY DRYER: ANÁLISE DE ISOTERMA E APLICAÇÃO DO MODELO DE BET

    Directory of Open Access Journals (Sweden)

    Ítalo Tuler Perrone

    2011-06-01

    Full Text Available Neste estudo foram produzidos em escala laboratorial pós de soro e de leite desnatado. A isoterma de sorção para cada produto desidratado foi obtida gravimetricamente. Os resultados das isotermas estão em concordância com o modelo de BET e as quantidades de água na monocamada, obtidos pelo modelo, são inferiores as quantidades de água dos pós. A produção em escala laboratorial de pós de leite e soro mostrou que o aumento da quantidade de soro em misturas de leite e soro produz problemas de adsorção de água durante a estocagem.

  8. LEITE EM PÓ DESNATADO, SORO EM PÓ E MISTURAS DE LEITE E SORO EM PÓ OBTIDOS EM MINISPRAY DRYER: ANÁLISE DE ISOTERMA E APLICAÇÃO DO MODELO DE BET

    OpenAIRE

    Ítalo Tuler Perrone; Antônio Fernandes de Carvalho; João Pablo Fortes Pereira; Paulo César Stringueta; Paulo Henrique Fonseca da Silva

    2011-01-01

    Neste estudo foram produzidos em escala laboratorial pós de soro e de leite desnatado. A isoterma de sorção para cada produto desidratado foi obtida gravimetricamente. Os resultados das isotermas estão em concordância com o modelo de BET e as quantidades de água na monocamada, obtidos pelo modelo, são inferiores as quantidades de água dos pós. A produção em escala laboratorial de pós de leite e soro mostrou que o aumento da quantidade de soro em misturas de leite e soro produz problemas de ad...

  9. Study on the Drying Technology and Drying Characteristics of Solar-dryer for High-quality Dried Apricot%优质杏干的太阳能干燥特点及其工艺研究

    Institute of Scientific and Technical Information of China (English)

    过利敏; 张谦; 赵晓梅; 邹淑萍; 刘路

    2008-01-01

    通过阐述2005~2008年在新疆南疆三地州采用标准化自制BG双波太阳能干燥(Solar-drying,简称SD)装置连续4年开展优质杏干的SD工艺研究,分析了影响SD的主要因素,并提出了相应的工艺措施以指导实际生产.研究表明,影响杏干SD特性的主要因素前期为排湿、中后期为温度,并且SD干燥温度应控制在40~60℃.还重点介绍了2008年6~8月在喀什地区泽普县进行赛买提杏的SD工艺研究.当装载量为60 kg时,赛买提杏干的实际SD干燥时间为10 d;杏干脱水率为1.804 kg/(m2·d),杏干优级品率达85%,分别是露天摊晒方式的1.9和2.8倍.可见,利用该装置在南疆地区进行SD杏干的生产是可行的,干燥效率高,产品品质好.

  10. Using Air Dryer to Improve Life of Booster Compressor's 2nd Stage Valves%利用空气干燥装置提高增压机二级气阀寿命

    Institute of Scientific and Technical Information of China (English)

    李群山; 李传华; 单正明; 邓发兵; 龚福辉

    2008-01-01

    介绍了压缩机工作原理及现场增压机二级气阀损坏情况,分析了损坏原因,提出了用冷却吸附干燥机分离气流中的水分来提高增压机二级气阀寿命的方法,实践证明该方法能够解决二级气阀寿命过短问题.

  11. STUDY ON DRYING UPGRADING AND FLOW CHARACTERISTIC OF LIGNITE IN VERTICAL PIPE DRYER%褐煤煤粉干燥立管提质干燥的流动特性研究

    Institute of Scientific and Technical Information of China (English)

    齐庆杰; 黄声和; 杨硕; 郭仁宁; 董子文

    2013-01-01

    Study on lignite coal powder in the drying process to mention the quality by which factors and how the factors are affected. Experimental data is used for the numerical simulation of the temperature, velocity and pressure fields by FLUENT6. 3. 26. It showed that lignite coal particles humidity changes when the brown one was upgrading and dry in low solid-gas ratio, and the results of upgrading and dry of the lignite is perfect; the drying effect of the pulverized coal had greatly improved when the inlet flue gas temperature was raised in the drying process, the flue gas velocity has little effect on the humidity of lignite powder particles.%通过实验研究褐煤煤粉在提质干燥过程受哪些因素的影响,利用FLUENT6.3.26对实验得到的数据进行温度、速度和压力场的数值模拟(气固两相流).对实验得到的数据和FLUENT6.3.26的数值模拟情况进行分析可知,褐煤煤粉在低气固比(体积比)进行提质干燥时,褐煤煤粉微粒的湿度有很大变化,提质干燥效果理想;在褐煤煤粉提质干燥过程中提高入口烟气温度,煤粉的干燥效果有很大提高;褐煤煤粉在提质干燥过程中烟气速度对褐煤粉颗粒湿度的影响很小.

  12. Research and Design of Steam-Knife Device in the Dryer%烘缸内汽刀式供汽装置的研究现状及其设计

    Institute of Scientific and Technical Information of China (English)

    李瑞虎; 胡玉莹; 薛文辉

    2010-01-01

    分析高速纸机烘缸在工作过程中,水蒸汽放热冷凝后形成水环的运动状态及其对烘缸热量传递过程的影响以及扰动对水环流动状态的影响;在此基础上,详细介绍了烘缸内汽刀式供汽装置的结构设计情况.通过该装置提供所谓的"汽刀"冲击水环,改变层液水环的运动状态,提高传热效率.

  13. Simulation Experimentation of the Steam Supply by Air-Knife in Dryer%用空气模拟蒸汽的烘缸汽刀式供给方式的实验

    Institute of Scientific and Technical Information of China (English)

    李瑞虎; 张勇; 马明; 乔丽洁

    2011-01-01

    高速烘缸内冷凝水形成的稳定水环层是热量传递的最主要阻力.分析烘缸内采用蒸汽汽刀式供给方式,对水环层进行剪切干扰,使原本稳定流动的水环层产生湍动的可行性初步设计蒸汽汽刀式供给系统结构.为方便观察,用有机玻璃制成的筒体代替烘缸,用空气气刀模拟蒸汽汽刀进行了实验研究.实验结果表明,采用蒸汽汽刀式供给方式,使水环层产生湍动,降低水环层热量传递的阻力,增加传热效率,能够达到节能效果.

  14. Control Difuso Adaptivo y su Aplicación a una Planta Piloto de Secado por Lecho Fluidizado Adaptive Fuzzy Control with an Application to a Fluidized Dryer Bed Pilot Plant

    Directory of Open Access Journals (Sweden)

    I. Velásquez

    2005-01-01

    Full Text Available En el presente trabajo, se muestra el diseño e implementación de un controlador difuso proporcional-prealimentado con Mecanismo de Adaptación (CDPP-MA para regular la temperatura en el interior del de un secador por lecho fluidizado. El algoritmo del controlador difuso se programa en el “Script” de Intouch, mientras que para diseñar y configurar los diferentes parámetros del controlador difuso se utiliza el software Matlab. Las pruebas se llevaron a cabo en una Planta Piloto e incluyeron cambios en la referencia del controlador y la aplicación de perturbaciones al sistema. El controlador presenta buen desempeño, tanto en el seguimiento de la referencia como en la atenuación de las perturbaciones. Los resultados indican que el controlador implementado es una alternativa factible de ser usado en el control de procesos no lineales o fuertemente perturbados.This work presents the design and implementation of a feed-forward proportional fuzzy controller with an adaptation mechanism (CDPP-MA. This controller was designed for temperature feedback control in a fluidized bed reactor. The fuzzy controller algorithm is programmed in Intouch’s Script language. Matlab software was used for the design and configuration of the fuzzy controller’s parameters. Experimental tests were carried out in a pilot plant and included changes of reference of the controller and applications of disturbances to the system. Excellent performance was obtained with the controller, both in following the reference and in attenuation of the disturbances. The results show the implemented controller to be a feasible alternative to for use in control of highly non-linear or strongly disturbed processes

  15. Analysis of Application of Steam- Driven Ejector Heat Pump in Dryer Section of Paper Machine%蒸汽喷射式热泵在纸机干燥部供热的应用分析

    Institute of Scientific and Technical Information of China (English)

    沈胜强; 张程; 李素芬

    2004-01-01

    将蒸汽喷射式热泵引入到传统的纸机干燥部多段式供热系统之中.建立了系统的计算模型,对一个典型的纸机三段供热干燥系统进行了计算.结果表明,引入喷射泵以后的系统较之传统系统,蒸汽耗量减少10%左右,段间流动压差增加,有利于烘缸内冷凝水的排出,干燥效果也更佳.

  16. 木薯酒糟在旋转闪蒸干燥器中的干燥特性%Basic Drying Characteristics of the Cassava Lees in Spin Flash Dryer

    Institute of Scientific and Technical Information of China (English)

    刘琨

    2003-01-01

    对木薯酒糟在旋转闪蒸干燥器中的基本干燥特性进行了实验研究.结果表明该物料干燥后的含水质量分数与干燥介质温度呈直线关系,与干燥时间呈指数曲线关系,这一特性与其薄层干燥过程相似.某些研究结果还为该物料的工业化干燥提供了依据.

  17. 空气制冷机干燥器充放气时间的确定与供气平稳性设计%CHARGE/DEFLATION TIME OF DRYERS AND STABILITY DESIGN FOR AIR REFRIGERATING MACHINE

    Institute of Scientific and Technical Information of China (English)

    赵雁纪; 张利珍; 周金辉

    2008-01-01

    对于空气制冷系统来讲,供气的平稳性十分重要,它涉及到核心设备--涡轮制冷机的运行安全.而在各种供气平稳性设计中,空气干燥器的储气罐充放气时间是一个十分重要的参数,它影响到切换动作程序.着重论述储气罐充放气时间的确定和该参数对供气平稳性设计的影响.

  18. 重新探讨干网张力--试验证明烘干能力同干网张力有关%Dryer fabric tensions revisited Tests confirm that drying capacity is related to fabric tension

    Institute of Scientific and Technical Information of China (English)

    I.Lang

    2004-01-01

    干网张力作为对张机烘干部烘干能力具有重要作用的因素而成为经常争论的论题,而行业杂志和标准关于推荐使用的张力方面的信息却是有限的.本文论述在模拟工业条件的实验室烘干设备上所作的试验.这些结果表明用比造纸业中常用的干网高的张力进行操作就能改善烘干能力.

  19. Estimativa das propriedades térmicas efetivas de grãos em um secador de leito fixo Estimation of effective grain thermal properties in a fixed bed dryer

    Directory of Open Access Journals (Sweden)

    L. V. Fregolente

    2004-06-01

    Full Text Available A secagem de grãos em leito fixo é um processo complexo, ocorrendo simultaneamente a transferência de calor e de massa, dificultando a estimativa dos parâmetros térmicos efetivos, pois estes podem sofrer variações significativas no decorrer da secagem em função de alterações no teor de umidade. Neste trabalho, este problema foi contornado estimando-se os parâmetros térmicos efetivos no final da secagem, quando o teor de umidade dos grãos que compõem o leito alcança valores de equilíbrio, deixando de existir a transferência de massa, persistindo apenas a transferência de calor em regime permanente. Nestas condições, o leito possui um teor de umidade constante e a estimativa dos parâmetros térmicos efetivos pode ser efetuada a partir do ajuste de um modelo pseudo-homogêneo bidimensional estático à várias medidas de temperatura no leito de grãos no final da secagem. Os resultados indicam que a estratégia utilizada para estimativa da condutividade térmica efetiva radial e do coeficiente efetivo de transferência de calor parede-leito foi adequada. Além do que, constatou-se que dentre os grãos estudados - soja, feijão, milho e trigo - a soja apresenta os menores valores de condutividade efetiva radial, enquanto o trigo apresenta o maior valor do coeficiente de transferência de calor parede-leito.Fixed bed grain drying is a complex process, where mass and heat transfer occur simultaneously, complicating the estimation of the effective thermal parameters, because they can go through significant variations along the drying process, due to moisture content variations. In this work, this problem was avoided by estimating the effective thermal parameters at the end of the drying process, when the grain moisture content reaches equilibrium, and mass transfer stops, persisting only the steady state heat transfer. In these conditions, the bed has a constant moisture content and the estimation of the effective thermal parameters can be obtained from the adjustment of a steadystate two-dimensional pseudohomogeneous model to several fixed bed temperature measurements at the end of the drying process. The results show that the strategy used to evaluate the effective thermal conductivity and the effective wall heat transfer coefficient was appropriate. In addition, among the grains analysed - soy, bean, corn and wheat-, soy presents the smallest values of effective radial conductivity, while wheat presents the greatest effective wall heat transfer value.

  20. DEWATERING TREATMENT SCALE-UP TESTING RESULTS OF HANFORD TANK WASTES

    Energy Technology Data Exchange (ETDEWEB)

    TEDESCHI AR

    2008-01-23

    This report documents CH2M HILL Hanford Group Inc. (CH2M HILL) 2007 dryer testing results in Richland, WA at the AMEC Nuclear Ltd., GeoMelt Division (AMEC) Horn Rapids Test Site. It provides a discussion of scope and results to qualify the dryer system as a viable unit-operation in the continuing evaluation of the bulk vitrification process. A 10,000 liter (L) dryer/mixer was tested for supplemental treatment of Hanford tank low-activity wastes, drying and mixing a simulated non-radioactive salt solution with glass forming minerals. Testing validated the full scale equipment for producing dried product similar to smaller scale tests, and qualified the dryer system for a subsequent integrated dryer/vitrification test using the same simulant and glass formers. The dryer system is planned for installation at the Hanford tank farms to dry/mix radioactive waste for final treatment evaluation of the supplemental bulk vitrification process.

  1. Solar Kilns: Feasibility of Utilizing Solar Energy for Drying Lumber in Developing Countries,

    Science.gov (United States)

    1977-01-01

    evaluation of shelf type solar driers. Sol. Energy 16(2):81-88. N Selcuk, M. K. 1967. Final report of the solar fruit dryer . Cooperation Medi- terraneenne...at one dryer orientation (long axis north-south) from 30 percent to 10 percent moisture content. 49 Table 15.--Greenhouse-type solar kiln capacity...out the success or failure of some design features, construction details, and applications of solar dryers . Feasibility _; estimates concluded that

  2. Development of Solar Biomass Drying System

    OpenAIRE

    Atnaw Samson Mekbib; Bin Che Ku Yahya Che Ku Mohammad Faizal; Jama Oumer Abduaziz

    2017-01-01

    The purpose of this paper focuses on the experimental pre-treatment of biomass in agricultural site using solar energy as power source and contribution of common use and efficiency solar dryer system for consumer. The main purpose of this design for solar cabinet dryer is to dry biomass via direct and indirect heating. Direct heating is the simplest method to dry biomass by exposing the biomass under direct sunlight. The solar cabinet dryer traps solar heat to increase the temperature of the ...

  3. Energieffektiv torkning av kläder : en studie av torktumlare med varm- respektive kallvattenanslutning

    OpenAIRE

    Ayedi, Omar

    2011-01-01

    Tumble dryers and drying cabinets have to a large extent replaced the traditional way of drying clothes outdoors. They are faster, more convenient, require less space and can be operated regardless of weather conditions. This replacement has significantly increased residential energy consumption, due to the fact that tumbles dryers consume large amounts of electrical energy. In the USA 9 % of the households electric energy is consumed when drying clothes. Over 4 million tumble dryers are sold...

  4. Energy Efficient Textile Drying

    OpenAIRE

    Brunzell, Lena

    2006-01-01

    Traditionally, textiles were dried outdoors with the wind and the sun enhancing the drying process. Tumble dryers offer a fast and convenient way of drying textiles independent of weather conditions. Tumble dryers, however, consume large amounts of electrical energy. Over 4 million tumble dryers are sold each year in Europe and a considerable amount of energy is used for drying of clothes. Increasing energy costs and the awareness about environmental problems related to a large energy use has...

  5. Installation Restoration General Environmental Technology Development. Task 8. Bench-Scale Investigation of Low Temperature Thermal Removal of TCE (Trichloroethylene) from Soil.

    Science.gov (United States)

    1985-03-01

    Most of the applicable indus- trial dryer designs subject the treated material to either extensive tumbling or they force purge gas through the...volatilization of TCE from soils. A brief review of chemical and metallurgical processing equipment resulted in industrial dryers being the .* prime...candidate for full-scale operations. A brief survey of dryer manufacturers and vendors was completed. It was evident from discussions with vendors that

  6. The Environmental Assessment and Management (TEAM) Guide; Rhode Island Supplement, Revised March 1998

    Science.gov (United States)

    1998-03-01

    drying by tumbling in an airstream. The facility includes, but is not limited to, any washer, dryer , filter, and purification system; waste disposal...solvent added to any degreaser or dryer at a facility during the previous calendar year (CRIR 12 031 022(22.1.8)). Anthracite - a hard, black lustrous...Azeotropic Device - an air pollution control device wherein the dryer exhaust from a dry cleaning machine is routed to a tank where the perchloroethylene

  7. Effect of processing techniques on color and active components amount of sweet potato (Ipomoea Batatas l) flakes

    Science.gov (United States)

    Rahmawati, Y.; Mahmudatussa'adah, A.; Yogha, S.

    2016-04-01

    Sweet potato processing is limited, such as flour, snacks, cystic, or chips. Flakes as pre-cooked meals are made through the stages of making pasta and drying. The purpose of this study was to optimize the production of sweet potato flakes at the stage of making pasta and drying. Making the pasta is done through techniques steamed or baked. Pasta drying using tools a drum dryer or cabinet dryer. As an indicator of optimization is the total of monomeric anthocyanins, β-carotene and color the resulting flakes. The results showed that the amount of anthocyanin monomeric flakes by using steam, and drum dryer (3.83 ± 0.03 mg CYE/g db), flakes by the technique of steam, and cabinet dryer (3.03 ± 0.02 mg CYE/g db), flakes with techniques bake, drum dryer (2.49 ± 0.05 CYE mg/g db), flakes with bake technique, cabinet dryer (1.98 ± 0.03 mg CYE/g db). The Color of purple sweet potato flakes produced through steamed techniques bright purple, while the color purple sweet potato flakes produced through techniques roast give a brownish purple color. The amount of β-carotene yellow flakes sweet potato with stages of cooking steamed, drum dryer (152±0.5 mg/Kg db), grilled drum dryer (136±0.4 mg/Kg db), flakes of yellow sweet potato with stages of roasted and cabinet dryer (140±0.8 mg/Kg db), and grilled stage with cabinet dryer (122±0.3 mg/Kg db). In conclusion sweet potato flakes production techniques through the stages of steam process, and used drum dryers have a number of anthocyanins or β-carotene bigger and brighter colors than the baked flakes techniques and used cabinet dryer.

  8. MESIN PENGERING KAYU SEDERHANA UNTUK HOME INDUSTRI

    Directory of Open Access Journals (Sweden)

    Murni Murni

    2012-02-01

    Full Text Available Dryer machine of wood is made to fulfill need of wood in order to produce raw of drying wood is notdepended weather. Making of dryer of wood usually requiree investment cost more expensive . it is heavyfor home industry .Inovation of simple dryer machine is done with flowing steam naturally and base onanalyzing it shows that drying can achieve moistur content 12 persen

  9. Geometry for web microwave heating or drying to a desired profile in a waveguide

    Science.gov (United States)

    Habeger, Jr., Charles C.; Patterson, Timothy F.; Ahrens, Frederick W.

    2005-11-15

    A microwave heater and/or dryer has a nonlinear or curvilinear relative slot profile geometry. In one embodiment, the microwave dryer has at least one adjustable field modifier making it possible to change the geometry of the heater or dryer when drying different webs. In another embodiment, the microwave dryer provides more uniform drying of a web when the field modifier is adjusted in response to a sensed condition of the web. Finally, a method of microwave heating and/or drying a web achieves a uniform heating and/or drying profile.

  10. Antimicrobially Treated Projects for Military Use

    Science.gov (United States)

    2007-11-30

    drained and the socks removed. The socks were dried in a gas- fired tumble dryer at a temperature of 300°F for 45 minutes, removed from the dryer and...The pick-up rate of the fabric was 50%. The fabric was dried and cured in a four zone dryer with temperatures of 410F, 420F, 430F and 430F...conventional dryer at 245° F. 9 For the initial laboratory screening triclosan was applied as MLF 9200-200 at 2%, the quat silane as MLF SiS 7200

  11. Prediction of lycopene degradation during dehydration of watermelon pomace (cv Sugar Baby)

    OpenAIRE

    Davinder Pal Singh Oberoi; Dalbir Singh Sogi

    2017-01-01

    Lycopene retention in watermelon pomace during drying was investigated in fluidized-bed and cabinet dryer at 50–70 °C using 2–6 kg/m2 tray loads. Page’s model described the drying behaviour of watermelon pomace better than other models. Lycopene content of watermelon pomace dried in fluidized-bed dryer was 5.67–9.86 mg/100 g (db) whereas in cabinet dryer 4.82–8.12 mg/100 g (db) under experimental conditions. Lycopene retention was lower in cabinet dryer due to longer drying time. Degradation ...

  12. 40 CFR Table 1b to Subpart Dddd of... - Add-on Control Systems Compliance Options

    Science.gov (United States)

    2010-07-01

    ... CATEGORIES National Emission Standards for Hazardous Air Pollutants: Plywood and Composite Wood Products Pt... new affected sources only); reconstituted wood product presses; softwood veneer dryer heated...

  13. 10 CFR 430.2 - Definitions.

    Science.gov (United States)

    2010-01-01

    ... energy consumption. (4) With respect to clothes dryers, which have the same primary energy source, which... heated air is circulated by means of a fan or blower. Electric clothes dryer means a cabinet-like appliance designed to dry fabrics in a tumble-type drum with forced air circulation. The heat source...

  14. Low-Temperature Effects on Systems for Composting of Explosives-Contaminated Soils. Part 1. Literature Review

    Science.gov (United States)

    1989-12-01

    and Inclined Flow Reactor cepts were developed for composting municipal Systems and industrial solid wastes. These types of solid 1. Tumbling solids...drying windrow or heat dryer rates; final drying may be required may be required in windrow or heat dryer usually required Sensitivity to cold

  15. JPRS Report Environmental Issues

    Science.gov (United States)

    2007-11-02

    spray booth with cross-current, Venturi gas scouring, and a dryer for catalytic immersion painting (KTL). The dryer units, which are completely...failure to achieve mass production, which could then let prices tumble , as the main problem. "The demand is there, especially in developing countries

  16. Textile Fingerprinting for Dismount Analysis in the Visible, Near, and Shortwave Infrared Domain

    Science.gov (United States)

    2014-03-01

    original laundry detergent. A Kenmore® standard dryer is used on its medium heat, 40 minute tumble dry cycle. The uniqueness data set is comprised of...techniques. Washing machines and dryers alter the spectral signatures of textiles, making it possible to uniquely identify a fabric of interest (FOI

  17. Suitability of a Freeze Dried Product as a Vehicle for Vitamin Fortification of Military Ration Packs: A Preliminary Study

    Science.gov (United States)

    2011-01-01

    loaded into the freeze dryer and dried over an eight hour period. The freeze dried product was removed from the freeze dryer and transferred to...plastic bags (one bag per treatment). While in the bag the pieces of freeze dried product were manually broken and tumbled to mix. The bags were placed

  18. 40 CFR 63.321 - Definitions.

    Science.gov (United States)

    2010-07-01

    ... to remove perchloroethylene from articles by tumbling them in a heated air stream (see dryer... system and its ancillary equipment. Dryer means a machine used to remove perchloroethylene from articles by tumbling them in a heated air stream (see reclaimer). Dry-to-dry machine means a one-machine...

  19. Development of drying equipment for heat sensitive material : final report

    Energy Technology Data Exchange (ETDEWEB)

    Schoenau, G.J.; Sokhansanj, S. [Saskatchewan Univ., Saskatoon, SK (Canada)

    2003-07-01

    This paper described a project in which two types of prototype heat pump dryer systems were designed, constructed and field tested in 2000 to 2002. Performance testing was accomplished through a computer based simulation model for predicting dryer performance. The paper describes the procedures followed and the results obtained. The dryer is used for high value specialty crops such as ginseng, herbs and echinacea which require low temperature drying. The heat pump dryer operates under a closed loop and can dry these crops at low temperatures, independent of ambient conditions. The first prototype was a small fixed bed cabinet dryer suitable for small growers. The other was a full scale prototype moving bed cross flow system suitable for large scale commercial drying of sensitive agricultural crops. The heat pump system is faster and more energy efficient than conventional dryers. The average moisture content of ginseng roots was reduced by 10 per cent in 5 days using 190 kWh of energy. The heat pump dryer is 22 per cent more efficient than a conventional dryer due to its recirculating system. Drying time is reduced by 65 per cent. A computerized simulation validated experimental results. 30 refs., 10 tabs., 29 figs.

  20. 40 CFR 63.9942 - What definitions apply to this subpart?

    Science.gov (United States)

    2010-07-01

    ... system that melts and chlorinates dehydrated brine to produce high purity molten magnesium chloride feed for electrolysis. Primary magnesium refining means the production of magnesium metal and magnesium.... Spray dryer means dryers that evaporate brine to form magnesium powder by contact with high...