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1 - NASA Technical Reports Server  

shown are gas turbine inlet temperature and hybridsolar energy percent. ... . arrangement.of solar and fossil fuel input to the gas-turbine cycle exhaust ...... Burner. - --Fossil fuel. HX. [,---. Solar. Exhaust. I gas path. Figure 14, Concept for ...

2

Exhaust purification with on-board ammonia production  

A system of ammonia production for a selective catalytic reduction system is provided. The system includes producing an exhaust gas stream within a cylinder group, wherein the first exhaust gas stream includes NOx. The exhaust gas stream may be supplied to an exhaust passage and cooled to a predetermined temperature range, and at least a portion of the NOx within the exhaust gas stream may be converted into ammonia.

3

Exhaust purification with on-board ammonia production  

A method of ammonia production for a selective catalytic reduction system is provided. The method includes producing an exhaust gas stream within a cylinder group, wherein the first exhaust gas stream includes NOx. The exhaust gas stream may be supplied to an exhaust passage and cooled to a predetermined temperature range, and at least a portion of the NOx within the exhaust gas stream my be converted into ammonia.

4

Chimney and exhaust gas systems for low-temperature and high-efficiency boilers. Schornstein- und Abgassysteme fuer Niedertemperatur- und Brennwertkessel  

When exchanging old heating systems against new, it is essential to find out whether the old chimney is still suitable. The following changes to the heating system can cause problems in this context: lower performance and consequent lower exhaust gas mass flow; lower exhaust gas losses and consequent lower exhaust gas temperatures; longer burner operating time impeding the evaporation of moisture in the chimney. The article presents a comparison of different means of exhaust gas conducting systems. (BWI)

5

Improved repowering techniques for power plants  

Repowering of existing coal-fired power plants is often accomplished by adding gas turbines. In this paper we assume that the gas turbine exhaust is used for feed water preheating.Typical gas turbine exhaust temperatures are in the range 450-600C whereas typical boiler inlet temperatures are 250-300C. The big difference in temperature between exhaust and water prevents an efficient exchange of heat. One way to lower the exhaust temperature is to expand the gas to sub atmospheric pressure. The result is a 50% increase in possible installed gas turbine power.

6

Combined cycle electric power plant with coordinated plural feedback turbine control  

A combined cycle electric power plant includes gas and steam turbines and a steam generator for recovering the heat in the exhaust gases exited from the gas turbine and for using the recovered heat to produce and supply steam to the steam turbine. The steam generator includes a superheater tube through which a fluid, E.G. Water, is directed to be additionally heated into superheated steam by the exhaust gas turbine gases. An afterburner further heats the exhaust gas turbine gases passed to the superheater tube. The temperature of the gas turbine exhaust gases is sensed for varying the fuel flow to the afterburner by a fuel valve, whereby the temperatures of the gas turbine exhaust gases and therefore of the superheated steam, are controlled. A plant load demand error signal is utilized for correcting a coordinated gas turbine load reference and for trimming a feedforward afterburner control signal derived from the sensed gas turbine exhaust temperatures.

7

Combined cycle electric power plant with feedforward afterburner temperature setpoint control  

A combined cycle electric power plant includes gas and steam turbines and a steam generator for recovering the heat in the exhaust gases exited from the gas turbine and for using the recovered heat to produce and supply steam to the steam turbine. The steam generator includes a superheater tube through which a fluid, e.g. water, is directed to be additionally heated into superheated steam by the exhaust gas turbine gases. An afterburner further heats the exhaust gas turbine gases passed to the superheater tube. The temperature of the gas turbine exhaust gases is sensed for varying the fuel flow to the afterburner by a fuel valve, whereby the temperatures of the gas turbine exhaust gases and therefore of the superheated steam, are controlled. The afterburner fuel flow is controlled through a feedforward setpoint signal derived as a predetermined function of sensed gas turbine exhaust temperature.

8

76 FR 64844 - Airworthiness Directives; General Electric Company Turbofan Engines  

...rotor stage 3 disks installed. The...high pressure turbine (HPT) and LPT...rotor stage 3 disks affected by those...repetitive exhaust gas temperature...i) An exhaust gas temperature Within...rotor stage 3 disk from service...and ensure the turbine mid-frame...

9

Exhaust gas purification system for lean burn engine  

An exhaust gas purification system for a lean burn engine includes a thermal mass unit and a NO.sub.x conversion catalyst unit downstream of the thermal mass unit. The NO.sub.x conversion catalyst unit includes at least one catalyst section. Each catalyst section includes a catalytic layer for converting NO.sub.x coupled to a heat exchanger. The heat exchanger portion of the catalyst section acts to maintain the catalytic layer substantially at a desired temperature and cools the exhaust gas flowing from the catalytic layer into the next catalytic section in the series. In a further aspect of the invention, the exhaust gas purification system includes a dual length exhaust pipe upstream of the NO.sub.x conversion catalyst unit. The dual length exhaust pipe includes a second heat exchanger which functions to maintain the temperature of the exhaust gas flowing into the thermal mass downstream near a desired average temperature.

10

Development of exhaust reburning technology for co-generation; Cogeneration yo haiki sainensho gijutsu no kaihatsu  

In this report, the energy-saving and economic features of the exhaust reburning system are described; the structures, combustion performance, and NOx performance of two types of burners are shown; and then the system design is outlined. In addition, a reference is made to an exhaust recombustion burner which adapts to the electrothermally variable chain cycle gas turbine and to the lean gas engine. In a co-generation system, the heat contained in the gas turbine exhaust is recovered in the waste heat boiler in the form of steam. It is the added combustion system and the exhaust recombustion system that increase the quantity of heat contained in the gas turbine exhaust for an increase in the amount of steam to be recovered. The gas turbine exhaust contains oxygen with its concentration level 13-15wet% and its temperature 500-600 degrees C, and the exhaust recombustion system utilizes only this exhaust as the combustion air. The exhaust recombustion burner is provided with two stages of swirlers installed near the gas nozzle for the augmentation of flame holding capability, and is assured of a stable combustion in the turbine exhaust until the post-combustion residual oxygen concentration level is as low as 3wet%. (NEDO)

11

Frozen Chemistry Effects on Nozzle Performance Simulations  

Simulations of exhaust nozzle flows are typically conducted assuming the gas is calorically perfect, and typically modeled as air. However the gas inside a real nozzle is generally composed of combustion products whose thermodynamic properties may differ. In this study, the effect of gas model assumption on exhaust nozzle simulations is examined. The three methods considered model the nozzle exhaust gas as calorically perfect air, a calorically perfect exhaust gas mixture, and a frozen exhaust gas mixture. In the latter case the individual non-reacting species are tracked and modeled as a gas which is only thermally perfect. Performance parameters such as mass flow rate, gross thrust, and thrust coefficient are compared as are mean flow and turbulence profiles in the jet plume region. Nozzles which operate at low temperatures or have low subsonic exit Mach numbers experience relatively minor temperature variations inside the nozzle, and may be modeled as a calorically perfect gas. In those which operate at the opposite extreme conditions, variations in the thermodynamic properties can lead to different expansion behavior within the nozzle. Modeling these cases as a perfect exhaust gas flow rather than air captures much of the flow features of the frozen chemistry simulations. Use of the exhaust gas reduces the nozzle mass flow rate, but has little effect on the gross thrust. When reporting nozzle thrust coefficient results, however, it is important to use the appropriate gas model assumptions to compute the ideal exit velocity. Otherwise the values obtained may be an overly optimistic estimate of nozzle performance.

12

Exhaust duct for internal combustion engines  

The aim of this invention is to provide an exhaust system for use with an internal combustion engine of the divided cylinder type, in order to make it possible for the exhaust gases from the working cylinders to flow to the catalyst, without it passing through the cylinders not in use, in order to keep the temperature of the waste gases flowing through the catalyst high, and thus to obtain an optimum catalyst performance. The invention designed for internal combustion engines with several cylinders divided into groups consists of a device, which responds to the engine operation conditions at low load in order to interrupt the flow of fuel and fresh air to the second group of cylinders and to an exhaust duct, with two individual ducts allocated to the groups of cylinders and an exhaust gas return duct with exhaust gas return valve. This valve opens the exhaust gas return duct depending on the operating conditions at low engine load.

13

Carbon capture with low energy penalty: Supplementary fired natural gas combined cycles  

Enhancing CO"2 concentration in exhaust gas has been considered as a potentially effective method to reduce the penalty of electrical efficiency caused by CO"2 chemical absorption in post-combustion carbon capture systems. Supplementary firing is an option that inherently has an increased CO"2 concentration in the exhaust gas, albeit a relatively low electrical efficiency due to its increased mass flow of exhaust gas to treat and large temperature difference in heat recovery steam generator. This paper focuses on the methods that can improve the electrical efficiency of the supplementary fired combined cycles (SFCs) integrated with MEA-based CO"2 capture. Three modifications have been evaluated: (I) integration of exhaust gas reheating, (II) integration of exhaust gas recirculation, and (I...

14

Summary and analysis of performance and stability characteristics of ...  

High Pressure Compressor, Burner and Turbines. 10. 3. .... JT8D-9/D-109 Maximum Exhaust Gas Temperatures (OF) ..... The burner section consists of nine separate ...... LSTIMATtD THkUSI AND FULL FLOW CORKECTIUN FACTORS. ' LPG ...

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76 FR 6323 - Airworthiness Directives; General Electric Company CF6-45 and CF6-50 Series Turbofan Engines  

...certain low-pressure turbine (LPT) rotor stage 3 disks installed. That AD currently...of the high-pressure turbine (HPT) rotor stage 1...the LPT rotor stage 3 disk under certain conditions...requires repetitive exhaust gas temperature (EGT)...

16

Gas sensors based on tin dioxide for exhaust gas application, modeling of response for pure gases and for mixtures  

This paper concerns tin dioxide gas sensors for automotive exhaust gas application. It consists in elaborating robust sensors on alumina substrate by screen-printing technology. Sensors have been tested on a synthetic gas bench which is able to generate high gas velocity and gases at high temperatur...

17

Heat exchanger for phosphoric acid fuel cell; Rinsan gata nenryo denchiyo netsukokanki  

The phosphoric acid mixed into the exhaust air of the fuel cell reacts chemically with the structural materials such as stainless steel of pipes in which fuel cell exhaust air flows and the air preheater, and produces phosphoric acid compound. This compound accumulates on the surface, grows with the passage of time to block up the exhaust air passage, and causes production of pin holes at welded area by corrosion. This invention is concerned with a phosphoric acid fuel cell, wherein an inlet for exhaust oxidizer gas to flow into the heat exchanger is provided at the lower part of the heat exchanger, and an outlet is provided at the upper part of the heat exchanger for flowing exhaust oxidizer gas from the heat exchanger. As a result, even when vapor in the exhaust oxide gas is condensed to become water, the water drops to contact with high temperature exhaust oxidizer gas at the lower area and evaporates to avoid production of strong acidic drain caused by phosphoric acid because high temperature exhaust oxidizer gas containing phosphoric acid forms upward flow ascending from the lower part to the upper part of the air preheater. 5 figs.

18

Apparatus and methods of reheating gas turbine cooling steam and high pressure steam turbine exhaust in a combined cycle power generating system  

In a combined cycle system having a multi-pressure heat recovery steam generator, a gas turbine and steam turbine, steam for cooling gas turbine components is supplied from the intermediate pressure section of the heat recovery steam generator supplemented by a portion of the steam exhausting from the HP section of the steam turbine, steam from the gas turbine cooling cycle and the exhaust from the HP section of the steam turbine are combined for flow through a reheat section of the HRSG. The reheated steam is supplied to the IP section inlet of the steam turbine. Thus, where gas turbine cooling steam temperature is lower than optimum, a net improvement in performance is achieved by flowing the cooling steam exhausting from the gas turbine and the exhaust steam from the high pressure section of the steam turbine in series through the reheater of the HRSG for applying steam at optimum temperature to the IP section of the steam turbine.

19

Municipal solid waste treatment and ash-melting technology; Toshi gomi shori to hai yoyu gijutsu  

Melting techniques of ash generated in municipal solid waste incinerators can be divided into a fuel process and an electric process. The fuel process was developed for applying to waste treatment such as sludge. The fuel process discharges a large amount of exhaust gas. Then, downsizing of exhaust gas treatment equipment can not be expected. However, the residence time in the high temperature region can be maintained due to a large quantity of heat from the exhaust gas, which results in the enhanced decomposition of dioxins. On the other hand, for the electric process, treatment of exhaust gas is easy due to a smaller amount of exhaust gas. Then, the initial cost of exhaust gas treatment equipment can be suppressed. However, for both the processes, it is not avoidable to regenerate the dioxins during cooling process of exhaust gas. Thorough control of temperature and protection of adhesion and deposition of dusts are essential for reducing the dioxins. All of items from the elution tests of slags satisfy the landfill standard. For recycling and reusing the molten slag, it is necessary to establish the social and technical rule as well as to arrange the treatment manual and standard and to construct the MSDS (material safety data sheet). 10 refs., 5 figs., 2 tabs.

20

Using Waste Heat for External Processes (English/Chinese) (Fact Sheet)  

Chinese translation of the Using Waste Heat for External Processes fact sheet. Provides suggestions on how to use waste heat in industrial applications. The temperature of exhaust gases from fuel-fired industrial processes depends mainly on the process temperature and the waste heat recovery method. Figure 1 shows the heat lost in exhaust gases at various exhaust gas temperatures and percentages of excess air. Energy from gases exhausted from higher temperature processes (primary processes) can be recovered and used for lower temperature processes (secondary processes). One example is to generate steam using waste heat boilers for the fluid heaters used in petroleum crude processing. In addition, many companies install heat exchangers on the exhaust stacks of furnaces and ovens to produce hot water or to generate hot air for space heating.

 
 
 
 
21

Mutagenic activities of exhaust gas and ash from sludge incineration plants  

We have found that the exhaust gas from many incineration plants of municipal solid wastes (MSW) show significant mutagenic activities. The mutagenic activities of exhaust gas from incineration plants of the other wastes have not been studied in detail. Here, we analyzed the mutagenic activities and compounds in exhaust gas and ash from seven sludge incineration plants. Some samples of the exhaust gas from the sludge incineration plants showed high mutagenic activities; although, none of the ash residues showed mutagenic activities. There was no relationship between the mutagenic activities and furnace types, the plant size or the apparent residence time of the gas in the furnace. The mutagenic activities of the exhaust gas were produced during incomplete combustion at lower temperatures. Direct mutagenic activities without S9 mix were higher than indirect mutagenic activities with S9 mix which was made from rat liver homogenate and was used to test mutagenic activity after metabolism. These results are different to those of MSW incineration plants. We analyzed the mutagenic compounds in the exhaust gas by GC/MS after fractionation by HPLC, but they could not be identified. We found that the mutagenic compounds in the exhaust gas were different from the compounds that were produced from the MSW incineration plants. We believed that these mutagenic compounds might be non-volatile and more polar than the heterocyclic amines, Trp-P-2, Trp-P-1 and Glu-P-1, which are typical mutagenic compounds in sewage and sludge

22

Face crack reduction strategy for particulate filters  

A system comprises a particulate matter (PM) filter that comprises an upstream end for receiving exhaust gas, a downstream end and at least one portion. A control module initiates combustion of PM in the PM filter using a heater and selectively adjusts oxygen levels of the exhaust gas to adjust a temperature of combustion adjacent to the at least one portion of the PM filter. A method comprises providing a particulate matter (PM) filter that comprises an upstream end for receiving exhaust gas, a downstream end and at least one portion; initiating combustion of PM in the PM filter using a heater; selectively adjusting oxygen levels of the exhaust gas to adjust a temperature of combustion adjacent to the at least one portion of the PM filter.

23

Conceptual design and thermal analysis of the exhaust duct for a fissioning uranium plasma test reactor  

The conceptual design and analysis of a film cooled exhaust duct for a gas core rocket test cavity is described. The cavity exhaust has a temperature of 4000 K and 200 atmosphere of pressure. The film cooled duct design uses seeded hydrogen coolant flow to reduce the duct outlet temperature to 850 K, and the maximum duct wall temperature to below 700 K. With this design less than 1 percent of the uranium fuel flow rate in the exhaust plates out on the duct walls.

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NOVEL GAS SENSORS FOR HIGH-TEMPERATURE FOSSIL FUEL APPLICATIONS  

SRI is developing ceramic-based microsensors for detection of exhaust gases such as NO, NO{sub 2}, and CO in advanced combustion and gasification systems. The sensors detect the electrochemical activity of the exhaust gas species on catalytic electrodes and are designed to operate at high temperatures, elevated pressures, and corrosive environments typical of large power generation exhausts. Under this research project we are developing sensors for multiple gas detection in a single package along with data acquisition and control software and hardware. The sensor package can be easily integrated into online monitoring systems for active emission control. This report details the research activities performed from October 2003 to April 2004.

25

Effects of various mixer types on the spatial distribution of a De-NOx reductant  

De-NOx catalytic systems generally perform better in rich or stoichiometric engine operating conditions due to high hydrocarbon (HC) concentrations in the exhaust gas. However, the hydrocarbon concentration in a diesel engine is typically low, so post or supplemental fuel injections into the exhaust gas have been employed in order to increase the HC concentration. A hydrocarbon-type lean NOx trap (HC-LNT) catalyst system that is a De-NOx system based on NOx-absorbing catalyst has also been developed to optimize control of the external HC injection into the diesel exhaust pipe. The system has a secondary injector that injects diesel fuel (HC) into an exhaust manifold. The typically high temperature (250-350degreeC) in the exhaust manifold affects the spray behavior of the secondary injector...

26

Study on reducing effects of NOx exhausted from combustion systems using azo compounds; Azo kagobutsu no nensho haikikei ni okeru dasshu koka ni kansuru kenkyu  

Reducing effects of nitric oxides (NOx) exhausted from combustion systems have been studied by adding various azo compounds such as azodicarbonamide and 2,2-azobis-isobutyronitrile to simulated exhaust gases in an electrically heated quartz flow reactor under different conditions of temperature, gas composition and residence period. As a result, it is shown that azo compounds can reduce nearly 100% of NOx in the simulated model exhaust gases at 750{degree}C. We suggest that at elevated temperature azo compounds should decompose to produce NH2, CN and alkyl radicals having NOx reducing effects. 8 refs., 7 figs., 2 tabs.

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75 FR 7407 - Airworthiness Directives; Piper Aircraft, Inc. Models PA-32R-301T and PA-46-350P Airplanes  

...spot-welded V-band exhaust couplings that...certain Piper Aircraft, Inc. Models...The V-band exhaust coupling attaches...to hot exhaust gases. Several failures...to Commander Aircraft Company Model...design V-band exhaust coupling has...high temperature gases inside the...

28

Use of gas-turbine exhaust for the direct drying of food products. Final report  

This report describes an investigation of the use of gas-turbine exhaust as a substitute for conventional burners in the direct drying of food products. Four different equipment configurations were examined, including: diluting exhaust gases with air to achieve suitable temperatures; directing exhaust through a heat exchanger; moving the exhaust through a heat recovery boiler and then a drying system; and utilizing a conventional gas turbine cogeneration system. The study determined that diluting exhaust with air and the heat recovery boiler/drying system were economically attractive. The concern with direct drying using gas turbine exhaust is that the presence of elevated nitrogen oxides in the gas may be found in the food products or cause the formation of nitrosamines (a potent carcinogen) in these products. The study concluded that for direct drying using turbine exhaust to be commercialized for food products, either methods for reducing nitrogren oxides levels must be developed for the turbines of pilot tests combined with food-product analysis have to be performed.

29

Engine Cylinder Temperature Control  

A method and apparatus for controlling a temperature in a combustion cylinder in an internal combustion engine. The cylinder is fluidly connected to an intake manifold and an exhaust manifold. The method and apparatus includes increasing a back pressure associated with the exhaust manifold to a level sufficient to maintain a desired quantity of residual exhaust gas in the cylinder, and varying operation of an intake valve located between the intake manifold and the cylinder to an open duration sufficient to maintain a desired quantity of fresh air from the intake manifold to the cylinder, wherein controlling the quantities of residual exhaust gas and fresh air are performed to maintain the temperature in the cylinder at a desired level.

30

Low exhaust temperature electrically heated particulate matter filter system  

A system includes a particulate matter (PM) filter, a sensor, a heating element, and a control module. The PM filter includes with an upstream end that receives exhaust gas, a downstream end and multiple zones. The sensor detects a temperature of the exhaust gas. The control module controls current to the heating element to convection heat one of the zones and initiate a regeneration process. The control module selectively increases current to the heating element relative to a reference regeneration current level when the temperature is less than a predetermined temperature.

31

An RC-1 Organic Rankine Bottoming Cycle for - NASA Technical ...  

product, or process disclosed, or represents that its use would not infringe privately .... An increase in exhaust gas temperature is characteristic of the adiabatic engine. .... A Shimadzu Model 6AM gas chromatograph with an integral ther- .... indicate two (2) peaks with molecular weights of 330 and 348. ...... on an ideal basis.

32

Transient Response Simulation of Downstream Thermofluid Field in a Gas Circuit Breaker during Current Interruption  

A transient response of SF6 thermofluid field inside the exhaust tube in a Gas Circuit Breaker under high temperature, high pressure and high velocity conditions is analyzed by taking compressible effect and some realistic processes into account related to the available experimental data of GCB test facility. Furthermore, computational simulation is conducted to clarify the effective cooling process of SF6 hot gas flow inside the exhaust tube for transient time to avoid the SF6 hot gas breakdown near exhaust tube exit after the arc current interruption. It is found that the SF6 hot gas flow can be effectively cooled down for the rough inside wall of exhaust tube due to the separation of SF6 hot gas flow from the inside wall and also active mixing with upstream cold gas. The effect of roughness pattern on the real time thermofluid field of SF6 hot gas flow and possible breakdown region are also clarified. Finally, the computed temperature in GCB shows the good agreement with the available experimental data for smooth surface of exhaust tube.   

33

Pulverizing, drying and transporting system for injecting a pulverized fuel into a blast furnace  

Disclosed is a pulverizing, drying and transporting system for a puvlerized fuel of a blast furnace of the type having at least one hot stove for supplying hot blast air, said hot stove also providing hot stove exhaust gas. The system includes a pulverizing and drying unit for pulverizing lump raw fuel and drying the pulverized fuel. The hot stove gas is supplied to the pulverizing and drying unit. The hot stove exhaust gas dries the pulverized fuel and conveys it to a pulverized fuel collecting and separating device which separates the gas from the pulverized fuel. The line supplying the hot stove gas to the pulverizing and drying unit includes a heating device for selectively supplying additional heat to the hot stove exhaust gas. Moreover, the line for supplying the hot stove gas to the pulverizing and drying unit can include at least one of a temperature stabilizing device and a cooling device. The heating and cooling devices are controlled by a controller sensitive to the gas temperature at the outlet of the pulverizing and drying unit for maintaining the gas temperature at the outlet of the pulverizing and drying unit at a constant level. The temperature stabilizing device maintains the gas temperature at the outlet of the temperature stabilizing device at a designated level.

34

Design and Performance of a Liquid-Hydrogen, Liquid-Oxygen Gas Generator for Driving a 1000-Horsepower Turbine  

The design and performance of a liquid-hydrogen, liquid-oxygen gas generator using several injector configurations and chamber lengths are presented. The results indicate that high combustion efficiency and reasonable gas temperatures can be achieved if a large number of annular injectors and chamber lengths of about 10 inches are used. Radial variations of gas temperature were observed in the combustion chamber and exhaust nozzle.

35

Fundamental study of NOx removal from diesel exhaust gas by dielectric barrier discharge reactor  

Due to increasingly stringent emission legislation, it is essential to find a solution of eliminating nitrogen oxides (NOx) from diesel exhaust gas. Non-thermal plasma (NTP) approach has been studied for years and has shown advantages. In this study, NOx removal from simulated diesel exhaust gas by a dielectric barrier discharge needle-to-cylinder reactor under room temperature condition is presented. The dielectric barrier consists of a diesel particulate filter (DPF) putting in the discharge field. A simulation gas of N2, NO and O2 combined with particulate matters (PM) was used as the test gas. PM was loaded from a diffusion flame PM generator. The effect of PM and oxygen fraction in exhaust gas on NOx removal characteristics was investigated experimentally. The results showed that PM p...

36

Corrosion behavior of ferritic stainless steels in exhaust gas condensate and evaluation method. Jidosha haiki gas kankyochu ni okeru stainless ko no fushoku kyodo to sono hyokaho  

The present paper studied the corrosion on the inside surface of muffler in the exhaust gas system under the condition of exhaust gas condensate ambience. The muffler materially is aluminium-galvanized steel and stainless steel. Test method was studied to anti-corrosively evaluate the stainless steel against the exhaust gas, through structurally observing corrosive product on the inside surface of muffler of an automobile, having actually run 20000km, and analyzing it by a X-ray micro-analyzer, and investigating the relation of corroding phenomenon with the chemical composition of exhaust gas condensate, etc. The temperature on the inside surface of muffler is higher than 573K as judged from the transformation temperature of corrosive product. The aluminium-galvanized steel plate so entirely thinned for pinholes to be generated, while localized corrosion (pitting corrosion and clearance corrosion) was generated on parts, on which condensate had resided on the stainless steel plate. The main corroding factors are sulfate ion and chloride ion. For the accelerated test to anti-corrosively evaluate the stainless steel in the exhaust gas ambience, the evaluation is optimized under the cyclic heating condition in liquid, around 373 to 673K in temperature. 6 refs., 9 figs., 2 tabs.

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The Effects of Cottonseed Oil-Kerosene Blends on a Diesel Engine Performance and Exhaust Emissions  

Nowadays, increasing crude oil prices and environmental pollution problems have lead to investigation of alternative fuel necessities, such as vegetable oils for internal combustion engines. This article presents the possibility of using cottonseed oil-kerosene blends in compression ignition engines. Engine performance and exhaust emissions were examined and diesel fuel was used as a basis for comparison. The influences of using various blended cottonseed oil-kerosenes on brake specific fuel consumption, exhaust gas temperature, and exhaust emissions values were investigated. Experimental results indicated that engine performance and brake specific fuel consumption were slightly different and SOx emissions were remarkably different from diesel fuel usage.

38

Real-Time Measurement of Vehicle Exhaust Gas Flow  

A flow measurement system was developed to measure, in real-time, the exhaust gas flow from vehicies. This new system was based on the vortex shedding principle using ultrasonic detectors for sensing the shed vortices. The flow meter was designed to measure flow over a range of 1 to 366 Ips with an inaccuracy of ~1o/0 of reading. Additionally, the meter was engineered to cause minimal pressure drop (less than 125mm of water), to function in a high temperature environment (up to 650oC) with thermal transients of 15 oC/s, and to have a response time of 0.1 seconds for a 10% to 90!40 step change. The flow meter was also configured to measure hi-directional flow. Several flow meter prototypes were fabricated, tested, and calibrated in air, simulated exhaust gas, and actual exhaust gas. Testing included gas temperatures to 600oC, step response experiments, and flow rates from O to 360 lps in air and exhaust gas. Two prototypes have been tested extensively at NIST and two additional meters have been installed in exhaust gas flow lines for over one year. This new flow meter design has shown to be accurate, durabIe, fast responding, and to have a wide rangeabi~ity.

39

Diesel and gas engines: evolution following new regulations; Moteurs diesel et gaz: evolution face aux nouvelles reglementations  

Engine emissions of CO, NMHC and ashes are easily lowered through a low-cost exhaust gas processing, while NOx processing in fumes is rather complex and environmentally hazardous; thus, engine manufacturers have emphasized their researches for NOx decrease on the engine design: lower combustion temperature in diesel engines through water cooling or air/air exchanger, lean mixture with excess air (open chamber or pre-chamber) in spark ignition gas engines. Examples of modifications in Caterpillar engines are given. Exhaust gas processing for CO, NMHC, NOx (3 way catalytic purifier, selective catalytic reduction) and ashes is also discussed

40

Aspects of highly transient catalyst simulation  

This work discusses two aspects of simulating catalysts in real world driving situations where frequent and random changes of engine load lead to recurrent, harsh and simultaneous changes in exhaust gas mass flow, temperature and composition. The signals at catalyst inlets attain frequencies of up to 5Hz. Many exhaust gas species composition, mass flow and temperature sensors exhibit delays and low pass behavior that smooth out the signals to frequencies of 1Hz and below. It was investigated how sensitive exhaust gas after-treatment models are to the sampling rate, time delay and low pass deformations of the pre-catalyst time signals used as the model input. Simulation outputs were shown to be very sensitive to these signal deformations. This sensitivity results from the fact that in most ...

 
 
 
 
41

A method for reducing the temperature of exhaust manifolds  

This report describes tests conducted at the Langley Memorial Aeronautical Laboratory on an "air-inducting" exhaust manifold for aircraft engines. The exhaust gases from each cylinder port are discharged into the throat of an exhaust pipe which has a frontal bellmouth. Cooling air is drawn into the pipe, where it surrounds and mixes with the exhaust gases. Temperatures of the manifold shell and of the exhaust gases were obtained in flight for both a conventional manifold and the air-inducting manifold. The air-inducting manifold was installed on an engine which was placed on a test stand. Different fuels were sprayed on and into the manifold to determine whether the use of this manifold reduced the fire hazard. The flight tests showed reductions in manifold temperatures of several hundred degrees, to values below the ignition point of aviation gasoline. On the test stand when the engine was run at idling speeds fuels sprayed into the manifold ignited. It is believed that at low engine speeds the fuel remained in the manifold long enough to become thoroughly heated, and was then ignited by the exhaust gas which had not mixed with cooling air. The use of the air-inducting exhaust manifold must reduce the fire hazard by virtue of its lower operating temperature, but it is not a completely satisfactory solution of the problem.

42

Cogeneration system using gas turbine in home-use paper mill. Kateishi kojo ni okeru gas turbine no cogeneration  

Since many paper mills use much steam and electric power generally, paper mills are suitable to use the cogeneration system. This paper introduces a cogeneration system installed in a paper mill in which a gas turbine is operated to generate electric power by combusting a type low sulfur fuel oil and steam is generated by using waste heat from the gas turbine. The gas turbine is installed indoors and an exhaust muffler is equipped at the back of the junction of the boiler outlet duct and the bypass duct, and the exhaust nozzles for the muffler, ventilation and exhaust gas are equipped on the roof. The generating end efficiency is 24.2% at the conditions of inlet air temperature of 15 centigrade and 100% load. The thermal heat utilization including the generating end efficiency and waste heat recovery is 75.2%. The equipment is to start since March, 1989. 9 figs.

43

Engagement with low-NOx burners in Sunray Reinetsu Co. Ltd. Sunray Reinetsu no tei NOx burner eno taio  

The simple small low-NOx burners, LGX type for medium pressure and LGXL type for low pressure, of Sunray Relnetsu Co. Ltd. were reported. 13A gas or LPG was used as fuel for both type burners, and NOx emission less than 60 ppm was achieved. Various NOx reduction measures were adopted such as membrane combustion, scatter flames and exhaust gas self-recirculation. The membrane combustion was formed by energy of fuel gas for LGX type one or energy of primary air for LGXL type one, and the scatter flames were formed by scatter supply of gas and air. Using the baffle plate with alternate injection and baffle sections for air, low peak combustion temperature and uniform temperature distribution were attained through self-recirculation of combustion gas from the baffle sections to a combustion center. In addition, further several measures were adopted such as baffle plate with an optimum scattering structure to reduce an oxygen content in exhaust gas. 8 figs.

44

Estudo do nitrogênio na combustão do gás natural/ Study of nitrogen in the combustion of natural gas  

Abstract in english Nitrogen content in natural gas was studied in experimental and computational investigations to identify its influence on the emission level of exhaust gases from combustion facilities. Changes in natural gas composition with different N2 concentrations may result from introducing a new source gas into the system. An industrial burner fired at 75 kW, housed in a laboratory-scale furnace, was employed for runs where the natural gas/N2 proportion was varied. The exhaust and (more) in-furnace measurements of temperature and gas concentrations were performed for different combustion scenarios, varying N2 content from 1-10 %v. Results have shown that the contamination of natural gas with nitrogen reduced the peak flame temperature, the concentration of unstable species, the NO X emission level and the heat transfer rate to the furnace walls, resulting from the recombination reactions.

45

Analysis of possibilities of waste heat recovery in off-road vehicles  

The paper presents the preliminary results of the waste heat recovery investigations for an agricultural tractor engine (7.4 dm3) and excavator engine (7.2 dm3) in real operating conditions. The temperature of exhaust gases and exhaust mass flow rate has been measured by precise portable exhaust emissions analyzer SEMTECH DS (SENSORS Inc.). The analysis shows that engines of tested vehicles operate approximately at constant speed and load. The average temperature of exhaust gases is in the range from 300 to 400 °C for maximum gas mass flows of 1100 kg/h and 1400 kg/h for tractor and excavator engine respectively. Preliminary tests show that application of TEGs in tested off-road vehicles offers much more beneficial conditions for waste heat recovery than in case of automotive engines.

46

Gas distributor for fluidized bed coal gasifier  

A gas distributor is described for distributing high temperature reaction gases to a fluidized bed of coal particles in a coal gasification process. The distributor includes a pipe with a refractory reinforced lining and a plurality of openings in the lining through which gas is fed into the bed. These feed openings have an expanding tapered shape in the downstream or exhaust direction which aids in reducing the velocity of the gas jets as they enter the bed.

47

Gas distributor for fluidized bed coal gasifier  

A gas distributor for distributing high temperature reaction gases to a fluidized bed of coal particles in a coal gasification process. The distributor includes a pipe with a refractory reinforced lining and a plurality of openings in the lining through which gas is fed into the bed. These feed openings have an expanding tapered shape in the downstream or exhaust direction which aids in reducing the velocity of the gas jets as they enter the bed.

48

Heated zirconia oxygen sensor for stoichiometric and lean air-fuel ratios  

This publication describes the design and operation of an electrically heated ZrO/sub 2/ sensor and demonstrates its advantages in comparison to the present unheated sensor in a lambda = 1 system. Control ability down to very low exhaust temperatures, minimized temperature dependence and reduced aging effects result in lower emissions with the heated sensor. The application advantages in a lambda = 1 system are discussed. The second part of the paper describes the properties of this heated sensor for measurement of lean exhaust gas. The lambda-range 1.0 to 1.5 can be covered without any additional temperature compensation with sufficient accuracy and stability over life time.

49

Trade-off between NO{sub x}, soot and EGR rates for an IDI diesel engine fuelled with JB5  

Diesel engines have a wide range of uses which has led to increased requirements for petroleum derived from fossil fuel. The depletion of fossil fuel and the impact of increasing environmental pollution from exhaust gas emissions have led the search for alternative fuels. To solve the concerns of both energy and environment, renewable energies with lower environmental pollution impact are necessary. The focus on renewable energy and alternative fuels has increased due to increased oil prices, environmental pollution, and also concern for preserving nature. Biodiesel is known as an attractive alternative fuel although biodiesel produced from edible oil is more expensive than conventional diesel. Therefore, the use of biodiesel produced from non-edible oils is a much better option. Currently Jatropha biodiesel is receiving attention as an alternative fuel for diesel engines. Previous studies reported that Jatropha biodiesel was found to emit higher nitrogen oxides and lower smoke emissions compared to ordinary diesel. Exhaust gas recirculation is an effective technique to reduce nitrogen oxides emission from diesel engines because it enables lowering of both flame temperature and oxygen concentration in the combustion chamber. Some studies succeeded to reduce nitrogen oxides emission from biodiesel fuelled engines using exhaust gas recirculation. However, they observed an increase in soot emission. The aim of this study was to investigate the optimum trade-off between reduction in nitrogen oxides and increase in soot emissions using exhaust gas recirculation for a compression ignition engine fuelled with Jatropha based biodiesel. A 4-cylinder, water-cooled, turbocharged, indirect injection diesel engine was used for investigation. Exhaust emission characteristics were recorded and various engine performance parameters were also evaluated. The results showed that, at 5% exhaust gas recirculation rate along with Jatropha biodiesel blend effectively reduced both nitrogen oxides and soot emission by 27 and 11.3%, respectively, compared to diesel fuel without exhaust gas recirculation.

50

Thermoelectric Generator for a Stationary Diesel Plant  

This paper describes the development and testing of a thermoelectric generator (TEG) using the exhaust heat of a 50-kW stationary diesel power plant. The generator consists of six units that represent primary generators for each diesel engine cylinder. Each primary generator comprises five sections with gas heat exchangers, thermoelectric modules, and liquid heat exchangers. The sections were optimized for the exhaust gas operating temperatures. The generator electric power was 2.1?kW at rated power of 2.2?kW, corresponding to 4.4% of the diesel plant electric power.

51

AEROJET: nonintrusive measurements of aircraft engine exhaust emissions  

The environment impact of air traffic and economical aspects require aircraft engines to be developed which have reduced trace gas emissions and, at the same time, increased efficiency. Each new engine must be shown to meet the environmental requirements laid down by regulatory bodies, and exhaust gas measurements must be performed for the certification. The goal of the EC project AEROJET is to demonstrate the equivalence of remote measurement techniques to conventional extractive methods for both gaseous and particulate measurements. The different remote measurement techniques will be compared and calibrated. A demonstrator measurement system for exhaust gases, temperature and particulates including data-analysis software will be regarded as result of this project.

52

Heating power and oxygen requirement of volatiles from fuel particles as a function of time  

A thermogravimetric analyzer and a flow-calorimeter are combined in order to determine as a function of time the heating power and the oxygen requirement for the complete combustion of the volatiles from solid fuels. The evolved volatiles are burnt in the flow-calorimeter with excess air. The temperature rise of the exhaust gas corresponds to the heating power of the volatiles, and the oxygen concentration in the exhaust gas results in the oxygen requirement for complete combustion of the volatiles. (Abstract Copyright[2002], Wiley Periodicals, Inc.)

53

NO(x) reduction additives for aircraft gas turbine engines  

The reduction of oxides of nitrogen (NO(x)) emissions from aircraft gas turbine engines is a vital part of the NASA High Speed Research Program. Emissions reductions are critical to the feasibility of future High Speed Civil Transports which operate at supersonic speeds in the stratosphere. It is believed that large fleets of such aircraft using conventional gas turbine engines would emit levels of NO(x) that would be harmful to the stratospheric ozone layer. Previous studies have shown that NO(x) emissions can be reduced from stationary powerplant exhausts by the addition of additives such as ammonia to the exhaust gases. Since the exhaust residence times, pressures and temperatures may be different for aircraft gas turbines, a study has been made of additive effectiveness for high speed, high altitude flight.

54

Exhaust-gas systems for modern furnaces. The most important questions and answers on stacks. 2. rev. and enlarged ed. Abgasanlagen fuer moderne Feuerstaetten. Die wichtigsten Fragen und Antworten rund um den Schornstein  

The design of the exhaust gas plant for furnaces with chimneys is of great influence on function and economy of gas- and oil furnaces. Information on the most important questions in connection with the chimney is therefore supplied. Contents: chimney engineering, connecting parts (exhaust gas pipes), accessories of exhaust gas equipment, breakdowns and repair, regulations and rules. Terminology and tables are supplied. (BR).

55

Power generation from waste heat in a food processing application  

In this paper, the potential of recovering waste heat from the fryer section and exhaust stream sent to the stack of a typical potato crisps or chips manufacturing plant and using the heat to drive an Organic Rankine Cycle (ORC) system for power generation has been presented. Five different ORC system Options (A, B, C, D and E) were considered. The first two options (A and B) make use of the waste heat from the foul gas and exhaust to stack respectively for power generation using a single ORC system each while the third option (option C) makes use of a novel dual heat source single ORC system where the low temperature waste heat from the foul gas is used to provide preheating and the high temperature waste from the exhaust to the stack used to provide the evaporation. Option D also shows a...

56

NOx reduction by electron beam-produced nitrogen atom injection  

Deactivated atomic nitrogen generated by an electron beam from a gas stream containing more than 99% N.sub.2 is injected at low temperatures into an engine exhaust to reduce NOx emissions. High NOx reduction efficiency is achieved with compact electron beam devices without use of a catalyst.

57

COMPREHENSIVE ANALYSIS ON PERFORMANCE, COMBUSTION AND EMISSION CHARACTERISTICS FUELED BY VARIOUS BLENDS OF BIODIESEL IN A C.I. ENGINE  

Objectives of this paper: To evaluate performance, combustion and emission of various blends of biodiesel (B20). Corn Oil, Palm Oil, Cotton Seed Oil, Various parameters, Brake Thermal Efficiency, Brake Specific Fuel Consumption, Brake Mean Effective Pressure, Instantaneous Heat Release, Cumulative Heat Release, Exhaust Gas Temperature, CO, CO2, HC, NOx, O2 and Smoke Intensity, To Compare with Diesel

58

Laboratory test of exhaust gas catalysts  

Volkswagen research is running laboratory tests for automotive catalysts. Synthetic exhaust gas is used for the determination of conversion rate in catalyst screening and the study of secondary reactions. The concept of the laboratory test is described and the influence of temperature, ageing and perturbation of air fuel ratio on conversion rate is shown.

59

Damages of compensators at gas turbine exit tubes; Kompensatorschaeden an Gasturbinen-Austrittskanaelen  

In the course of the development of gas turbines for gas and steam turbine power stations (so-called gas/steam installations) providing ever more powerful types, new designs appeared for the subsequent exhaust gas ducting. The various manufacturers applied quite different design solutions to deal with the large cross-sections (several square meters) and the high operating temperatures in the exhaust gas ducts - with the compensators and their internal lining appearing as weak points. (orig.) [German] Im Verlauf der Weiterentwicklung von Gasturbinen fuer Gas- und Dampfkraftwerke (sog. GuD-Anlagen) zu immer leistungsstaerkeren Typen kam es zu Neukonstruktionen der anschliessenden Abgasfuehrung. Die jeweiligen Hersteller gelangten zu recht unterschiedlichen konstruktiven Loesungen fuer die mehrere Quadratmeter grossen Querschnitte und die hohen Betriebstemperaturen in den Abgaskanaelen, wobei sich die Kompensatoren und ihre Innenverkleidung als Schwachstellen herausstellten. (orig.)

60

Study of ceramic rotor and turbine housing material of a turbocharger up to the turbine inlet gas temperature 1050[degree]C  

In order to apply to lean burn engine which drastically reduces the fuel consumption, IHI has been studying a new ceramic turbocharger. Since the exhaust gas temperature is expected to be over 1,000 centigrade, the target of this turbocharger was determined to endure 1,050 centigrade exhaust gas temperature. In addition, the cost is important to be kept in reasonable level as the automotive parts, so that the material of turbine housing was carefully investigated as well as ceramic rotor. For this turbocharger, a ceramic turbine impeller was employed. According to the use of SN84 ceramics which have good properties up to 1,200 centigrade of the turbine inlet gas temperature, enough durability at high temperature and the response were confirmed. These technologies were applied to the IHI RX6 turbocharger for racing, then gave satisfactory results in F1 race. 6 refs., 19 figs., 3 tabs.

 
 
 
 
61

Facility for exhaust gas recirculation regarding diesel engines. Verbrennungskraftmaschine  

A facility for exhaust gas recycling regarding diesel engines is described in which an exhaust gas filter for the recircled exhaust gas is arranged in an exhaust gas recycling circuit branching from the exhaust gas circuit. The insert of the exhaust gas filter in the branch-off point of the exhaust gas recirculation circuit is arranged in a way that its surface on the side of the sewage lies almost parallel to the flow direction of the main exhaust gas flow in the area and course of a normal flow line near to the wall. In a preferred type of design the insert of the filter consists of a shape stabil porous pipe made of sintered ceramics or sintered metal.

62

Facility of exhaust gas recirculation regarding diesel engines. Einrichtung zur Abgasrueckfuehrung bei Dieselmotoren  

A facility for exhaust gas recycling regarding diesel engines is described in which an exhaust gas filter for the recircled exhaust gas is arranged in an exhaust gas recycling circuit branching from the exhaust gas circuit. The insert of the exhaust gas filter in the branch-off point of the exhaust gas recirculation circuit is arranged in a way that its surface on the side of the sewage lies almost parallel to the flow direction of the main exhaust gas flow in the area and course of a normal flow line near to the wall. In a preferred type of design the insert of the filter consists of a shape stabil porous pipe made of sintered ceramics or sintered metal.

63

Roller bearing for exhaust gas turbo-supercharger. Waelzlager fuer Abgasturbolader  

A roller bearing for an exhaust gas turbo-supercharger consists of two roller bearings arranged on a shaft at a distance from each other. High temperatures occur on one side of the shaft. Accurate bearing insensitive to high temperatures is achieved by means of an outer ring which is one-piece and a widened inner ring which is divided. The inner ring, which is adjacent to the high temperatures, is made of a material with high heat resistance.

64

Study of recycling exhaust gas energy of hybrid pneumatic power system with CFD  

A hybrid pneumatic power system (HPPS) is integrated by an internal combustion engine (ICE), a high efficiency turbine, an air compressor and an energy merger pipe, which can not only recycle and store exhaust gas energy but also convert it into useful mechanical energy. Moreover, it can make the ICE operate in its optimal state of maximum efficiency; and thus, it can be considered an effective solution to improve greatly the exhaust emissions and increase the overall energy efficiency of the HPPS. However, in this system, the flow energy merger of both high pressure compressed air flow and high temperature exhaust gas flow of the ICE greatly depends on the merging capability of the energy merger pipe. If the compressed air pressure (P{sub air}) at the air inlet is too high, smooth transmission and mixture of the exhaust gas flow are prevented, which will interfere with the operation condition of the ICE. This shortcoming is mostly omitted in the previous studies. The purpose of this paper is to study the effect of the level of P{sub air} and the contraction of cross-section area (CSA) at the merging position on the flow energy merger and determine their optimum adjustments for a better merging process by using computation fluid dynamics (CFD). In addition, the CFD model was validated on the basis of the experimental data, including the temperature and static pressure of the merger flow at the outlet of the energy merger pipe. It was found that the simulation results were in good agreement with the experimental data. The simulation results show that exhaust gas recycling efficiency and merger flow energy are significantly dependent on the optimum adjustment of the CSA for changes in P{sub air}. Under these optimum adjustments, the exhaust gas recycling efficiency can reach about 83%. These results will be valuable bases to research and design the energy merger pipe of the HPPS.

65

Study of recycling exhaust gas energy of hybrid pneumatic power system with CFD  

A hybrid pneumatic power system (HPPS) is integrated by an internal combustion engine (ICE), a high efficiency turbine, an air compressor and an energy merger pipe, which can not only recycle and store exhaust gas energy but also convert it into useful mechanical energy. Moreover, it can make the ICE operate in its optimal state of maximum efficiency; and thus, it can be considered an effective solution to improve greatly the exhaust emissions and increase the overall energy efficiency of the HPPS. However, in this system, the flow energy merger of both high pressure compressed air flow and high temperature exhaust gas flow of the ICE greatly depends on the merging capability of the energy merger pipe. If the compressed air pressure (P{sub air}) at the air inlet is too high, smooth transmission and mixture of the exhaust gas flow are prevented, which will interfere with the operation condition of the ICE. This shortcoming is mostly omitted in the previous studies. The purpose of this paper is to study the effect of the level of P{sub air} and the contraction of cross-section area (CSA) at the merging position on the flow energy merger and determine their optimum adjustments for a better merging process by using computation fluid dynamics (CFD). In addition, the CFD model was validated on the basis of the experimental data, including the temperature and static pressure of the merger flow at the outlet of the energy merger pipe. It was found that the simulation results were in good agreement with the experimental data. The simulation results show that exhaust gas recycling efficiency and merger flow energy are significantly dependent on the optimum adjustment of the CSA for changes in P{sub air}. Under these optimum adjustments, the exhaust gas recycling efficiency can reach about 83%. These results will be valuable bases to research and design the energy merger pipe of the HPPS. (author)

66

Throttleless Otto-cycle natural-gas-engine experiments. Final report, July 1989  

The throttleless Otto-cycle natural gas engine (TONE) control concept can potentially improve the part-load fuel economy of gas-fueled homogeneous-charge internal combustion engines by reducing the impact of throttle losses. The experimental apparatus and test procedure are described; original data and preliminary test results are included. Results with a Ford LSG423 engine show that for inlet temperatures of 675 degrees F and above with lean fuel mixtures, the exhaust gas temperature was below the heated inlet air temperature. An external heat source would be required for operation in this region of the TONE map.

67

Catalytic converter applications for two stroke, spark-ignited marine engines  

When catalytic converters are used for cleansing of exhaust gas from two-stroke marine engines, new issues must be brought up in combination with prior technology. Therefore, a study was made of V6, 2600cc engine having a large volume of hydrocarbon emissions with respect to three issues: (1) To what degree seawater effects catalytic converter performance and possible countermeasures; (2) Effects attained on cleansing level and catalyst temperature; (3) Finding abatement levels for catalyst deterioration and exhaust emission output in the marine mode. It was found that physical adsorption was a significant factor in catalytic degradation resulting from direct contact with seawater. The cleansing levels obtained when a marine engine is equipped with a catalyst converter were found by clarifying the extent of effects of catalyst volume, performance and temperature. The reduction obtained in exhaust emission allowing for a deterioration factor, is shown in a catalytic converter heated to the maximum temperature of 960 C.

68

Heat exchanger/catalytic system for reducing the exhaust emissions from diesel engines  

A system has been researched over the past 3 years for reducing the exhaust pollutants from diesel engines for light commercial vehicles. The system researched achieves Euro 6 standards for reduction of polluting gases (CO, HC, PM, NO). It consists of 4 main sections: 1. A heater and heat exchanger (HE); 2. A CO/HC oxidising catalyst (D°C); 3. Pt catalyst on a diesel particulate filter (DPF); 4. A NO reducing reaction (SCR) within the DPF. The system operates as follows. The exhaust gas contains oxidising gases, namely both O2 and NO2. The levels of CO and HC are oxidised by O2 to CO2 for temperatures above 200°C. Carbon (PM) is oxidised to CO2 by NO2 but requires a temperature above 250°C. The operating exhaust temperature of 300°C is ideal for the removal of NO by using the Pt catalyst a...

69

Use of gas turbine exhaust for the direct drying of food products: Final report  

The objective of this program was to evaluate the merits of using natural gas-fired gas turbine exhaust to directly dry food products. A survey of drying practices utilized in the food industry and a detailed review of worldwide regulatory drying practices were completed. An investigation of the economic advantages associated with direct drying was also considered. Four drying scenarios were used as part of the analysis: Dilution - hot turbine exhaust gases were diluted with ambient air to achieve temperatures suitable for food product drying; Indirect Heat Exchanger - gas turbine exhaust was directed through an intermediate heat exchanger to avoid flue-gas contamination of the ambient air; Tri-Generation - exhaust gases from the gas turbine were first directed to a heat recovery boiler and then through the drying system to dry the food product; and Conventional Cogeneration - the most conventional simple cycle gas turbine cogeneration (this scenario served as the baseline for all evaluations). Although the economics associated with direct drying appear attractive, the principal concern of any potential use would be the extraordinarily high NO/sub x/ levels and the potential nitrate and nitrosamine (potential carcinogens and carcinogenic precursors) contamination in food products. 21 refs., 21 figs., 17 tabs.

70

Estimating Performance Degradation in Reformers for PAFC Power Plants by Using Increases in Steam-Reformed and Burner-Exhaust Gas Temperatures  

We simulated the performance degradation in a reformer for phosphoric-acid-fuel-cell (PAFC) power plants caused by deterioration of the catalyst loaded in the reformer. We found that the temperatures of the catalyst bed, steam-reformed gas, reformer-tube outer-wall, and burner-exhaust gas rise as the catalyst deteriorates. Increases in the steam-reformed and burner-exhaust gas temperatures at the reformer outlet proved to be the most useful parameters for estimating the drop in reformer performance caused by catalyst deterioration because they could be easily measured during power generation. These temperatures rise and the methane-conversion rate decreases as the catalyst deteriorates. By comparing the simulation results with measurements taken for a 200 kW PAFC power plant, we found that increases in the steam-reformed and burner-exhaust gas temperatures at the reformer outlet, instead of the methane-conversion rate, can be used as parameters for estimating the reformer-performance degradation, and that the steam-reformed-gas temperature is the better parameter of the two.   

71

Investigations on operation of CI engine using producer gas and rice bran oil in mixed fuel mode  

A naturally aspirated multi cylinder diesel genset (DG) was operated successfully with mixed fuels (fossil-diesel (FD), refined rice bran oil (RRBO) and producer gas from a wood gasifier). Performance of DG set in FD, dual fuel mode (FD+RRBO in different proportion and FD+producer gas) and mixed fuels mode (with preheated blend of 75% RRBO+FD and producer gas) at different engine load conditions are presented in this paper. Performance of DG was evaluated in terms of specific energy consumption (SEC), brake thermal efficiency, exhaust gas temperature and exhaust gas composition. Study revealed that blends containing up to 75% RRBO with FD could be used as engine fuel without any adverse effect on the engine. The blend of RRBO and FD was preheated to 60degreeC before use in the compression ...

72

Fuel cell and advanced turbine power cycle  

Solar has a vested interest in integration of gas turbines and high temperature fuels (particularly solid oxide fuel cells[SOFC]); this would be a backup for achieving efficiencies on the order of 60% with low exhaust emissions. Preferred cycle is with the fuel cell as a topping system to the gas turbine; bottoming arrangements (fuel cells using the gas turbine exhaust as air supply) would likely be both larger and less efficient unless complex steam bottoming systems are added. The combined SOFC and gas turbine will have an advantage because it will have lower NOx emissions than any heat engine system. Market niche for initial product entry will be the dispersed or distributed power market in nonattainment areas. First entry will be of 1-2 MW units between the years 2000 and 2004. Development requirements are outlined for both the fuel cell and the gas turbine.

73

Comparative performance and emission studies when using olive oil as a fuel supplement in DI and IDI diesel engines. [Direct inject and indirect injection  

An experimental study is conducted to evaluate and compare the use of a diesel fuel supplement, specifically a 25/75% and a 50/50% blend of waste olive oil and commercial diesel fuel, in a four-stroke, DI (Direct Injection) diesel engine and in a four-stroke, IDI (Indirect Injection) diesel engine having a swirl-combustion chamber. The influence of the blends (diesel fuel + olive oil), for a large range of loads, has been examined on fuel consumption, maximum pressure, exhaust temperature, exhaust smokiness and exhaust-gas emissions such as nitrogen oxides (NO[sub x]), hydrocarbons (HC) and carbon monoxide (CO). The differences in the measured performance and exhaust-emission parameters, from the baseline operation of either engine, are determined and compared. The study shows, for both the DI and IDI engines, a small penalty in specific fuel consumption, a moderate increase in exhaust smokiness and essentially unaltered maximum pressures and exhaust temperatures when using the blends. Also, for both the IDI and DI engines when using the blends, the study shows moderate decreases in emitted nitrogen oxides and increases in hydrocarbons as well as negligible increases in emitted carbon monoxide. Theoretical aspects of diesel engine combustion are used to aid the interpretation of the observed engines' behaviour. (Author).

74

Method and apparatus for ignition system spark timing control where exhaust gas recirculation is used  

A method and apparatus are disclosed for controlling ignition system spark timing where exhaust gas recirculation is employed. The value of spark advance is determined based upon engine operating parameters and exhaust gas recirculation rate is sensed. Correction means is provided which corrects the value of spark advance in accordance with the sensed value or actual valve of exhaust gas recirculation rate.

75

Exhaust gas filter apparatus capable of regeneration of a particulate filter and method  

An exhaust gas filter apparatus includes a particulate filter for collecting a particulate from an exhaust gas. The exhaust gas filter also includes a electromagnetic radiation resonator to heat a portion of the particulate to ignite the particulate and regenerate the particulate filter.

76

In-line hydrocarbon adsorber system for ULEV  

An in-line hydrocarbon (HC) adsorber system was developed to reduce cold start HC emissions. The system comprises a first catalyst, adsorber unit, and a second catalyst for oxidation of desorbed HC. During cold start, exhaust gas is directed to the hydrocarbon adsorber using a fluidic flow diverter unit without any mechanical moving parts in the exhaust system. After the first catalyst lights off, the diverter is shut off and the major portion of the exhaust gas then flows directly to the second catalyst without heating the adsorber unit. After the second catalyst reaches light-off temperature additional air was added to oxidize the desorbed HC. The system attributes are: NMHC emissions in ULEV range; straight line axial flow; reliable design; and limited back pressure penalty. The system was tested on a 3.8L US vehicle.

77

Thermodynamic analysis of a new combined cooling, heat and power system driven by solid oxide fuel cell based on ammonia-water mixture  

Although a solid oxide fuel cell combined with a gas turbine (SOFC-GT) has good performance, the temperature of exhaust from gas turbine is still relatively high. In order to recover the waste heat of exhaust from the SOFC-GT to enhance energy conversion efficiency as well as to reduce the emissions of greenhouse gases and pollutants, in this study a new combined cooling, heat and power (CCHP) system driven by the SOFC is proposed to perform the trigeneration by using ammonia-water mixture to recover the waste heat of exhaust from the SOFC-GT. The CCHP system, whose main fuel is methane, can generate electricity, cooling effect and heat effect simultaneously. The overall system performance has been evaluated by mathematical models and thermodynamic laws. A parametric analysis is also condu...

78

Physical principles governing nonideal behavior of the zirconia oxygen sensor  

Zirconia galvanic cells of the form exhaust gas, Pt parallel stabilized ZrO/sub 2/ parallel Pt, air are installed in the exhaust pipe of automobile engines to provide a voltage signal indicative of engine air-fuel ratio. To account for deviation of experimental sensor behavior from predicted ideal performance, a physical model of nonideal sensors is derived. Nonideal behavior is accounted for by simultaneous presence of two electrochemical reactions occurring at the anode (exhaust gas) electrode; one reaction involves oxygen and the other involves carbon monoxide. Correlation of calculated sensor characteristics with experimental results shows that nonideal sensor electrodes possess surface adsorption properties and catalytic activities which are many orders of magnitude less than ideal equilibrium values. The present theory indicates that undesired temperature-dependent shifting of sensor voltage curves with respect to engine air-fuel ratio is caused by competition between O/sub 2/ and CO gases for triple-point adsorption sites on the anode electrode. (13 fig, 3 tables.)

79

Study on afterburner of aircraft engine. Koku engine yo afterburner no kenkyu  

This paper explains concepts of aircraft engine afterburner, and describes history of afterburner study, and describe the result of major research items. An afterburner is located down stream of a fan, compressor, burner, and turbine in a jet engine. Its basic principle is that fuel is injected into turbine exhaust and fan air flows from an fuel injector, ignited by a spark plug using oxygen remaining in the exhaust gas flow, burned and flame-held by a flame stabilizer. The combustion gas of high temperature (1,700 to 1,800 {degree}c) thus generated is jetted out from an exhaust nozzle to increase the thrust. The prototype afterburner is featured by adoption of a mixed type fuel injection system that provides wide stable combustion range, and flame stabilizer with a scoop aimed at improving the ignition performance and combustion efficiency. A confirmation test verified smooth ignition and wide air to fuel ratio for stabilized combustion. 4 refs., 16 figs.

80

NOVEL GAS SENSORS FOR HIGH-TEMPERATURE FOSSIL FUEL APPLICATIONS  

SRI is developing ceramic-based microsensors for detection of exhaust gases such as NO, NO{sub 2}, and CO in advanced combustion and gasification systems. The sensors detect the electrochemical activity of the exhaust gas species on catalytic electrodes and are designed to operate at high temperatures, elevated pressures, and corrosive environments typical of large power generation exhausts. Under this research project we are developing sensors for multiple gas detection in a single package along with data acquisition and control software and hardware. The sensor package can be easily integrated into online monitoring systems for active emission control. This report details the research activities performed from May 2004 to October 2004 including testing of catalytic materials, sensor design and fabrication, and software development.

 
 
 
 
81

Selective gas exhaustion method  

The present invention provides a method capable of evacuating gases at an exhaustion rate which varies depending on the kind of gases. For example, in a thermonuclear experimental device, a hydrogen gas exhaustion rate is determined to 0 and an exhaustion rate for other impure gases is made greater. Namely, a baffle plate is cooled to a temperature to a level at which the vapor pressure of gases to evacuate a baffle plate is required in a pump incorporating a baffle plate, for example, a cryopump or a sorption pump. In this case, the level of the vapor pressure required for evacuating the exhaustion gas ingredients is 1 x 10{sup -8} Torr or less, preferably, 1 x 10{sup -9} Torr. In a thermonuclear experimental device, a gas having a lower boiling point next to hydrogen is neon, but neon is scarcely present in natural world. Nitrogen has a lower boiling point next thereto, and if the temperature is lowered to such a level that the vapor pressure for evacuating gases such as nitrogen, and carbon monoxide, oxygen, fluorine, argon or methane having a boiling point at or lower than nitrogen is required. Then, evacuation rate sufficient for gases other than hydrogen gas can be obtained. (I.S.)

82

Energy Efficient Thermal Management for Natural Gas Engine Aftertreatment via Active Flow Control  

The project is focused on the development of an energy efficient aftertreatment system capable of reducing NOx and methane by 90% from lean-burn natural gas engines by applying active exhaust flow control. Compared to conventional passive flow-through reactors, the proposed scheme cuts supplemental energy by 50%-70%. The system consists of a Lean NOx Trap (LNT) system and an oxidation catalyst. Through alternating flow control, a major amount of engine exhaust flows through a large portion of the LNT system in the absorption mode, while a small amount of exhaust goes through a small portion of the LNT system in the regeneration or desulfurization mode. By periodically reversing the exhaust gas flow through the oxidation catalyst, a higher temperature profile is maintained in the catalyst bed resulting in greater efficiency of the oxidation catalyst at lower exhaust temperatures. The project involves conceptual design, theoretical analysis, computer simulation, prototype fabrication, and empirical studies. This report details the progress during the first twelve months of the project. The primary activities have been to develop the bench flow reactor system, develop the computer simulation and modeling of the reverse-flow oxidation catalyst, install the engine into the test cell, and begin design of the LNT system.

83

Energy Efficient Thermal Management for Natural Gas Engine Aftertreatment via Active Flow Control  

The project is focused on the development of an energy efficient aftertreatment system capable of reducing NOx and methane by 90% from lean-burn natural gas engines by applying active exhaust flow control. Compared to conventional passive flow-through reactors, the proposed scheme cuts supplemental energy by 50%-70%. The system consists of a Lean NOx Trap (LNT) system and an oxidation catalyst. Through alternating flow control, a major amount of engine exhaust flows through a large portion of the LNT system in the absorption mode, while a small amount of exhaust goes through a small portion of the LNT system in the regeneration or desulfurization mode. By periodically reversing the exhaust gas flow through the oxidation catalyst, a higher temperature profile is maintained in the catalyst bed resulting in greater efficiency of the oxidation catalyst at lower exhaust temperatures. The project involves conceptual design, theoretical analysis, computer simulation, prototype fabrication, and empirical studies. This report details the progress during the first twelve months of the project. The primary activities have been to develop the bench flow reactor system, develop the computer simulation and modeling of the reverse-flow oxidation catalyst, install the engine into the test cell, and begin design of the LNT system.

84

ENERGY EFFICIENT THERMAL MANAGEMENT FOR NATURAL GAS ENGINE AFTERTREATMENT VIA ACTIVE FLOW CONTROL  

The project is focused on the development of an energy efficient aftertreatment system capable of reducing NOx and methane by 90% from lean-burn natural gas engines by applying active exhaust flow control. Compared to conventional passive flow-through reactors, the proposed scheme cuts supplemental energy by 50%-70%. The system consists of a Lean NOx Trap (LNT) system and an oxidation catalyst. Through alternating flow control, a major amount of engine exhaust flows through a large portion of the LNT system in the absorption mode, while a small amount of exhaust goes through a small portion of the LNT system in the regeneration or desulfurization mode. By periodically reversing the exhaust gas flow through the oxidation catalyst, a higher temperature profile is maintained in the catalyst bed resulting in greater efficiency of the oxidation catalyst at lower exhaust temperatures. The project involves conceptual design, theoretical analysis, computer simulation, prototype fabrication, and empirical studies. This report details the progress during the first twelve months of the project. The primary activities have been to develop the bench flow reactor system, develop the computer simulation and modeling of the reverse-flow oxidation catalyst, install the engine into the test cell, and begin design of the LNT system.

85

Zirconia oxygen sensor. Zirconia sanso sensor  

This paper explains firstly two types of oxygen sensor used to measure oxygen concentration in subject gases (such as exhaust gases). One is a sensor corresponding to an oxygen concentration cell provided with porous electrodes (consisting mainly of Pt) on front and rear sides of a solid electrolyte (consisting mainly of ZrO{sub 2}), which generates an electromotive force determined by a ratio of oxygen partial pressures (and of temperatures) between the subject gas coming into contact with respective electrodes and the reference gas (normally air). The other sensor utilizes a fact that the strength of a limit current generated by applying a voltage across the electrodes is proportional to the oxygen concentration in the subject gas. Secondly, the paper describes that controlling automotive exhaust gases uses a tertiary system which combines a tertiary catalyst with an oxygen sensor, and that the point of exhaust gas control using the tertiary system is the output of the said zirconia oxygen sensor that identifies precisely the air excess rate in the exhaust gas at an optimal state (a level the tertiary catalyst exhibits its function most effectively). 2 refs., 3 figs., 1 tab.

86

Chimney manual. Firing and exhaust gas systems: planning, calculation, construction; 3. ed.; Handbuch der Schornsteintechnik. Feuerungsanlagen und Abgassysteme: Planung, Berechnung, Ausfuehrung  

As more and more modern high-efficiency heat generators with low exhaust gas temperature are installed the early adjustment of heat generator and chimney or exhaust gas system is of increasing importance. This book goes into the following subjects of chimney technology: Development of chimney construction, fuels and combustion, bases of chimney technology, chimney systems (design and field of application), chimney and building, air-exhaust gas chimney systems for the connection to gas heating systems which are independent of room air, high-efficiency burner technology, construction and exhaust gas removal of open chimneys, isolated chimneys, chimney retrofitting, costs, environmental protection, building specifications, standards, regulations. (HW) [Deutsch] Durch den verstaerkten Einbau moderner Waermeerzeuger mit hohen feuerungstechnischen Wirkungsgraden und entsprechend niedrigen Abgastemperaturen kommt einer fruehzeitigen Abstimmung von Waermeerzeuger und Schornstein bzw. Abgasanlage steigende Bedeutung zu. Das vorliegende Buch stellt dabei folgende Themenbereiche der Schornsteintechnik vor: Entwicklung des Schornsteinbaus, Brennstoffe und Verbrennung, Grundlagen der Schornsteintechnik, Schornsteinsysteme (Ausfuehrung und Einsatzbereich), Schornstein und Gebaeude, Schornstein und Heizung, Luft-Abgas-Schornsteinsysteme (LAS) zum Anschluss von raumluftunabhaengigen Gasfeuerstaetten, Brennwerttechnik, Aufstellung und Abgasfuehrung von offenen Kaminfeuern, freistehende Schornsteine, Schornsteinsanierung, Kosten, Umweltschutz, Bauvorschriften, Normen, Richtlinien. (HW)

87

A Study on the Control of the Exhaust CO from Gas Boiler  

In this work, the chemical composition of the exhaust gas from domestic gas boiler has been analysed in the point of thermodynamics and CO sensor has been characterized. We proposed that the combustion condition can be estimated by the exhaust gas composition, i.e., the excess air ratio and combustion temperature can be calculated simply by the measurement of the O{sub 2} fraction and H{sub 2}/CO in the exhaust gas. By analyse the on site situation domestic boiler, the excess air ration is about 55 {approx} 110%. Therefor, the CO may be produced in domestic gas boiler by luminous(yellow) flames rapidly lose heat by radiation, turbulent flames may be partially quenched by the action of steep velocity gradients, and flames burning very close to a cold wall may be partially quenched by heat conductivity to the wall. The output voltage of CO sensor is lineally depend on the CO and H{sub 2} concentration. And the exhaust CO from boiler can be reduced by closed loop control with CO sensor. 4 refs., 6 figs., 3 tabs.

88

Thermally activated mobile ejector refrigeration system analysis  

A waste-heat activated vapour ejector refrigeration cycle for automotive air-conditioning applications was studied and analysed. Conservation equations of continuity, momentum, and energy were solved simultaneously, and pressures, temperatures, enthalpies, and mass flow rates at various points in the cycle were computed. The ejector system energy requirements were compared to the available energy in the exhaust gas and the engine coolant. It was found that the engine's coolant energy is superior to that of the exhaust heat energy in activating the system, for most of the engines considered. When considering the exhaust heat, only partial cooling loads up to 1.25 tons of refrigeration could be accommodated. During start-up, when the coolant temperature is not high enough, a supplemental heating system would be necessary. (author)

89

Compact Laser-Based Sensors for Monitoring and Control of Gas Turbine Combustors  

Research is reported on the development of sensors for gas turbine combustor applications that measure real-time gas temperature using near-infrared water vapor absorption and concentration in the combustor exhaust of trace quantities of pollutant NO and CO using mid-infrared absorption. Gas temperature is extracted from the relative absorption strength of two near-infrared transitions of water vapor. From a survey of the water vapor absorption spectrum, two overtone transitions near 1800 nm were selected that can be rapidly scanned in wavelength by injection current tuning a single DFB diode laser. From the ratio of the absorbances on these selected transitions, a path-integrated gas temperature can be extracted in near-real time. Demonstration measurements with this new temperature sensor showed that combustor instabilities could be identified in the power spectrum of the temperature versus time record. These results suggest that this strategy is extremely promising for gas turbine combustor control applications. Measurements of the concentration of NO and CO in the combustor exhaust are demonstrated with mid-infrared transitions using thermo-electrically cooled, quantum cascade lasers operating near 5.26 and 4.62 microns respectively. Measurements of NO are performed in an insulated exhaust duct of a C2H4-air flame at temperatures of approximately 600 K. CO measurements are performed above a rich H2-air flame seeded with CO2 and cooled with excess N2 to 1150 K. Using a balanced ratiometric detection technique a sensitivity of 0.36 ppm-m was achieved for NO and 0.21 ppm-m for CO. Comparisons between measured and predicted water-vapor and CO2 interference are discussed. The mid-infrared laser quantum cascade laser technology is in its infancy; however, these measurements demonstrate the potential for pollutant monitoring in exhaust gases with mid-IR laser absorption.

90

2D mixture fraction measurements in a high pressure and high temperature combustion system using NO tracer-LIF  

Mixture fraction measurements in a jet-in-cross flow configuration at high pressures (15 bar) and temperatures (above 1000 K) were performed using planar laser induced fluorescence of nitric oxide (NO-PLIF) as trace species. The goal was the evaluation of this tracer LIF technique for the characterization of the mixing of fuel and hot exhaust gas in the mixing channel. The fuel (natural gas (NG) or H2/N2/NG mixture) along with the tracer were injected into the crossflow of the exhaust gas and PLIF measurements were performed in different planes. In order to relate the measured NO-LIF signal to fuel concentration and mixture fraction, effects of pressure, temperature and species concentration were taken into account. Numerical calculations and spectroscopic simulations that mimic the experi...

91

Robust control of speed and temperature in a power plant gas turbine  

In this paper, an H~ robust controller has been designed for an identified model of MONTAZER GHAEM power plant gas turbine (GE9001E). In design phase, a linear model (ARX model) which is obtained using real data has been applied. Since the turbine has been used in a combined cycle power plant, its speed and also the exhaust gas temperature should be adjusted simultaneously by controlling fuel signals and compressor inlet guide vane (IGV) position. Considering the limitations on the system inputs, the aim of the control is to maintain the turbine speed and the exhaust gas temperature within desired interval under uncertainties and load demand disturbances. Simulation results of applying the proposed robust controller on the nonlinear model of the system (NARX model), fairly fulfilled the pr...

92

Robust control of speed and temperature in a power plant gas turbine.  

In this paper, an H(?) robust controller has been designed for an identified model of MONTAZER GHAEM power plant gas turbine (GE9001E). In design phase, a linear model (ARX model) which is obtained using real data has been applied. Since the turbine has been used in a combined cycle power plant, its speed and also the exhaust gas temperature should be adjusted simultaneously by controlling fuel signals and compressor inlet guide vane (IGV) position. Considering the limitations on the system inputs, the aim of the control is to maintain the turbine speed and the exhaust gas temperature within desired interval under uncertainties and load demand disturbances. Simulation results of applying the proposed robust controller on the nonlinear model of the system (NARX model), fairly fulfilled the predefined aims. Simulations also show the improvement in the performance compared to MPC and PID controllers for the same conditions. PMID:22062324

93

Turbo-supercharger. Turbolader  

For turbochargers where an auxiliary exhaust gas duct is provided next to the main exhaust gas duct from the exhaust gas side of a turbine casing, there are problems regarding the tolerances to be complied with on the exhaust pipe. The manufacturing costs are also unavoidably increased. Furthermore, the connection of the exhaust pipe is complicated. Finally, the exhaust pipe itself becomes heavy. The purpose of the invention is therefore to create a turbo-supercharger, where an exhaust pipe which is commercially available can be used as the common exhaust pipe for the main exhaust duct and the auxiliary exhaust duct. This makes the manufacture of the exhaust pipe simpler, its weight is lowered, the exhaust pipe connection is made easier, the manufacturing costs are reduced and a satisfactory ejection operation of the main exhaust flow is ensured. A characteristic of the two patent claims is the formation of a single part annular exhaust pipe connection on the outlet side of the turbine case and the separating wall between the main exhaust duct and the auxiliary exhaust duct.

94

Development of glimiting current type zirconia oxygen sensor. Genkai denryushiki zirconia sanso sensor no kaihatsu  

For the purpose of enhancement of the fuel consumption efficiency and purification of the combustion exhaust gas in vehicles, an exhaust gas sensor for lean-burn gasoline engines was developed. Oxygen-pump function of zirconia solid electrolyte was taken notice of, in order to obtain output in proportion to oxygen concentration. When an oxygen pump cell is constructed with zirconia solid electrolyte and oxygen fed into the cathode is controlled by gas diffusion, limiting current is obtained which indicates the oxygen concentration. Oxygen feed into the sensor cathode was limited with a porous layer, by which a rate-determining mechanism for gas diffusion was constructed. It was verified that the developed sensor had many excellent characteristics, such as the output proportional to oxygen concentration, fast response, low dependence on temperature, simple structure of components. The limiting current-type oxygen sensors are applied to vehicles in mass production, and expected for boilers and other combustion machinery. 8 refs., 8 figs.,

95

Production of sulfate aerosol precursors in the turbine and exhaust nozzle of an aircraft engine  

Recent in-flight measurements of aircraft engine exhaust have suggested much higher conversions of fuel sulfur to sulfuric acid aerosols than can be explained by gas-phase oxidation within the exhaust plume. This paper describes the effects of turbine and exhaust nozzle aerodynamics and chemical kinetics on the production of sulfate aerosol precursors in engine exhaust. Results from both one-dimensional (1-D) and two-dimensional (2-D) numerical simulations are presented for a range of flow and chemistry conditions. One-dimensional calculations for the entire postcombustor flow path of an advanced subsonic engine resulted in up to 6.3% sulfur oxidation through the turbine and exhaust nozzle. Results were most sensitive to species concentrations at the combustor exit, combustor exit temperature, and cooling flow mass addition in the turbine. Two-dimensional calculations for a representative turbine demonstrated that intraengine fluid mechanics can increase sulfur oxidation by a factor of 3 across a single blade row because of cooling-induced temperature nonuniformities. Comparisons of averaged 2-D results with 1-D simulations of the same blade row further showed that while 1-D simulations produce the correct trends, the magnitude of change in sulfur oxidation may be underpredicted by as much as 47% over a single blade row if spatial nonuniformities in flow field temperature are not included.

96

Technical evaluation of simplified IGCC components  

Simplified integrated gasification combined cycle (IGCC) power plants offer attractive advantages for improving the performance of coal to electricity systems. This plant configuration, which utilizes a coal gasifier, hot gas cleanup system, and gas turbine combined cycle, has the potential to reduce both capital costs for equipment and fuel costs through improved efficiency. This paper reports the results of fuel supply and gas turbine testing on actual hot low-Btu coal gas. A pilot-scale advanced fixed-bed gasifier has been modified to supply hot coal gas to a particulate removal cyclone and then to a gas turbine simulator. The hot gas is combusted in a General Electric MS6000 combustor developed for low-Btu gas fuel. The combusted product flows through a MS6000 turbine first-stage nozzle sector. The exhaust gases from the nozzle sector pass over air-cooled cylindrical ash deposition pin specimens and then into a water quench exhaust system. Extensive instrumentation and sampling provisions are utilized to characterize the fuel gas, the combustion gases, and the ash deposits formed on turbine components. Two regimes of nozzle metal surface temperatures have been investigated by separate testing performed including 500-600 /sup 0/F with water-cooled and 1500-1650 /sup 0/F with air-cooled nozzle sectors. Results from the test program have provided key data related to fuel gas cleanup and the tolerance of gas turbine hot gas path parts to the products of combustion from coal-derived fuels.

97

Combination acoustical muffler and exhaust converter  

A combination acoustical muffler and exhaust converter for use with internal combustion engines, comprising an elongated hollow cylinder adapted to be connected to a source of exhaust gas, screen means positioned at a plurality of longitudinally spaced locations within said cylinder for partitioning the cylinder into a plurality of chambers arranged in series flow relation with each other and with respect to the flow of exhaust gas through said cylinder, the screens having a silencing action on said exhaust gas, magnet means in one of said chambers for exerting a magnetic pressure on the gas passing therethrough to serve to separate ferrous particles from the exhaust gas stream, a packing material of mineral material, such as mineral wool, in another of said chambers for condensing moisture in said exhaust gas and for removing hydrocarbon therefrom, and a material such as a ceramic material of an extremely fine porous nature, in still another of said chambers for removing carbon monoxide from said exhaust gas.

98

Experimental and numerical investigation on combustion characteristics of premixed hydrogen/air flame in a micro-combustor with a bluff body  

Combustion characteristics of lean hydrogen/air mixture in a planar micro-channel with a bluff body were investigated experimentally and numerically. Effects of the inlet velocity and equivalence ratio on the blow-off limit, combustion efficiency and exhaust gas temperature were examined. The results show that the blow-off limit is greatly extended as compared with that of the micro-combustor without a bluff body. Moreover, the blow-off limit increases as the equivalence ratio is increased from 0.4 to 0.6. Furthermore, with the increase of inlet velocity, the flame front is prolonged and becomes narrower, and the high temperature segment of outer wall shifts downstream. In addition, the combustion efficiency and exhaust gas temperature increase first and then decrease with the increase of ...

99

Experimental Study on Pressurization Smoke Control by Using a Medium-Size Model (Part 1)  

A series of pressurization smoke control experiments were conducted using a fire room [2. 7 m × 3. 6 m × 1. 18 m (height)] of two-fifths reduced scale model for examining air supply conditions necessary to prevent smoke efflux from a fire room. For understanding the prediction of the critical air velocity to prevent smoke backflow under pressurization smoke control, the temperature of the hot layer formed in a fire room shall be well-assessed. Therefore, the temperature of the hot layer in a fire room and the waste gas of the exhaust were measured for constructing equations for simple prediction. In case of pressurization smoke control, the algebraic simple equation on the temperature of the hot layer in a fire room at unsteady state is proposed in consideration of the heat loss by the waste gas of the exhaust based on these experimental data.   

100

Turbocharger for internal combustion engines. Turbolader fuer Brennkraftmaschinen  

The invention deals with a turbocharger for internal combustion engines. The running wheel of the turbine is impelled by a radial directed flow. The circumference of the running wheel is provided with a helical shaft channel with inlet slit. The width of this inlet slit aperture can be controlled in function of the engine parameters. It is intended to control the flow volume for the running wheel in dependence of the exhaust temperature. For this reason a ring disk, installed parallel to the turbine case, controls by heat deformation the cross-section of the slit aperture. If the temperature increases then the cross-section is enlarged; a decreasing temperature reduces the aperture size. By this measure it is possible to design the turbocharger for the complete gas volume. In the maximum load range the exhaust gas pressure can be smaller.

 
 
 
 
101

Energy and exergy analyses of a CFB-based indirectly fired combined cycle power generation system  

Combined cycle configuration has the ability to use the waste heat from the gas turbine exhaust gas using the heat recovery steam generator for the bottoming steam cycle. In the current study, a natural gas-fired combined cycle with indirectly fired heating for additional work output is investigated for configurations with and without reheat combustor (RHC) in the gas turbine. The mass flow rate of coal for the indirect-firing mode in circulating fluidized bed (CFB) combustor is estimated based on fixed natural gas input for the gas turbine combustion chamber (GTCC). The effects of pressure ratio, gas turbine inlet temperature, inlet temperatures to the air compressor and to the GTCC on the overall cycle performance of the combined cycle configuration are analysed. The combined cycle effic...

102

Pollution control apparatus  

This patent describes a pollution control apparatus for a motor vehicle having an engine discharging exhaust gases into a muffler and out through a tail pipe. It comprises: means to spray water into the exhaust gases into produce a mist of water droplets containing dissolved and entrained pollutants in the exhaust gases and connected to the muffler, means to separate the water droplets from the exhaust gas mist and pass cleaned exhaust gases from the muffler and out through the tail pipe.

103

Gas separation process using membranes with permeate sweep to remove CO.sub.2 from gaseous fuel combustion exhaust  

A gas separation process for treating exhaust gases from the combustion of gaseous fuels, and gaseous fuel combustion processes including such gas separation. The invention involves routing a first portion of the exhaust stream to a carbon dioxide capture step, while simultaneously flowing a second portion of the exhaust gas stream across the feed side of a membrane, flowing a sweep gas stream, usually air, across the permeate side, then passing the permeate/sweep gas back to the combustor.

104

A Highly Efficient Six-Stroke Internal Combustion Engine Cycle with Water Injection for In-Cylinder Exhaust Heat Recovery  

A concept is presented here that adds two additional strokes to the four-stroke Otto or Diesel cycle that has the potential to increase fuel efficiency of the basic cycle. The engine cycle can be thought of as a 4 stroke Otto or Diesel cycle followed by a 2-stroke heat recovery steam cycle. Early exhaust valve closing during the exhaust stroke coupled with water injection are employed to add an additional power stroke at the end of the conventional four-stroke Otto or Diesel cycle. An ideal thermodynamics model of the exhaust gas compression, water injection at top center, and expansion was used to investigate this modification that effectively recovers waste heat from both the engine coolant and combustion exhaust gas. Thus, this concept recovers energy from two waste heat sources of current engine designs and converts heat normally discarded to useable power and work. This concept has the potential of a substantial increase in fuel efficiency over existing conventional internal combustion engines, and under appropriate injected water conditions, increase the fuel efficiency without incurring a decrease in power density. By changing the exhaust valve closing angle during the exhaust stroke, the ideal amount of exhaust can be recompressed for the amount of water injected, thereby minimizing the work input and maximizing the mean effective pressure of the steam expansion stroke (MEPsteam). The value of this exhaust valve closing for maximum MEPsteam depends on the limiting conditions of either one bar or the dew point temperature of the expansion gas/moisture mixture when the exhaust valve opens to discard the spent gas mixture in the sixth stroke. The range of MEPsteam calculated for the geometry of a conventional gasoline spark-ignited internal combustion engine and for plausible water injection parameters is from 0.75 to 2.5 bars. Typical combustion mean effective pressures (MEPcombustion) of naturally aspirated gasoline engines are up to 10 bar, thus this concept has the potential to significantly increase the engine efficiency and fuel economy while not resulting in a decrease in power density.

105

Method and apparatus for disposing of water at gas wells  

This patent describes a method for disposing of water produced by a gas well assembly, which gas well assembly includes a gas compressor which produces hot exhaust and a muffler for muffling the noise of the exhaust from the gas compressor. It comprises: circulating the water in heat exchange relation with the hot exhaust under conditions permitting the water to vaporize, wherein such circulation is carried out in a vessel through which a conduit carrying the hot exhaust is submerged; venting steam produced by such circulation; and feeding a stream of hot exhaust from the muffler through the vessel for promoting the venting of steam from the vessel.

106

Research and development of ceramic gas turbine  

The CO{sub 2} caused by the consumption of hydrocarbon fuel is one of the main gases which affect the global climate. In order to reduce the formation of CO{sub 2}, it is necessary to conserve energy as effectively as possible. Therefore the heat energy provided by the fuel should be utilized in multi-cascades. The energy at the high temperature should be used for the generation of electric power and the energy at low temperature could be used for making the steam and the hot water. The gas turbine is preferable for this purpose. The heat energy of exhaust gas can be reused more easily. The two systems are proposed by using the gas turbine as the high temperature stage. One is the cogeneration system and the other is the combined cycle. The former generates electric power by the gas turbine and make steam or hot water in the exhaust gas. The latter employs the gas turbine as the high temperature cycle and the steam turbine as the low temperature cycle.

107

Thermal engine driven heat pump for recovery of volatile organic compounds  

This patent describes an apparatus for separating volatile organic compounds from a stream of gas. It comprises an internal combustion engine including a rotating shaft; an inert gas generating means for converting at least a portion of exhaust from the internal combustion engine into an inert gas and mixing the inert gas into the stream of gas; heat transfer means for recovering waste heat from the internal combustion engine to heat a portion of the stream of gas; a first and a second refrigeration system operatively connected to the rotating shaft of the internal combustion engine, the first and the second refrigeration systems operating at substantially different temperatures, the first and second refrigeration systems receiving the stream of gas and cooling the stream of gas thereby extracting the volatile organic compounds therefrom.

108

High Velocity Exhaust Diffuser and Water Baffle.  

The patent describes a diffuser and baffle device which prevents sea water intrusion or ingestion into a marine gas turbine engine exhaust system without significantly increasing exhaust back pressure. Inboard and outboard rows of vertical turning vanes a...

109

Evaluating tractor performance and exhaust gas emissions using biodiesel from cotton seed oil  

Alternative fuels for diesel engines, such as biodiesel, have attracted much attention recently due to increasing fuel prices and the imperative to reduce emissions. The exhaust gas emissions from tractors and other agricultural machinery make a significant contribution to these emissions. The use of biodiesel in internal combustion engines (ICE) has been reported to give comparable performance to conventional diesel (CD), but with generally lower emissions. There is however, contradictory evidence of NO emissions being both higher and lower from the use of biodiesel. In this work, agriculture tractor engine performance and its emission using both CD and biodiesel from cotton seed oil (CSO-B20) mixed at a 20% blend ration has been evaluated and compared. The PTO test results showed comparable exhaust emissions between CD and CSO-B20. However, the use of CSO-B20 led to reductions in the thermal efficiency and exhaust temperature and an increase in the brake specific fuel consumption (BSFC), when compared to CD.

110

A failure analysis of exhaust systems for naval gas turbines. Part II: Design changes  

Cracks have nucleated and propagated through the exhaust systems of naval gas turbines. The main cracks have propagated, along the circumferential direction, from the weld toe of some butt and fillet welded joints located near the lower supporting ring, where the temperature measured with a Cu-Ni thermocouple was about 350degreeC. The exhaust system studied has more than 8m long and the dimensions of the cross sections varies from 1.5mx1m at the inlet section to 2.6mx2m at the outlet section. The structure is thermally insulated and is made of AISI 316L stainless steel grade type plates, with a wall thickness of about 4mm, which were bent in roll machines and mainly butt welded by MIG/MAG welding process. This paper presents finite element analyses (FEA) of the exhaust system outlined befo...

111

Development of dry analytical method for formaldehyde in exhaust emissions. Haishutsu gas chu no aldehyde no kanshiki bunsekiho no kaihatsu  

In the dry analytical method of formaldehyde in automobile exhaust emission, sampling conditions such as temperature and flow rate, and measurable concentration ranges were examined. Silicagel cartridges coated with 2,4-dinitrophenylhydrazin (DNPH) were prepared, and a prototype gas sampling system was fabricated to sample by both conventional impinger method and the cartridge method at the same time, and a high performance liquid chromatograph was used for analysis. As a result, since a collection efficiency reached 100% at 70 {degree} C in a high formaldehyde concentration range over 10ppm, it was necessary to heat a sampling line. As heated, formaldehyde was fully collected independently of moisture in exhaust emission, and a sampling rate of 0.5l/min was also desirable. The measurable concentration range entirely covered that of formaldehyde in exhaust emission, and a measurement accuracy was also equivalent to that of the impinger method. 4 refs., 7 figs., 4 tabs.

112

Combustion and NOx emission characteristics of a retrofitted down-fired 660 MWe utility boiler at different loads  

Industrial experiments were performed for a retrofitted 660 MWe full-scale down-fired boiler. Measurements of ignition of the primary air/fuel mixture flow, the gas temperature distribution of the furnace and the gas components in the furnace were conducted at loads of 660, 550 and 330 MWe. With decreasing load, the gas temperature decreases and the ignition position of the primary coal/air flow becomes farther along the axis of the fuel-rich pipe in the burner region under the arches. The furnace temperature also decreases with decreasing load, as does the difference between the temperatures in the burning region and the lower position of the burnout region. With decreasing load, the exhaust gas temperature decreases from 129.8{sup o}C to 114.3{sup o}C, while NOx emissions decrease from 2448 to 1610 mg/m{sup 3}. All three loads result in low carbon content in fly ash and great boiler thermal efficiency higher than 92%. Compared with the case of 660 MWe before retrofit, the exhaust gas temperature decreased from 136 to 129.8{sup o}C, the carbon content in the fly ash decreased from 9.55% to 2.43% and the boiler efficiency increased from 84.54% to 93.66%.

113

Prediction and Performance of Compact Heat Exchanger with Small Diameter Tubes for Latent Heat Recovery  

The most part of energy losses in power system such as fuel cells is due to the heat released by the exhaust gas to atmosphere. The exhaust gas consists of non-condensable gas and steam with sensible and latent heat. As a lot of latent heat is included in the exhaust gas, its recovery is very important to improve the power system efficiency. Based on the previous basic studies, a thermal hydraulic prediction method for latent heat recovery exchangers was proposed. For the condensation of steam on heat transfer tubes, the modified Sherwood number taking account of the mass absorption effect on the wall was used. Two kinds of compact heat exchanger with staggered banks of bare tubes of 10.5 or 4mm in outer diameter was designed with the prediction method. The more compactness was obtained with the smaller tubes at a designed heat recovery. The thermal hydraulic behavior in the compact heat exchangers was experimentally studied with air-steam mixture gas. In the parametric experiments varying the steam mass concentration, the temperature distributions of cooling water and mixture gas were measured. The experimental results agreed well with the prediction proposed in this study and the more compactness with the smaller tubes was proved.   

114

Impact of EGR fraction on diesel engine performance considering heat loss and temperature-dependent properties of the working fluid  

Exhaust gas recirculation (EGR) to reduce feed gas NOx emission is common practice in modern diesel engines. Dilution of the intake air with cooled recirculated exhaust gas limits the production of in-cylinder NOx due to a lowering of the adiabatic flame temperature and a reduction in oxygen content of the intake mixture. EGR also reduces the mixture-averaged ratio of specific heats (g) of the combustion charge leading to a reduction in the thermodynamic cycle efficiency. This trade-off between minimizing NOx production and maximizing cycle efficiency is of critical importance when calibrating EGR control schemes. Modeling tools that allow a quantitative analysis of this trade-off can be very beneficial in tuning EGR systems over a range of operating conditions. In this study, the systemat...

115

Control-oriented modeling of a three-way catalytic converter with observation of the relative oxygen level profile  

The paper presents a novel control-oriented, first-principle model of a three-way catalytic converter (TWC). The model accurately predicts the air-fuel ratio downstream of the catalyst and provides insights into the relative oxygen level (ROL) profile along the catalyst. The reaction mechanism of the TWC model is simplified to only two reactions, with oxygen being the only species stored on the active surface of the catalyst. All the information about the gas composition is taken from the upstream wide-range oxygen sensor. Additional model inputs are the exhaust gas temperature and the exhaust mass flow. The model is parameterized with only a few measurements from an engine test bench. Exact values of gas concentrations are not needed at any point. The ROL profile is a good indicator for t...

116

Performance of High Temperature Air Combustion Boiler with Low NOx Emission  

Thermal performance in the experiments and three-dimensional numerical simulations for a high temperature air combustion boiler where fuel can be efficiently combusted by high temperature preheated air (800°C-1000°C) is examined. The boiler can burn not only natural gas but also low calorific gas (e. g. full gasification gas obtained from coal or wastes). In the boiler, four regenerative burners are installed. This boiler has new features that not only air but also gasification gas is heated up to 900°C, and combination of burners is switched every 15 seconds where two burners are used as inlets of fuel and air and the other two burners are used as outlets of exhaust gas. Natural gas and syngas obtained from coal are burned. The NOx emission for each fuel is less than 50ppm. The heat transfer of three-dimensional calculation is predicted higher than that of experiment.   

117

Effect of exhaust gas recirculation on diesel engine nitrogen oxide reduction operating with jojoba methyl ester  

Jojoba methyl ester (JME) has been used as a renewable fuel in numerous studies evaluating its potential use in diesel engines. These studies showed that this fuel is good gas oil substitute but an increase in the nitrogenous oxides emissions was observed at all operating conditions. The aim of this study mainly was to quantify the efficiency of exhaust gas recirculation (EGR) when using JME fuel in a fully instrumented, two-cylinder, naturally aspirated, four-stroke direct injection diesel engine. The tests were carried out in three sections. Firstly, the measured performance and exhaust emissions of the diesel engine operating with diesel fuel and JME at various speeds under full load are determined and compared. Secondly, tests were performed at constant speed with two loads to investigate the EGR effect on engine performance and exhaust emissions including nitrogenous oxides (NO{sub x}), carbon monoxide (CO), unburned hydrocarbons (HC) and exhaust gas temperatures. Thirdly, the effect of cooled EGR with high ratio at full load on engine performance and emissions was examined. The results showed that EGR is an effective technique for reducing NO{sub x} emissions with JME fuel especially in light-duty diesel engines. With the application of the EGR method, the CO and HC concentration in the engine-out emissions increased. For all operating conditions, a better trade-off between HC, CO and NO{sub x} emissions can be attained within a limited EGR rate of 5-15% with very little economy penalty. (author)

118

Dynamic optimal design of a power generation system utilizing industrial waste heat considering parameter fluctuations of exhaust gas  

The industrial waste heat parameters, like flow rate and temperature, usually fluctuate in a certain range due to the variation of upstream industrial process. However, the heat recovery systems are usually designed not under the fluctuation range but under a specific point, therefore, the most reasonable design condition of the waste heat should be estimated based on the fluctuation ranges. A single pressure waste heat recovery system was studied in this paper. Static models were developed for system design and dynamic models were established to simulate the system transient performance when the temperature or flow rate of exhaust gas fluctuates. Systems designed at different exhaust gas parameters were operated under the same fluctuation condition to find out which one could generate the...

119

Operating experience with fabric filters in lime shaft kilns. Betriebserfahrungen mit Faserstoff-Filtern an Kalkschachtoefen  

In order to comply with the increased requirements of the legislature 2 lime shaft kilns in a Sauerland lime plant were equipped with a reverse-jet fabric filter. The dust in the crude gas from the kilns, which are fired with a variety of fuels, contained constituents from the fuel and impurities from the limestone in addition to the predominant calcium carbonate and calcium oxide. The dedusting system is adapted to suit the changing operating conditions such as starting and stopping, and one- and two-kiln operation with various fuels. The operating temperature required for Nomex needle felt of 180deg C is maintained by cooling the kiln exhaust gas with exhaust air from the lime silo or with fresh air. The plant is designed so that it can deal with corrosion, temperature fluctuations and changing operating conditions. The emission limit of less than 50 mg/m{sup 3} required by the Clean Air Technical Code is met during continuous operation. (orig.).

120

Analysis of reformed EGR on the performance of a diesel particulate filter  

The use of a diesel particulate filter (DPF) in combination with an upstream diesel oxidation catalyst (DOC) has been successfully implemented and shown to reduce carbon monoxide (CO), hydrocarbon (HC) and Particulate Matter (PM) diesel exhaust gas emissions. However issues including cost, size and uncontrolled active regeneration under a low temperature window still require attention. This study therefore primarily focuses on the potential benefits of using a single catalytic coated DPF (cDPF) and a combined DOC-cDPF instead of the DOC-DPF aftertreatment system utilising a passive, low temperature regeneration method. Comparisons were made through monitoring exhaust gas compositions from an experimental single cylinder diesel engine as well as measuring the pressure drop across the filter...

 
 
 
 
121

Thermodynamic analysis of a Rankine cycle applied on a diesel truck engine using steam and organic medium  

A theoretical study is conducted to investigate the potential improvement of the overall efficiency of a heavy-duty truck diesel engine equipped with a Rankine bottoming cycle for recovering heat from the exhaust gas. To this scope, a newly developed thermodynamic simulation model has been used, considering two different working media: water and the refrigerant R245ca. As revealed from the analysis, due to the variation of exhaust gas temperature with engine load it is necessary to modify the Rankine cycle parameters i.e. high pressure and superheated vapor temperature. For this reason, a new calculation procedure is applied for the estimation of the optimum Rankine cycle parameters at each operating condition. The calculation algorithm is conducted by taking certain design criteria into a...

122

Experimental investigation of diesel engine performance and emission characteristics using jojoba/diesel blend and sunflower oil  

Experimental study has been carried out to investigate performance parameters, emissions, cylinder pressure, exhaust gas temperature (Texhaust) and engine wall temperatures (Twall) for direct injection diesel engine. Tests were conducted for sunflower oil (S100) and 20% jojoba oil+80% pure diesel fuel (B20) in comparison to pure diesel fuel with different engine speeds. S100 and B20 were selected for the study because of its being widely used in Egypt and in the world. Also, series of tests are conducted at same previous conditions with different percentage of exhaust gas recirculation (EGR) from 0% to 12% of inlet mass of air fresh charge. Results indicate that S100 or B20 gives lower brake thermal efficiency (B), brake power (BP), brake mean effective pressure (BMEP), and higher brake sp...

123

Fast optical measurements and imaging of flow mixing: Fast optical measurements and imaging of temperature in combined fossil fuel and biomass/waste systems  

Project is focused on fast time-resolved infrared measurements of gas temperature and fast IR-imagining of flames in various combustion environments. The infrared spectrometer system was developed in the project for fast infrared spectral measurements on industrial scale using IR-fibre- optics. Fast time-and spectral-resolved measurements in 1.5-5.1 mu spectral range give information about flame characteristics like gas and particle temperatures, eddies and turbulent gas mixing. Time-resolved gas composition in that spectral range (H{sub 2}O, CH{sub 4}, CO{sub 2}, CO) which is one of the key parameters in combustion enhancement can be also obtained. The infrared camera was also used together with special endoscope optics for fast thermal imaging of a coal-straw flame in an industrial boiler. Obtained time-resolved infrared images provided useful information for the diagnostics of the flame and fuel distribustion. The applicability of the system for gas leak detection is also demonstrated. The infrared spectrometer system with minor developments was applied for fast time-resolved exhaust gas temperature measurements performed simultaneously at the three optical ports of the exhaust duct of a marine Diesel engine and visualisation of gas flow behaviour in cylinder. (Author)

124

Modeling and sensitivity analysis study of the reduction of NO sub x by HNCO. [RAPRENOx process  

A chemical mechanism for the reduction of NO{sub x} by HNCO has been constructed to allow for the modeling of NO{sub x} in exhausts typical of natural gas combustion (RAPRENOx process). The reduction was modeled assuming plug flow, and either isothermal combustion or constant pressure adiabatic combustion. Variables were initial concentrations of NO, NO{sub 2}, CO, CH{sub 4}, H{sub 2}, and HNCO as well as initial temperatures. Exhaust residence time was nominally 1 s. Reduction was not achieved for prototypical natural gas exhaust'' for a reasonable residence time. Radical generation is crucial for reduction. H{sub 2} addition enhanced ignition and reduction. The final combustion temperature determines where NO{sub x} reduction ceases and NO{sub x} production increases. Reduction increases with HNCO, and breakthrough of NH{sub 3} and HNCO increses as well. N{sub 2}O production is due to NCO + NO, but the reduction of NO also occurs through reactions associated with the Thermal De-NOx chemistry. NH{sub 3} production and reactions are important to the reduction of NO. Sensitivity analysis under easy ignition conditions indicated that the same reactions involving nitrogen species, NH{sub 2} and NNH, important in De-NOx, are important when HNCO is used to reduce NO{sub x}. A real combustion exhaust would contain radicals, but it would be neither isothermal nor adiabatic, and heat release and loss would accompany the reduction process. Three-body recombination reactions are important and need further study.(DLC)

125

Modeling and sensitivity analysis study of the reduction of NO{sub x} by HNCO  

A chemical mechanism for the reduction of NO{sub x} by HNCO has been constructed to allow for the modeling of NO{sub x} in exhausts typical of natural gas combustion (RAPRENOx process). The reduction was modeled assuming plug flow, and either isothermal combustion or constant pressure adiabatic combustion. Variables were initial concentrations of NO, NO{sub 2}, CO, CH{sub 4}, H{sub 2}, and HNCO as well as initial temperatures. Exhaust residence time was nominally 1 s. Reduction was not achieved for prototypical ``natural gas exhaust`` for a reasonable residence time. Radical generation is crucial for reduction. H{sub 2} addition enhanced ignition and reduction. The final combustion temperature determines where NO{sub x} reduction ceases and NO{sub x} production increases. Reduction increases with HNCO, and breakthrough of NH{sub 3} and HNCO increses as well. N{sub 2}O production is due to NCO + NO, but the reduction of NO also occurs through reactions associated with the Thermal De-NOx chemistry. NH{sub 3} production and reactions are important to the reduction of NO. Sensitivity analysis under easy ignition conditions indicated that the same reactions involving nitrogen species, NH{sub 2} and NNH, important in De-NOx, are important when HNCO is used to reduce NO{sub x}. A real combustion exhaust would contain radicals, but it would be neither isothermal nor adiabatic, and heat release and loss would accompany the reduction process. Three-body recombination reactions are important and need further study.(DLC)

126

Effect of operating and sampling conditions on the exhaust gas composition of small-scale power generators.  

Small stationary diesel engines, like in generator sets, have limited emission control measures and are therefore responsible for 44% of the particulate matter (PM) emissions in the United States. The diesel exhaust composition depends on operating conditions of the combustion engine. Furthermore, the measurements are influenced by the used sampling method. This study examines the effect of engine loading and exhaust gas dilution on the composition of small-scale power generators. These generators are used in different operating conditions than road-transport vehicles, resulting in different emission characteristics. Experimental data were obtained for gaseous volatile organic compounds (VOC) and PM mass concentration, elemental composition and nitrate content. The exhaust composition depends on load condition because of its effect on fuel consumption, engine wear and combustion temperature. Higher load conditions result in lower PM concentration and sharper edged particles with larger aerodynamic diameters. A positive correlation with load condition was found for K, Ca, Sr, Mn, Cu, Zn and Pb adsorbed on PM, elements that originate from lubricating oil or engine corrosion. The nitrate concentration decreases at higher load conditions, due to enhanced nitrate dissociation to gaseous NO at higher engine temperatures. Dilution on the other hand decreases PM and nitrate concentration and increases gaseous VOC and adsorbed metal content. In conclusion, these data show that operating and sampling conditions have a major effect on the exhaust gas composition of small-scale diesel generators. Therefore, care must be taken when designing new experiments or comparing literature results. PMID:22442670

127

Characterization of major chemical components of fine particulate matter in North Carolina.  

Small stationary diesel engines, like in generator sets, have limited emission control measures and are therefore responsible for 44% of the particulate matter (PM) emissions in the United States. The diesel exhaust composition depends on operating conditions of the combustion engine. Furthermore, the measurements are influenced by the used sampling method. This study examines the effect of engine loading and exhaust gas dilution on the composition of small-scale power generators. These generators are used in different operating conditions than road-transport vehicles, resulting in different emission characteristics. Experimental data were obtained for gaseous volatile organic compounds (VOC) and PM mass concentration, elemental composition and nitrate content. The exhaust composition depends on load condition because of its effect on fuel consumption, engine wear and combustion temperature. Higher load conditions result in lower PM concentration and sharper edged particles with larger aerodynamic diameters. A positive correlation with load condition was found for K, Ca, Sr, Mn, Cu, Zn and Pb adsorbed on PM, elements that originate from lubricating oil or engine corrosion. The nitrate concentration decreases at higher load conditions, due to enhanced nitrate dissociation to gaseous NO at higher engine temperatures. Dilution on the other hand decreases PM and nitrate concentration and increases gaseous VOC and adsorbed metal content. In conclusion, these data show that operating and sampling conditions have a major effect on the exhaust gas composition of small-scale diesel generators. Therefore, care must be taken when designing new experiments or comparing literature results. PMID:16933642

128

Time-resolved nature of exhaust gas emissions and piston wall temperature under transient operation in a small diesel engine  

Diesel combustion and exhaust gas emissions under transient operation (when fuel amounts abruptly increased) were investigated under a wide range of operating conditions with a newly developed gas sampling system. The relation between gas emissions and piston wall temperatures was also investigated. The results indicated that after the start of acceleration NOx, THC and smoke showed transient behaviors before reaching the steady state condition. Of the three gases, THC was most affected by piston wall temperature; its concentration decreased as the wall temperature increased throughout the acceleration except immediately after the start of acceleration. The number of cycles, at which gas concentrations reach the steady-state value after the start of acceleration, were about 1.2 times the cycle constant of the piston wall temperature for THC, and 2.3 times for smoke.

129

Feeding exhaust gases to the rotor of a centripetal turbine of an exhaust turbo-supercharger  

The feed pipe of the exhaust gases from a combustion engine to the rotor of a centrifugal turbine of an exhaust gas turbo-supercharger consists of a system of pipes connecting the engine to the turbine case, where the turbine case has three radial outlets opening towards the rotor. With well-known feed pipes, variations of axial thrust of the exhaust gases entering the turbine adversely affect the efficiency. In order to improve the efficiency, half of the cylinders of the engine have the first exhaust gas pipe and the other half of the cylinders have the second exhaust gas pipe connected to them. Further, the first exhaust gas pipe is connected to the central of the three outlets of the turbine case, and the second exhaust gas pipe is connected by two pipes to the two outer of the three outputs of the turbine case.

130

Process engineering aspects of coal grinding/drying plants of explosion-resistant design with pressure relief  

The coal grinding and drying plant of the Alsen-Breitenburg cement works is briefly described. The reasons that prompted the construction of this plant are outlined. Design details are highlighted in examples. Besides taking a look at some of the problems associated with size reduction and drying, the article deals with temperature conditions and the relation between dew-point and oxygen content in the exhaust gas in greater detail. Finally, some process, engineering relationships are indicated in qualitative form.

131

Energy valorization of fatty wastes into biofuels; Valorisation energetique de dechets graisseux en biocarburant  

Biofuels are coming up as an ecological alternative solution to fossil fuels. This article describes an emulsification method which allows to transform an animal fat into a biofuel for the supply of a cogeneration diesel engine: formation of the emulsion (material and method, wetting agent, co-wetting agent, rotation speed); combustion of emulsions (micro-explosion effect, influence of water content); experimental results (energy efficiency, exhaust gas temperature, pollutant emissions (smokes, nitrogen oxides)). (J.S.)

132

Investigations of combustion processes by means of statistical test programs  

Romanian laboratory tests on a radiant burner involved setting up a statistical program that included as independent variables the methane content of the fuel, the ratio between the measured and the theoretical air requirements, and the exhaust gas temperature. The combustion and thermal efficiency were considered dependent variables. The procedure is useful for investigating multiple variables simultaneously and testing gases with compositions differing from the ones recommended by the STAS Romanian standards.

133

Advanced combustion technologies for gas turbine power plants  

Objectives are to develop actuators for enhancing the mixing between gas streams, increase combustion stability, and develop hgih-temperature materials for actuators and sensors in combustors. Turbulent kinetic energy maps of an excited jet with co-flow in a cavity with a partially closed exhaust end are given with and without a longitudinal or a transverse acoustic field. Dielectric constants and piezoelectric coefficients were determined for Sr{sub 2}(Nb{sub x}Ta{sub 1-x}){sub 2}O{sub 7} ceramics.

134

A COOLED-TUBE PYROMETER WITH EXPERIMENTAL RESULTS OBTAINED IN A HIGH- TEMPERATURE GAS STREAM  

An immersion-type pyrometer is described whose primary sensing element is a cylindrical tube in cross flow. The heat-transfer rate to this unit is determined by measurement of the flow rate and temperature rise of a coolant passing through the tube. The heat-transfer rate can then be related to free- stream temperature, after determination of a constant of proportionality by calibration against a reference pyrometer at some convenient lower temperature. Experimental data were obtained in a subsonic exhaust-gas stream over a pressure range of 2/3 to 11/2 atmospheres and a temperature range of 1600 to 4400 deg R. (auth)

135

Exhaust gas recirculation in a homogeneous charge compression ignition engine  

A homogeneous charge compression ignition engine operates by injecting liquid fuel directly in a combustion chamber, and mixing the fuel with recirculated exhaust and fresh air through an auto ignition condition of the fuel. The engine includes at least one turbocharger for extracting energy from the engine exhaust and using that energy to boost intake pressure of recirculated exhaust gas and fresh air. Elevated proportions of exhaust gas recirculated to the engine are attained by throttling the fresh air inlet supply. These elevated exhaust gas recirculation rates allow the HCCI engine to be operated at higher speeds and loads rendering the HCCI engine a more viable alternative to a conventional diesel engine.

136

Test of noise reduction in an internal combustion engine by the use of a light-weight and anti-corrosion muffler (Part 2). Heat-resistant epoxide resin muffler for a 1. 5-L gasoline engine  

In order to reduce exhaust gas noise of a four-stroke gasoline engine, a light-weight muffler made of heat-resistant epoxide resine, instead of steel, has been tested, setting at the outlet of a 1.5 liter gasoline engine exhaust system. The noise level of the exhaust gas was measured and analyzed by a standard noise meter and a FET analyzer. The inside surface of the muffler was coated with stainless steel or ceramic paper. The three-dimensional bridge formation heat resistant epoxide resin, which was developed in this study, releases the elastic constraint between molecular chained segments at a temperature of glass transition point. Subsequently, a noise absorbability of the epoxide resin is displayed absorbing a noise energy of gas flow by a resonance. Increasing a temperature higher than glass transition point reduce noise absorbability, eliminating oscillation system with a linear viscous damping characteristics. As an experimental result, increasing a surface temperature of the outside of the muffler higher than 400K, noiseabsorbability was disappeared. 2 references, 9 figures, 1 table.

137

Vehicle exhaust gas chemical sensors using acoustic wave resonators  

Under Sandia`s Laboratory Directed Research and Development (LDRD) program, novel acoustic wave-based sensors were explored for detecting gaseous chemical species in vehicle exhaust streams. The need exists for on-line, real-time monitors to continuously analyze the toxic exhaust gases -- nitrogen oxides (NOx), carbon monoxide (CO), and hydrocarbons (HC) -- for determining catalytic converter efficiency, documenting compliance to emission regulations, and optimizing engine performance through feedback control. In this project, the authors adapted existing acoustic wave chemical sensor technology to the high temperature environment and investigated new robust sensor materials for improving gas detection sensitivity and selectivity. This report describes one new sensor that has potential use as an exhaust stream residual hydrocarbon monitor. The sensor consists of a thickness shear mode (TSM) quartz resonator coated with a thin mesoporous silica layer ion-exchanged with palladium ions. When operated at temperatures above 300 C, the high surface area film catalyzes the combustion of the hydrocarbon vapors in the presence of oxygen. The sensor acts as a calorimeter as the exothermic reaction slightly increases the temperature, stressing the sensor surface, and producing a measurable deviation in the resonator frequency. Sensitivities as high as 0.44 (ppm-{Delta}f) and (ppm-gas) have been measured for propylene gas, with minimum detectable signals of < 50 ppm of propylene at 500 C.

138

Burned Gas Characteristics of Laminar Lifted Flame at the Beginning of Stream Heating  

This research experimentally investigates the exhaust gas characteristics of a methane-air lifted-jet flame with elevated stream temperatures up to 450 K. Emission indices of NOx and CO were measured by direct gas sampling using a gas detector tube. The index of NOx decreased or did not change with increasing stream temperature up to 350 K, and then increased with further temperature increases. The index of CO changed in an opposite manner to that of NOx with increasing stream temperature. These tendencies demonstrated that the generation of emission gases did not monotonically increase with stream temperature. These non-monotonic properties of the emission indices were caused by particular variations in the lift-off height of flame and flame length. In order to examine these flame characteristics, we measured the flame curvature with OH-PLIF and related it to the lift-off height of triple flame. These flame properties could explain the unique emission characteristics of a lifted-jet flame with stream heating.   

139

Method of hybrid plume plasma propulsion  

A technique for producing thrust by generating a hybrid plume plasma exhaust is disclosed. A plasma flow is generated and introduced into a nozzle which features one or more inlets positioned to direct a flow of neutral gas about the interior of the nozzle. When such a neutral gas flow is combined with the plasma flow within the nozzle, a hybrid plume is constructed including a flow of hot plasma along the center of the nozzle surrounded by a generally annular flow of neutral gas, with an annular transition region between the pure plasma and the neutral gas. The temperature of the outer gas layer is below that of the pure plasma and generally separates the pure plasma from the interior surfaces of the nozzle. The neutral gas flow both insulates the nozzle walls from the high temperatures of the plasma flow and adds to the mass flow rate of the hybrid exhaust. The rate of flow of neutral gas into the interior of the nozzle may be selectively adjusted to control the thrust and specific impulse of the device.

140

Estimation of energy conservation benefits in excess air controlled gas-fired systems  

The most significant energy consumers in energy related industries are boilers and other gas-fired systems. Combustion efficiency term commonly used for boilers and other fired systems and the information on either carbon dioxide (CO2) or oxygen (O2) in the exhaust gas can be used. The aim of this study is to develop a simple-to-use predictive tool which is easier than the existing approaches less complicated with fewer computations and suitable for combustion engineers for predicting the natural gas combustion efficiency as a function of excess air fraction and stack temperature rise (the difference between the flue gas temperature and the combustion air inlet temperature). The results of the proposed predictive tool can be used in follow-up calculations to determine relative operating ef...

 
 
 
 
141

Exhaust purification with on-board ammonia production  

A power source is provided for use with selective catalytic reduction systems for exhaust-gas purification. The power source includes a first cylinder group with a first air-intake passage and a first exhaust passage, and a second cylinder group with a second air-intake passage and a second exhaust passage. The second air-intake passage is fluidly isolated from the first air-intake passage. A fuel-supply device may be configured to supply fuel into the first exhaust passage, and a catalyst may be disposed downstream of the fuel-supply device to convert at least a portion of the exhaust stream in the first exhaust passage into ammonia.

142

Mine-fire diagnostics and implementation of water injection with fume exhaustion at Renton, PA. Rept. of Investigations/1991  

U.S. Bureau of Mines research to develop diagnostic methods to locate and evaluate fires in abandoned mines and waste banks and techniques to extinguish such fires was applied to an abandoned 60-acre underground bituminous coal mine (Renton, Allegheny County, PA) to locate and extinguish three separated fire zones. Mine fire diagnostics interpret changes from baseline values in subsurface pressures, temperatures and mine gas composition under imposed pressure gradients induced by a borehole exhaust fan. The effective gas-sampling area surrounding each borehole is greatly enlarged. Sampling iterations, using a communicating boreholes set, provide fire signature information for locating both heated and cold areas. Time-dependent monitoring differentiates heating and cooling periods resulting from combustion front movement and/or fire extinguishment activities. A water injection with fume exhaustion extinguishment effort involved injecting water through boreholes to quench the heated zones while exhaust fans actively removed heated gases from the mine. The technique was ineffective as implemented, primarily because of inadequate spreading of water from the injection points. The Bureau's diagnostic method determined the fire locations and the effectiveness of the water injection with fume exhaustion extinguishment technique.

143

Exhaust Heat Recirculation System for Fuel Economy Improvement  

This paper introduces an automotive exhaust heat recirculation system. This system was developed to improve fuel economy after cold starts in the winter. The warm-up speed of the engine and heater performance can be improved by recovering exhaust heat from exhaust gas to the engine coolant. As a result, the actual fuel economy is improved due to earlier engine stops in hybrid vehicles.   

144

Rational use of gas in the household. Proceedings. Rationelle Gasanwendung im haeuslichen Bereich. Referate  

At the specialists' meeting in Kaiserslautern on June 21, 1985 under the heading 'The rational use of gas in the household', the following papers were presented: Operating gas burners in airtight dwellings - working aids for the planning, installation and operation of gas burners; new developments in the conventional technology of heat generators in heating systems; hot water heating with gas; new heating - the first step in energy economy; gas cookers in modern kitchens; the L.A.S. - (air, exhaust, chimneys) system, a new way for decentralised heating without indoor air; energy saving by means of fuel-value boilers and flue gas conduction with low temperature flue gases from the chimney sweep's point of view. For each of the papers a separate summary of contents has been made. (BR).

145

High load operation in a homogeneous charge compression ignition engine  

A homogeneous charge compression ignition engine is set up by first identifying combinations of compression ratio and exhaust gas percentages for each speed and load across the engines operating range. These identified ratios and exhaust gas percentages can then be converted into geometric compression ratio controller settings and exhaust gas recirculation rate controller settings that are mapped against speed and load, and made available to the electronic

146

77 FR 14010 - Millennium Pipeline Company, LLC; Notice of Availability of the Environmental Assessment for the...  

...and operate a natural gas compressor station in...interconnection with Algonquin Gas Transmission, LLC at...two 6,130-horsepower gas-fired compressor units that would be housed within...and exhaust silencers, turbine lube oil coolers,...

147

Influence of high rates of supplemental cooled EGR on NOx and PM emissions of an automotive HSDI diesel engine using an LP EGR loop  

Previous experimental studies on diesel engine have demonstrated the potential of exhaust gas recirculation (EGR) as an in-cylinder NOx control method. Although an increase in EGR at constant boost pressure (substitution EGR) is accompanied with an increase in particulate matter (PM) emissions in the conventional diesel high-temperature combustion (HTC), the recirculation of exhaust gases supplementary to air inlet gas (supplemental EGR) by increasing the boost pressure has been suggested as a way to reduce NOx emissions while limiting the negative impact of EGR on PM emissions. In the present work, a low-pressure (LP) EGR loop is implemented on a standard 2.0 l automotive high-speed direct injection (HSDI) turbocharged diesel engine to study the influence of high rates of supplemental coo...

148

Start up system for hydrogen generator used with an internal combustion engine  

A hydrogen generator provides hydrogen rich product gases which are mixed with the fuel being supplied to an internal combustion engine for the purpose of enabling a very lean mixture of that fuel to be used, whereby nitrous oxides emitted by the engine are minimized. The hydrogen generator contains a catalyst which must be heated to a pre-determined temperature before it can react properly. To simplify the process of heating up the catalyst at start-up time, either some of the energy produced by the engine such as engine exhaust gas, or electrical energy produced by the engine, or the engine exhaust gas may be used to heat up air which is then used to heat the catalyst.

149

ZIRCONIA-BASED MIXED POTENTIAL CARBON MONOXIDE/HYDROCARBON SENSORS WITH LANTHANUM MAGNESIUM OXIDE, AND TERBIUM-DOPED YTTRIUM STABILIZED ZIRCONIA ELECTRODES  

We have investigated the performance of dual metal oxide electrode mixed potential sensors in an engine-out, dynamometer environment. Sensors were fabricated by sputtering thin films of LaMnO{sub 3} and Tb-doped YSZ onto YSZ electrolyte. Au gauze held onto the metal oxide thin films with Au ink was used for current collection. The exhaust gas from a 4.8L, V8 engine operated in open loop, steady-state mode around stoichiometry at 1500 RPM and 50 Nm. The sensor showed a stable EMF response (with no hysteresis) to varying concentrations of total exhaust gas HC content. The sensor response was measured at 620 and 670 C and shows temperature behavior characteristic of mixed potential-type sensors. The results of these engine-dynamometer tests are encouraging; however, the limitations associated with Au current collection present the biggest impediment to automotive use.

150

Process Analysis and Evaluation of Exergy Loss in Solid Oxide Fuel Cell  

A solid oxide fuel cell (SOFC) is expected to be applied to the distributed energy systems because of its high thermal efficiency and exhaust gas utilization. The exhaust heat from the SOFC can be transferred to the electric power by a gas turbine and the high efficiency power generation can be achieved. In this paper, the local processes in electrodes and electrolyte of unit SOFC are analyzed taking into account the heat conduction, mass diffusion, electrode reactions and transport of electron and oxygen ion. The temperature and concentration distributions in electrodes and electrolyte membrane are investigated. The effects of operating conditions on the cell performance are also shown. Furthermore, the entropy generation and exergy loss of each process are analyzed and the reason for generating the exergy loss in the SOFC is clarified. It is noted that two electrode reactions are responsible for the major exergy loss.   

151

Exhaust gas reforming of gasoline at moderate temperatures  

This paper presents theoretical and experimental results of exhaust gas reforming of gasoline at lower reformer temperatures (650 and 600{sup o}C). The reformed fuel, containing some quantities of hydrogen and carbon monoxide, was fed at a constant rate to the intake manifold of a single cylinder Ricardo E6 engine as an additive to gasoline. The study of the effects of reformed gas addition on engine performance at extreme lean burn conditions was performed at fixed conditions of speed, load and throttle setting, for different ignition timing settings. Results are encouraging in terms of improved engine deficiency and extended lean burn operation for most ignition timings, despite quite low hydrogen content in the reformed fuel which resulted in low proportions of energy input to the engine from the reformed fuel. Also the levels of pollutant exhaust contents (NO{sub x} and HC) were lower and cycle-to-cycle variations of cylinder pressure was reduced. (author)

152

Development of refining control system in combined blowing converter based on exhaust gas information. Hai gas joho wo riyoshita tenro suiren no keisanki seigyo gijutsu no kaihatsu  

A mass spectrometer was employed for analyzing the exhaust gas at the No.2 BOF shop at the NKK Fukuyama Works. The level-up of refining by using the computer control system for obtaning the exhaust gas information was achieved. Consequently, the continuous estimations of bath temperature, (T. Fe) and reactions of oxidation and decarburization were enabled. It was shown that the accuracy of end point control can be much improved. In addition, rationalizing such as reductions of flux and steel making time was achieved. Especially, the productivity was remarkably improved by this computer control system, and the production amount reached to 330,000t month under one vessel operation with two vessels. Thus, it was demonstrated that the present method would play an important role in the increasing efficiency of converter operation. 9 refs., 18 figs., 2 tabs.

153

Influence of fuel on the particle emission of Diesel engines. Der Kraftstoffeinfluss auf die Partikelemission von Dieselmotoren  

Regarding gaseous exhaust gas components the diesel engine represents the most advantageous combustion engine. Although, the high degree of emission of particles consisting of soot, with attached hydrocarbons sulfates and being in part considered to be mutagenic, remains. The influence of the quality of diesel fuel upon the emission of particles from Heavy Duty-diesel engines, is being investigated. In the low level load range, distinct HC-particle and PAH-emissions have been found to increase with decreasing cetane numbers. Cold start tests have indicated that with decreasing cetane numbers the starting and cold run behaviour of diesel engines is definitely impeded. When, by means of ignition-improver, the cetane number is increased, the achieved improvement of the cold start is (in part) not as high as one would expect from the higher cetane number. When exhaust gas temperatures become as high as above approx. 200deg C, oxidizing catalysts contribute to a distinct reduction of the hydrocarbons that are attached to the soot and thus, to the emission of particles. The influence of the sulphate, being contained in the fuel, upon the sulphate emission in the application (employment) of the oxidizing catalyst at high exhaust gas temperatures, will be discussed (in a graph/diagram). (orig./HW).

154

Compression ratio effect on methane HCCI combustion  

We have used the HCT (Hydrodynamics, Chemistry and Transport) chemical kinetics code to simulate HCCI (homogeneous charge compression ignition) combustion of methane-air mixtures. HCT is applied to explore the ignition timing, bum duration, NOx production, gross indicated efficiency and gross IMEP of a supercharged engine (3 atm. Intake pressure) with 14:1, 16:l and 18:1 compression ratios at 1200 rpm. HCT has been modified to incorporate the effect of heat transfer and to calculate the temperature that results from mixing the recycled exhaust with the fresh mixture. This study uses a single control volume reaction zone that varies as a function of crank angle. The ignition process is controlled by adjusting the intake equivalence ratio and the residual gas trapping (RGT). RGT is internal exhaust gas recirculation which recycles both thermal energy and combustion product species. Adjustment of equivalence ratio and RGT is accomplished by varying the timing of the exhaust valve closure in either 2-stroke or 4-stroke engines. Inlet manifold temperature is held constant at 300 K. Results show that, for each compression ratio, there is a range of operational conditions that show promise of achieving the control necessary to vary power output while keeping indicated efficiency above 50% and NOx levels below 100 ppm. HCT results are also compared with a set of recent experimental data for natural gas.

155

Turbocharger for internal combustion engine, particularly a multi-flow exhaust gas turbocharger for engines and motor vehicles. Turbolader fuer Brennkraftmaschinen, insbesonere mehrflutiger Abgasturbolader fuer Motoren von Kraftfahrzeugen  

The invention is concerned with a multi-flow exhaust gas turbocharger for internal combustion engines of automobiles. The turbocharger is equipped with a radial-turbine wheel, a helical shaped exhaust gas inlet pipe and a system for controlling the turbine operation in relation to the operation conditions of the engine for achieving a optimal performance. If the engine load is high, a partial volume of the exhaust gas flows through a bypass outside the turbine wheel. This bypass channel is located on the case of the turbine, provided with ring slit apertures for the flow connection to the helical exhaust gas inlet.

156

High pressure ceramic air heater for indirectly fired gas turbine applications  

The EFCC cycle is conceptually simple. Air enters the compressor where it is pressurized and becomes the tube-side flow of the ceramic air heater. Heat transferred from the hot combustion gases flowing through the shell-side raises the air temperature to the desired turbine inlet temperature. Internally insulated high pressure piping returns the heated compressor air to the turbine, where it is expanded providing power to drive the electric generator and gas turbine compressor. Exhaust air from the turbine is used as the combustion air for the coal combustor. The EFCC cycle burns pulverized coal in an atmospheric combustion chamber similar to the combustion system in a conventional steam generator. The combustion gas exits the combustor and enters a slag screen, or impact separator, where the larger ash particles are collected to prevent fouling of the heat exchanger. After the slag screen, the combustion gas enters the shell-side of the CerHX where its thermal energy is transferred to the tube side air flow. Shell-side exit temperatures are sufficiently high to provide thermal energy for the bottoming Rankine Cycle through a heat recovery steam generator. Exhaust gas exiting the steam generator passes through a flue gas desulfurization system and a particulate removal system.

157

A GAS TEMPERATURE PROFILE BY INFRARED EMISSION-ABSORPTION SPECTROSCOPY  

This computer program calculates the temperature profile of a flame or hot gas. Emphasis is on profiles found in jet engine or rocket engine exhaust streams containing water vapor or carbon dioxide as radiating gases. The temperature profile is assumed to be axisymmetric with a functional form controlled by two variable parameters. The parameters are calculated using measurements of gas radiation at two wavelengths in the infrared spectrum. Infrared emission and absorption measurements at two or more wavelengths provide a method of determining a gas temperature profile along a path through the gas by using a radiation source and receiver located outside the gas stream being measured. This permits simplified spectral scanning of a jet or rocket engine exhaust stream with the instrumentation outside the exhaust gas stream. This program provides an iterative-cyclic computation in which an initial assumed temperature profile is altered in shape until the computed emission and absorption agree, within specified limits, with the actual instrument measurements of emission and absorption. Temperature determination by experimental measurements of emission and absorption at two or more wavelengths is also provided by this program. Additionally, the program provides a technique for selecting the wavelengths to be used for determining the temperature profiles prior to the beginning of the experiment. By using this program feature, the experimenter has a higher probability of selecting wavelengths which will result in accurate temperature profile measurements. This program provides the user with a technique for determining whether this program will be sufficiently accurate for his particular application, as well as providing a means of finding the solution. The input to the program consists of four types of data: (1) computer program control constants, (2) measurements of gas radiance and transmittance at selected wavelengths, (3) tabulations from the literature of gas transmission parameters at selected wavelengths, and (4) independently determined or estimated profiles of partial pressures of the gas reaction products. The output consists of error figures for the temperature and partial pressure profiles in tabular form. This program is written in FORTRAN IV for execution on an UNIVAC 1100 series computer with a main memory requirement of 21K of 36 bit words. This program was developed in 1977.

158

Study on technologies for isolating and recovering CO2 from boiler exhaust gas; Boiler hai gas karano CO2 bunri kaishu gijutsu ni kansuru kenkyu  

Pressure swing adsorption (PSA) method is used in this report in the investigation of methods for isolating and recovering CO2 from combustion exhaust gas generated by thermoelectric power stations, etc. The PSA method is a process in which the exhaust gas is kept at a specified pressure and flow rate for a certain period of time for specified components to be adsorbed by the adsorbent in the PSA tower, the gas flow is then stopped, and the specified components in the adsorbent are taken out of the tower for isolation and concentration. The product is in the form of gas. Two or more towers should be available so that the process will not be interrupted. The collected gas of concentrates is then subjected to low-temperature separation for conversion into liquids. The off-gas from the low-temperature separator is fed back to the PSA inlet for an improved CO2 recovery rate. In this experiment, a liquefied CO2 concentration of 99% and an overall recovery rate of 90% are achieved. In a tentatively drafted design, a CO2 recovery system for a 700,000kW-level coal-fired thermoelectric power station occupies more than 40,000m{sup 2}. Now that a practical way of disposing of the recovered CO2, for instance, has not yet been established, this technology will demand a great deal of technological development efforts and political breakthroughs before it is put to use. 8 refs., 11 figs., 2 tabs.

159

Effect of temperature and CO2 concentration on laser-induced breakdown spectroscopy measurements of alkali fume.  

Laser-induced breakdown spectroscopy (LIBS) was used in the evaluation of aerosol concentration in the exhaust of an oxygen/natural-gas glass furnace. Experiments showed that for a delay time of 10 {micro}s and a gate width of 50 {micro}s, the presence of CO{sub 2} and changes in gas temperature affect the intensity of both continuum emission and the Na D lines. The intensity increased for the neutral Ca and Mg lines in the presence of 21% CO{sub 2} when compared to 100% N{sub 2}, whereas the intensity of the Mg and Ca ionic lines decreased. An increase in temperature from 300 to 730 K produced an increase in both continuum emission and Na signal. These laboratory measurements were consistent with measurements in the glass furnace exhaust. Time-resolved analysis of the spark radiation suggested that differences in continuum radiation resulting from changes in bath composition are only apparent at long delay times. The changes in the intensity of ionic and neutral lines in the presence of CO{sub 2} are believed to result from higher free electron number density caused by lower ionization energies of species formed during the spark decay process in the presence of CO{sub 2}. For the high Na concentration observed in the glass furnace exhaust, self-absorption of the spark radiation occurred. Power law regression was used to fit laboratory Na LIBS calibration data for sodium loadings, gas temperatures, and a CO{sub 2} content representative of the furnace exhaust. Improvement of the LIBS measurement in this environment may be possible by evaluation of Na lines with weaker emission and through the use of shorter gate delay times.

160

Effect of temperature and CO{sub 2} concentration on laser-induced breakdown spectroscopy measurements of alkali fume  

Laser-induced breakdown spectroscopy (LIBS) was used in the evaluation of aerosol concentration in the exhaust of an oxygen/natural-gas glass furnace. Experiments showed that for a delay time of 10 {mu}s and a gate width of 50 {mu}s, the presence of CO{sub 2} and changes in gas temperature affect the intensity of both continuum emission and the Na D lines. The intensity increased for the neutral Ca and Mg lines in the presence of 21% CO{sub 2} when compared to 100% N{sub 2}, whereas the intensity of the Mg and Ca ionic lines decreased. An increase in temperature from 300 to 730 K produced an increase in both continuum emission and Na signal. These laboratory measurements were consistent with measurements in the glass furnace exhaust. Time-resolved analysis of the spark radiation suggested that differences in continuum radiation resulting from changes in bath composition are only apparent at long delay times. The changes in the intensity of ionic and neutral lines in the presence of CO{sub 2} are believed to result from higher free electron number density caused by lower ionization energies of species formed during the spark decay process in the presence of CO{sub 2}. For the high Na concentration observed in the glass furnace exhaust, self-absorption of the spark radiation occurred. Power law regression was used to fit laboratory Na LIBS calibration data for sodium loadings, gas temperatures, and a CO{sub 2} content representative of the furnace exhaust. Improvement of the LIBS measurement in this environment may be possible by evaluation of Na lines with weaker emission and through the use of shorter gate delay times.

 
 
 
 
161

Performance responsive muffler for internal combustion engines  

This patent describes an engine muffler responsive to exhaust flow rate for an internal combustion engine. It comprises: a body forming an internal expansion chamber and having an inlet port and an exhaust port spaced apart from one another, to receive and to discharge exhaust gas stream, respectively, and a variable restrictor downstream from the inlet port and upstream from the outlet port, through which the exhaust gas stream must flow to reach the exhaust port. The variable restrictor including a valving element whose operative position can variably occlude the gas stream flow as a function of engine exhaust flow rate. Wherein the variable restrictor is formed with a solid wall disposed about the valving element to define a constricting annular passageway having a cross section that varies with distance from the inlet port and from the exhaust port.

162

An experimental study on the effects of exhaust gas on spruce (Picea abies L. Karst.)  

Motor vehicle exhausts are significant contributors to air pollution. Besides fine particles and inorganic gases, like CO, SO{sub 2} and NO{sub x}, exhaust gas contains a large group of aromatic hydrocarbon compounds, many of which are phytotoxic. In field studies, exhausts are found to have both direct and indirect harmful effects on roadside plants. However, only few experimental studies have been made about the effects of exhaust gas emissions on coniferous trees. The aim of this study was to survey the effects of exhausts on spruce (Picea abies L. Karst.) in standardized conditions. The concentrations of major exhaust gas components in the chamber atmosphere were detected simultaneously. The effects of exhaust on epistomatal waxes of first-year spruce needles are described. (author)

163

Method and apparatus for detection of catalyst failure on-board a motor vehicle using a dual oxygen sensor and an algorithm  

Apparatus is described for detecting motor vehicle exhaust gas catalytic converter deterioration comprising a first exhaust gas oxygen sensor adapted for communication with an exhaust stream before passage of the exhaust stream through a catalytic converter and a second exhaust gas oxygen sensor adapted for communication with the exhaust stream after passage of the exhaust stream through the catalytic converter, an on-board vehicle computational means, said computational means adapted to accept oxygen content signals from the before and after catalytic converter oxygen sensors and adapted to generate signal threshold values, said computational means adapted to compare over repeated time intervals the oxygen content signals to the signal threshold values and to store the output of the compared oxygen content signals, and in response after a specified number of time intervals for a specified mode of motor vehicle operation to determine and indicate a level of catalyst deterioration.

164

Exhaust catalyst selection for small two-stroke engines  

A laboratory test has been used to evaluate the behavior of different oxidation catalyst formulations for conventional two-stroke engines. The test gas composition was as close as possible to the real exhaust gas composition with respect to its hydrocarbon and oxygen contents. Small size catalyst samples were located inside a quartz tube and heated by an electric furnace. Several wash-coat types and noble metal formulations applied on metallic substrates were compared. Determinations included light-off temperature and pollutant conversion rates. It was generally observed that the most active catalysts for hydrocarbon elimination produced the highest amount of CO at temperatures between 350 and 500 C. This was due to the substoichiometric oxygen content of the simulated exhaust gas. Some tests were then performed to evaluate the possibility of converting the CO produced, back to CO{sub 2} and H{sub 2}, by the water gas-shift reaction. CO conversion rates were determined using two different catalysts in series, with the second being at a lower temperature than the first one. Several formulations were compared for the second catalyst bed with an offset of temperature between the two beds of about 300 C.

165

Wood chip stoker and furnace for curing tobacco  

The system, retrofitted to an existing bulk curing barn, successfully cured tobacco and required about the same amount of fuel energy input as oil or gas fired barns. Fire box temperatures were in the 900C (1600F) range and no difficulty was experienced in burning fresh (43% moisture) chips. The exhaust was clear and no cresote deposits were found, but because of the large amount of excess combustion air, overall efficiency was not as high as expected. At present prices, wood chips are a significantly cheaper fuel than gas or oil.

166

Hot gas environment around STOVL aircraft in ground proximity. II - Numerical study  

Ingestion of hot exhaust gases by the engines of STOVL aircraft has been an important research problem for several years. The hot gas environment around STOVL aircraft is three-dimensional and turbulent. In this study, the Navier-Stokes equations governing the hot gas ingestion flowfield are solved by an efficient finite-difference calculation procedure. The complete geometry including the head wind and the fuselage is simulated. Four demonstration calculations with variations in the height of the fuselage and the head wind velocity are presented. It is shown that the calculation procedure efficiently provides a solution to the governing equations and produces realistic descriptions of the flow and temperature fields.

167

Catalysts for lean burn engine exhaust abatement  

The present invention provides a process for catalytically reducing nitrogen oxides in an exhaust gas stream containing nitrogen oxides and a reductant material by contacting the gas stream under conditions effective to catalytically reduce the nitrogen oxides with a catalyst comprising a aluminum-silicate type material and a minor amount of a metal, the catalyst characterized as having sufficient catalytic activity so as to reduce the nitrogen oxides by at least 60 percent under temperatures within the range of from about 200.degree. C. to about 400.degree. C.

168

Development of after-burner for cogeneration. Co-generation yo oitaki burner no kaihatsu  

Concerning after-burnner in cogeneration system for increasing steam generation and for energy saving, by heating high temperature exhaust gas of gas turbine, its development was achieved. As the targets of the development, domestic production for maintenance, low cost, low NOx, were stated. System and structure of burnner were introduced by figures. An equation for estimating the amount of generated NOx was introduced to obtain correlation with load of burnner. In addition, outline of standard specifications were explained. Operating conditions for pertinent burnning were shown by graph, and improvement of boiler efficiency and total efficiency were explained. 6 figs.

169

Parametric study on particle size and SOF effects on EGR cooler fouling  

Recent diesel engine technologies, developed for enhanced regulation of exhaust emissions, are characterized by high exhaust gas recirculation (EGR) rates and high-pressure fuel injection. The use of high EGR rates, by which high temperatures can be avoided in a cylinder, is an effective method for reduction of nitrogen oxide (NO x ) emissions. High-pressure fuel injection leads to smaller soot particles, which decreases mass-based soot emission. These technologies, however, also have effects on particulate matter (PM) characteristics that are closely related to EGR cooler fouling. High-pressure fuel injection, which makes smaller soot particles, increases the concentration of soot particles, and a high EGR rate, which lowers the temperature in the cylinder, increases the soluble organic fraction (SOF). In this study, we evaluated the effects of these changes in PM characteristics on EGR cooler fouling. Instead of an engine-based experiment, in which a parametric study is nearly impossible, a laboratory experiment was performed to separate variables. A soot generator was used to make model exhaust gas because the variables could be controlled separately (e.g., mean particle size and concentration of soot particles) and this improved the reproducibility of the experiments. Additionally, n-dodecane, a model compound representing diesel fuel, was vaporized and injected into the exhaust gas to test the effects of SOF on cooler fouling. For particle sizes ranging from 41 to 190 nm in diameter, the deposition fraction was inversely proportional to particle size. Thus, smaller soot particles in the exhaust gas were more likely to cause formation of thermophoretic deposits on the wall of the EGR cooler. At an EGR gas temperature of 350 °C, the deposition fraction was greatest (84%) for the smallest particle size of 41 nm, whereas the deposition fraction was least (7%) for the largest particle size, 190 nm. The performance degradation of the EGR cooler showed a similar trend to the measured deposit mass. As coolant temperature decreased, the effect of n-dodecane injection on the growth of PM deposits increased, which significantly reduced the overall thermal conductivity of the EGR cooler. This result showed that 'wet soot' caused greater contamination of the EGR cooler.

170

Transient experiments on a full-scale DOC-Methodology and techniques to support modelling  

A methodology was developed, which enables transient experiments to be performed on a DOC connected to a live diesel engine, while the temperature of the DOC substrate is monitored at various locations. This was demonstrated on a full-scale Pt/g-alumina DOC (o.d.=106mm; length=114mm), connected to a Ford 2.0L diesel engine. The engine was operated at a constant speed of 2000rpm, and by varying the engine torque, experiments were performed at fixed gas inlet temperatures to the DOC, e.g. 150, 320^oC, and at each setting a constant background level of exhaust emissions was obtained. Then, a known quantity of pollutant (e.g. CO, propane) was injected into the exhaust, so as to create an approximated pulse input into the DOC (e.g. with peak CO concentration=3000ppm). The transient response of ...

171

Regeneration of DPF at low temperatures with the use of a cerium based fuel additive  

A light duty truck with a naturally aspirated engine was equipped with a DPF (changing the exhaust pipe and eliminating the muffler) and operated on fuel doped with a cerium based additive in various concentrations. Tests were carried out on chassis dynamometer using the European urban cycle, but also under city driving conditions with maximum speeds up to 50 km/h and exhaust gas temperature up to 300 C. Under these conditions, it was observed that filter regeneration was always possible at relatively high particulate accumulation in the filter, while the effect on fuel consumption (as measured over the emission test cycles) was not detectable, compared to baseline data of the vehicle. Change in driving conditions from slow urban to highway with highly loaded trap led to spontaneous trap regeneration at higher temperatures, without effect on fuel consumption. This paper documents the operation of a fully passive DPF system for diesel light duty vehicles.

172

Comparative combustion characteristics of gasoline and hydrogen fuelled ICEs  

In this paper, some models of comparative combustion characteristics for gasoline and hydrogen fuelled spark ignition internal combustion engines were developed and discussed from a thermodynamic and heat transfer perspective. The geometry used was that of a 3.4L GM V6 engine with a compression ratio of 9.5:1. Models for mass fraction burned, pressure, temperature, and gas speed were developed according to the literature survey and graphed over the cycle range. Furthermore, Pressure-Volume and Temperature-Entropy models were developed for both gasoline and hydrogen fuelled engines. Analysis of these models indicated approximately a 6.42% increase thermal efficiency for the hydrogen fuelled engine due to less exhaust blow down, less heat rejection during the exhaust stroke, and its shorter ...

173

Modeling and Simulation of Coke Combustion Regeneration for Coked Cr2O3/Al2O3 Propane Dehydrogenation Catalyst  

A heterogeneous model is developed for the regeneration of the Cr2O3/Al2O3 catalyst for the propane dehydrogenation process by considering the internal mass transfer and external mass/heat transfer during the coke combustion. Simulation shows that under practical operating conditions, multi-steady states exist for the catalyst pellets and the catalyst temperature is sensitive to gas temperature. However, at increased mass flow rate or lowered oxygen concentration, multi-steady states will not appear. Under the strong influences of film diffusion, the coke in the packed bed reactor will first be exhausted at the inlet, while if the film diffusion resistance is decreased, the position of first coke exhaustion moves toward the outlet of the reactor.

174

Diesel engine exhaust gas recirculation system with greater atmospheric pressure compensation at low engine load  

An exhaust gas recirculation system is described for a diesel engine for a vehicle utilizing an air intake system and an exhaust system including: (a) an exhaust gas recirculation passage a downstream and of which is connected to the exhaust system and an upstream end of which is connected to the air intake system, so as to recirculate exhaust gas from the exhaust system to the air intake system; (b) an exhaust gas recirculation control valve comprising a pressure chamber, which regulates flow resistance of the exhaust gas recirculation passage according to an amount by which the pressure in the pressure chamber is lower than ambient atmospheric pressure, so as to regulate a flow amount of the recirculation of exhaust gas from the exhaust system to the air intake system; (c) means for providing a supply of low pressure; (d) an absolute pressure control valve, comprising an input port and an output port, which receives supply of low pressure from the means for providing low pressure at the input port, and which provides a supply of a pressure at the output port an absolute pressure valve of which is substantially fixed; and (e) a vacuum control valve comprising a pressure regulating chamber receives a supply of pressure from the output port of the absolute pressure control valve.

175

Coal gasification system using high temperature gasifier; Koon gas ro ni yoru sekitan gas ka sochi  

This invention relates to the coal gasification system, wherein coal and superheated steam are supplied to a steam gasifier which utilizes high temperature helium of the high temperature gasifier, which is a graphite-moderated helium cooling reactor, to produce coal gasified gas by steam gasification reaction. This coal gasifier system employs the primary helium gas and the secondary helium gas as media, and is structured by combining a steam gasifier, which utilizes the heat of the high temperature gasifier fully, with a partial oxidation gasifier, which requires no outside heat input and is independent thermally by the use of calorie of the fuel itself. In this structure, unreacted char exhausted from the steam gasifier is recovered by the cyclone which is supplied to the juxtaposed partial oxidation gasifier for re-gasification, and high coal gasification efficiency can be attained as the whole coal gasification system utilizing the heat of graphite moderated helium cooling reactor. 4 figs.

176

Effects of Porosity and Temperature on Oxidation Behavior in Air of Selected Nuclear Graphites  

Nuclear graphite endures gas oxidation in High Temperature Gas-cooled Reactor (HTGR), which may threaten the safety of reactor. To study the oxidation behavior of nuclear graphite, weight loss curve is usually measured through Thermo Gravimetric Analysis (TGA) method. In this work, three brands of nuclear graphite for HTGR (i.e., HSM-SC, IG-11, and NBG-18) are oxidized under 873 and 1073 K in open air, and their weight loss curves are obtained. The acceleration of oxidizing rate is observed for both HSM-SC and IG-11, and is attributed to the large porosity increase during oxidation process. For HSM-SC, the porosity increase comes from preferential binder oxidation, and thus its binder quality shall be improved to obtain better oxidation resistance. Temperature effects on oxidation for HSM-SC are also studied, which shows that oxidizing gas tends to be exhausted at graphite surface at high temperature instead of penetrate into the interior of bulk.   

177

Performance analysis of a trigeneration system based on a micro gas turbine and an air-cooled, indirect fired, ammonia-water absorption chiller  

The objective of this paper is to experimentally determine the efficiency and viability of the performance of an advanced trigeneration system that consists of a micro gas turbine in which the exhaust gases heat hot thermal oil to produce cooling with an air cooled absorption chiller and hot water for heating and DHW. The micro gas turbine with a net power of 28kW produces around 60kW of heat to drive an ammonia/water air-cooled absorption chiller with a rated capacity of 17kW. The trigeneration system was tested in different operating conditions by varying the output power of the micro gas turbine, the ambient temperature for the absorption unit, the chilled water outlet temperature and the thermal oil inlet temperature. The modelling performance of the trigeneration system and the electr...

178

Electrochemical separation of hydrogen from reformate using PEM fuel cell technology  

This article is an examination of the feasibility of electrochemically separating hydrogen obtained by steam reforming a hydrocarbon or alcohol source. A potential advantage of this process is that the carbon dioxide rich exhaust stream should be able to be captured and stored thereby reducing greenhouse gas emissions. Results are presented for the performance of the anode of proton exchange membrane (PEM) electrochemical cell for the separation of hydrogen from a H2-CO2 gas mixture and from a H2-CO2-CO gas mixture. Experiments were carried out using a single cell state-of-the-art PEM fuel cell. The anode was fed with either a H2-CO2 gas mixture or a H2-CO2-CO gas mixture and hydrogen was evolved at the cathode. All experiments were performed at room temperature and atmospheric pressure. W...

179

Study on incineration technology of oil gas generated during the recovery process of oil spill  

The objective of this study is to design, set up and operate an incinerator system capable of providing clean exhaust and safety control for burning oil gas generated during the recovery process of oil spill in Taiwan. In this study, we successfully develop a vertical-type incinerator, which consists of five oil gas burners with entrained primary air, a pilot burner, and an auxiliary burner. The incinerator system is equipped with necessary control units in order to achieve safe, easy, fast, and efficient operation. Flame appearance, flue gas temperature and CO emission of the incinerator system for burning oil gas are reported and discussed. Under the long-term operation, it is found that the new designed incinerator is satisfactory for burning oil gas with low supply pressure at various ...

180

Numerical Study of Stratified Charge Combustion in Wave Rotors  

A wave rotor may be used as a pressure-gain combustor effecting non-steady flow, and intermittent, confined combustion to enhance gas turbine engine performance. It will be more compact and probably lighter than an equivalent pressure-exchange wave rotor, yet will have similar thermodynamic and mechanical characteristics. Because the allowable turbine blade temperature limits overall fuel/air ratio to sub-flammable values, premixed stratification techniques are necessary to burn hydrocarbon fuels in small engines with compressor discharge temperature well below autoignition conditions. One-dimensional, unsteady numerical simulations of stratified-charge combustion are performed using an eddy-diffusivity turbulence model and a simple reaction model incorporating a flammability limit temperature. For good combustion efficiency, a stratification strategy is developed which concentrates fuel at the leading and trailing edges of the inlet port. Rotor and exhaust temperature profiles and performance predictions are presented at three representative operating conditions of the engine: full design load, 40% load, and idle. The results indicate that peak local gas temperatures will result in excessive temperatures within the rotor housing unless additional cooling methods are used. The rotor itself will have acceptable temperatures, but the pattern factor presented to the turbine may be of concern, depending on exhaust duct design and duct-rotor interaction.

 
 
 
 
181

On use of CO{sub 2} chemiluminescence for combustion metrics in natural gas fired reciprocating engines.  

Flame chemiluminescence is widely acknowledged to be an indicator of heat release rate in premixed turbulent flames that are representative of gas turbine combustion. Though heat release rate is an important metric for evaluating combustion strategies in reciprocating engine systems, its correlation with flame chemiluminescence is not well studied. To address this gap an experimental study was carried out in a single-cylinder natural gas fired reciprocating engine that could simulate turbocharged conditions with exhaust gas recirculation. Crank angle resolved spectra (266-795 nm) of flame luminosity were measured for various operational conditions by varying the ignition timing for MBT conditions and by holding the speed at 1800 rpm and Brake Mean effective Pressure (BMEP) at 12 bar. The effect of dilution on CO*{sub 2}chemiluminescence intensities was studied, by varying the global equivalence ratio (0.6-1.0) and by varying the exhaust gas recirculation rate. It was attempted to relate the measured chemiluminescence intensities to thermodynamic metrics of importance to engine research -- in-cylinder bulk gas temperature and heat release rate (HRR) calculated from measured cylinder pressure signals. The peak of the measured CO*{sub 2} chemiluminescence intensities coincided with peak pressures within {+-}2 CAD for all test conditions. For each combustion cycle, the peaks of heat release rate, spectral intensity and temperature occurred in that sequence, well separated temporally. The peak heat release rates preceded the peak chemiluminescent emissions by 3.8-9.5 CAD, whereas the peak temperatures trailed by 5.8-15.6 CAD. Such a temporal separation precludes correlations on a crank-angle resolved basis. However, the peak cycle heat release rates and to a lesser extent the peak cycle temperatures correlated well with the chemiluminescent emission from CO*{sub 2}. Such observations point towards the potential use of flame chemiluminescence to monitor peak bulk gas temperatures as well as peak heat release rates in natural gas fired reciprocating engines.

182

High efficiency carbonate fuel cell/turbine hybrid power cycles  

Carbonate fuel cells developed by Energy Research Corporation, in commercial 2.85 MW size, have an efficiency of 57.9 percent. Studies of higher efficiency hybrid power cycles were conducted in cooperation with METC to identify an economically competitive system with an efficiency in excess of 65 percent. A hybrid power cycle was identified that includes a direct carbonate fuel cell, a gas turbine and a steam cycle, which generates power at a LHV efficiency in excess of 70 percent. This new system is called a Tandem Technology Cycle (TTC). In a TTC operating on natural gas fuel, 95 percent of the fuel is mixed with recycled fuel cell anode exhaust, providing water for the reforming of the fuel, and flows to a direct carbonate fuel cell system which generates 72 percent of the power. The portion of the fuel cell anode exhaust which is not recycled, is burned and heat is transferred to the compressed air from a gas turbine, raising its temperature to 1800{degrees}F. The stream is then heated to 2000{degrees}F in the gas turbine burner and expands through the turbine generating 13 percent of the power. Half the exhaust from the gas turbine flows to the anode exhaust burner, and the remainder flows to the fuel cell cathodes providing the O{sub 2} and CO{sub 2} needed in the electrochemical reaction. Exhaust from the fuel cells flows to a steam system which includes a heat recovery steam generator and stages steam turbine which generates 15 percent of the TTC system power. Studies of the TTC for 200-MW and 20-MW size plants quantified performance, emissions and cost-of-electricity, and compared the characteristics of the TTC to gas turbine combined cycles. A 200-MW TTC plant has an efficiency of 72.6 percent, and is relatively insensitive to ambient temperature, but requires a heat exchanger capable of 2000{degrees}F. The estimated cost of electricity is 45.8 mills/kWhr which is not competitive with a combined cycle in installations where fuel cost is under $5.8/MMBtu.

183

Design and development test of a gas turbine combustor for air-blow Lurgi coal gas fuel  

A heavy-duty industrial gas turbine combustion system has been designed and laboratory tested for use with low heating value coal gas produced by an air-blown Lurgi coal gasifier. The design fuel has a nominal lower heating value of 4.21 MJ/Nm/sup 3/ (107 BTU/SCF). The combustor design utilizes high-swirl fuel and air injection to provide rapid fuel/air mixing and a stable flame front, and is physically interchangeable with the conventional fuel combustion system for the General Electric Model MS5001 gas turbine. Full-pressure, full-scale tests of the new combustion system have been conducted at the General Electric Gas Turbine Development Laboratory in Schenectady, New York, USA, for the Shanghai Power Plant Equipment Research Institute (SPPERI) of the Peoples Republic of China. Simulated clean low heating value coal gas fuel with a composition specified by SPPERI was used for these tests. Laboratory test reults are presented for important combustor operating parameters, including exhaust emissions, combustion efficiency, exhaust temperature profile, dynamic pressure, and metal temperature distribution.

184

Automobile exhaust gas as a source of aqueous phase OH radical in the atmosphere and its effects on physiological status of pine trees  

Free radical generation potential of automobile exhaust gas was examined by measuring hydroxyl (OH) radical photo-formation rates in exhaust gas-scrubbing water. Effects of automobile exhausts on physiological status of Japanese red pine trees (Pinus densiflora Sieb. et Zucc.) were also investigated to elucidate the mechanism how the free radicals derived from exhaust gas damage higher plants. Gasoline and diesel exhaust gases were scrubbed into pure water. Potential photo-formation rates of OH radical in aqueous phase (normalized to sun light intensity of clear sky midday on May 1 at 34degreeN) for gasoline and diesel cars were ave. 51 and 107mMh-1m-3 of exhaust gas, respectively. Nitrite was a dominant source (ca. 70-90%) of photochemical formation of OH radical in both gasoline and dies...

185

Performance of ferritic stainless steels for automobile muffler corrosion  

Corrosion behavior of ferritic stainless steels was studied in artificial exhaust gas condensates containing corrosive ions such as Cl{sup {minus}} and SO{sub 3}{sup 2{minus}}. Continuous immersion tests in flasks and Dip and Dry tests by using the alternate corrosion tester with a heating system clarified the effects of chromium and molybdenum additions on the corrosion resistance of a ferritic stainless steel in the artificial exhaust gas condensates. Effects of surface oxidation on the corrosion behavior were investigated in a temperature range of 573K to 673K. Oxidation of 673K reduced the corrosion resistance of the ferritic stainless steels in the artificial environment of the automobile muffler. Particulate matter deposited on the muffler inner shell from the automobile exhaust gas was also examined. Deposited particulate matter increased the corrosion rate of the ferritic stainless steel. Finally, the authors also investigated the corrosion of the automobile mufflers made of Type 436L ferritic stainless steel with 18% chromium-1.2% molybdenum after 24 months, in Japan. The sets of results clarified that Type 436L ferritic stainless steel as the material for the automobile muffler exhibited acceptable corrosion resistance.

186

Cooling facility for reactor container  

A suction port of a condensator to a condensate pipe is connected to a main steam pipe, a discharge port of a incondensible gas exhaustion pipe is connected from an inlet header of the condensator to a main steam pipe by way of a valve, and an exhaustion port of the incondensible gas exhaustion pipe is connected from an exit header of the condensator to a pressure suppression pool by way of a valve. In addition, a condensate return pipe is connected from the exit header of the condensator to the pressure vessel by way of a value. When the reactor is isolated, steams are flown from the pressure vessel to a condensator by way of a main steam pipe. In this case, since incondensible gas is not present, the flow rate of inflown steams is great, the condensate heat conductivity is great and temperature difference between the inside and the outside of the pipes is great, the amount of heat released out of the container is increased. The value of the condensate return pipe is opened, condensates are injected to the pressure vessel. Upon occurrence of an accident, steams and incondensible gases are mixed and flown from the suction pipe of the condensator into the condensator, and noncondensed steams are discharged to a pressure suppression pool by the pressure difference between the inside of the condensate pipe and the inside of the pressure suppression chamber. (N.H.)

187

Studies on continuous measurement of formaldehyde with second order derivative spectrophotometry. Niji bibun kyuko bunko hoshiki ni yoru formaldehyde renzoku sokuteiho no kaihatsu  

A new method of continuous measurement of formaldehyde has been developed with second order derivative spectrophotometry, in order to establish the measurement device of practical use for exhaust gas out of methanol fueled vehicles. In this device, a suppressing system of flow rate change due to pressure change of exhaust gas during a transient drive and a heating system to uniform temperature distribution of the cell are adopted. Detection limit, responsibility, effect of interference component and et al. are examined and evaluated. For application tests, the steady test and the modal test are carried out by using exhaust gas out of a methanol fueled vehicle (M85). Results obtained by the experimental studies are as follows. Minimum detection limit is 5 ppm. Responsibility is about 5 seconds at 5 l/min in measured flow rate. The measurement of formaldehyde is not interfered by SO{sub 2} or NO{sub 2} when 304.4 nm is used as the wave length for measurement. This method corresponds well with DNPH-GC method and so is highly reliable. 5 refs., 11 figs., 1 tab.

188

Automobile dirty smoke eliminator  

An automobile dirty smoke eliminator is disclosed which mainly consists of two oval tin plates externally, and upper and lower exhaust pipes , left and right support plates, a blade, a discharge chamber, a discharge pipe, etc. internally. The principle of the present invention mainly consists in making use of the effect of mixing water and gas to entirely eliminate automobile dirty smoke. When the dirty smoke (exhaust gas) of automobile enters into the lower exhaust pipe of the present invention, the blade at the outlet of said lower exhaust pipe submerged in water is impacted by the compression force derived from the engine exhaust stroke so as to generate a mixture of said water and exhaust gas and to form a whirlpool having many buddles. The effect of walls of left and right support plates promote the toxin in the said dirty smoke (Exhaust gas) automatically to deposit in the said water. The surplus toxin is discharged through the upper exhaust pipe and then mixed with the water to form a colorless, odorless nontoxious fog-like vapor which exhausts through the discharge pipe in order to achieve the best result of eliminating the said dirty smoke (Exhaust gas).

189

Cogeneration at Hotel New Grand. Hotel New Grand no cogeneration  

This paper introduces a summary of the gas cogeneration installation introduced to Hotel New Grand in Yokohama. The installation is a gas cogeneration system which has advantages in overall efficiency and in environmental preservation. This system is a steam recovering type. The engine cooling water temperature is raised to 120[degree]C, the calorific power of the cooling water is recovered as steam. Steam of 8 kg/cm[sup 2]G is further recovered from the waste gas to raise the efficiency. The gas engine generator generates power of 480 kW, which is linked to a utility power line. Cooling the engine interior using high-temperature water produces saturated steam of 1 kg/cm[sup 2]G in the air-water tank, which is utilized for preheating the hot water supply system. Waste heat from the exhaust gases is recovered in a steam boiler which generates saturated steam of 8 kg/cm[sup 2]G that is utilized for room warming and cooling. Recovery of the exhaust gases raising their temperature up to 150[degree]C, plus recovery of both saturated steams result in a steam recovery rate of 44.8% and an overall efficiency of 77%. 9 figs., 1 tab.

190

Electronically controlled electromagnetic Visco fan clutches for commercial vehicles. Elektronisch geregelte elektromagnetische Visco-Luefterkupplungen fuer Nutzfahrzeuge  

The individual cooling of all the media in a commercial vehicle which require cooling necessitates the use of a fan clutch which is directly controlled by the temperature of these media. With the aid of such a fan clutch the operating temperature of the engine can be kept constant, the engine power output increased and the amount of exhaust gas as well as its pollutant emissions reduced. With the new electronically controlled and electromagnetically actuated Visco fan clutch individual cooling can now be realized. The clutch, which is currently being developed by Behr, is a 4-stage clutch whose inertia is considerably lower than that of the standard Visco clutch. (orig.)

191

$\\rho$ self energy at finite temperature and density in the real-time formalism  

The $\\rho$ meson self-energy in nuclear matter from baryonic loops is analysed in the real time formulation of field theory at finite temperature and density. The discontinuities across the branch cuts of the self-energy function are evaluated for an exhaustive set of resonances in the loops considering the fully relativistic thermal baryon propagator including anti-baryons. Numerical calculations show a significant broadening of the $\\rho$ spectral function coming from the Landau cut. Adding the contribution from mesonic loops, the full spectral function of the $\\rho$ in a thermal gas of mesons, baryons and antibaryons in equilibrium is evaluated at various values of temperature and baryonic chemical potential.

192

Evaluation of jet-exhaust emission scattering for the aft telescope configuration on SOFIA.  

This report describes the study undertaken at Ames Research Center to evaluate and understand the potential effects of the exhaust plume from the JT9D-7 engines on the SOFIA (Stratospheric Observatory for Infrared Astronomy) aft telescope configuration. Even though the telescope will not look through the plume, the thermal IR from the hot exhaust gas could potentially scatter into the telescope beam and cause an undesirable increase in the IR background. The nature of the signal is described, the results from actual plume measurements are presented, and the straylight calculations are summarized. Exhaust gas abundances and thermodynamic properties were provided by Pratt and Whitney. The IR emissivity of the plume was calculated based on these data. Development of the plume was predicted downstream of the engine, including evolution of the streamlines and mixing and cooling of the gases. Given the considerable amount of modeling involved and the inability to predict the fluctuations in the IR emission, actual IR measurements of the plume of the Shuttle Carrier Aircraft were conducted. The measured temperature profiles, absolute power and fluctuations were close to those anticipated and were used in the final straylight modeling. The emission from the engine tail cone was included in the analysis. The results of the investigation indicate that without taking any remedial action to reconfigure the telescope for improved rejection of the exhaust plume background, the only situations where the exhaust plume would be a problem are at low elevation angles (less than 25 deg) for narrow-band observations near or at water spectral lines around 5-8 microns.

193

The influence of exhaust sound and emission by according to automobile muffler inner shapes  

This study represents effect to attain to the exhaust gas and the exhaust noise by the inner shapes of automobile muffler, and obtained optimization-data for the inner muffler shapes by the temperature variation of the exhaust gas in muffler. The results of noise show to decrease in order of model-1, 2 and 3 under that the engine speed is 3500 R.P.M and similar values beyond it. CO represented good the model-2 at low engine speed and model-1 at high engine speed. The model-3 was show to tiny variation difference by the variables. HC decrease mostly by increase of the engine speed and expressed low values the model-2 at 3,000 R.P.M and the model-1 at high speed. Wholly, the model-2 expressed stable results. The temperature distributions expressed high distributions by increase of the engine speed, and the model-3 was express most good among three models. (author). 11 refs., 8 figs., 1 tab.

194

Test of reduction in an internal combustion engine by the use of a light-weight and anti-corrosion muffler (Part 1). Heat-resistant epoxide resin muffler for a motor-cycle  

In order to reduce exhaust gas noise of a motorcycle, a light-weight muffler made of heat-resistant epoxide resin, instead of steel, has been tested, setting at the outlet of a 250 ml engine exhaust system. The noise level of the exhaust gas after being introduced into the shielding compartment was measured by a standard noise meter and analyzed its frequency distribution by a FET analyzer for the comparison of noise reduction effect. After mixing an acid anhydride curing agent and an accelerator, etc. to the bisphenol epoxide resin, the mixture was impreged to glass fibers and then was thermoset by a hot press as the heat-resistant epoxide resin muffler. The inside surface of the muffler was coated with stainless steel or ceramic paper. As a test result, the noise level of the heat-resistant epoxide resin muffler was comparable with those of the steel muffler with asbestos coating of 1.6mm thick. The heat-resistant epoxide resin muffler with ceramic paper coating showed effectiveness of noise reduction when the temperature of the muffler increased at a temperature of glass transition point. 3 references, 10 figures, 3 tables.

195

Low-temperature selective catalytic reduction of NO{sub x}. Catalytic behavior and kinetic modeling  

The aim of this study was to design new catalytic systems for the selective catalytic reduction of NO{sub x} with increased activity and improved dynamic behavior, particularly in the lower temperature range. This included the optimization of the kinetics. The catalysts, developed in our laboratory, were scrutinized under conditions corresponding to real exhausts and the sensitivity of the activity and selectivity to the different components in the exhaust gas was determined. Additionally, the kinetic behavior of a commercial sample, used as a reference catalyst, was investigated in the low temperature range. The work can be subdivided in the following main topics: - setup of a fully computer controlled pilot plant for exhaust gas catalysts, - preparation of chromia on titania catalysts with an improved activity and selectivity, - experimental investigations and simulations of the intrinsic kinetics of a commercial catalyst, a vanadia-titania aerogel catalyst and a titania supported chromia catalyst, - investigations of the deactivation behavior and of the SO{sub 2} poisoning of titania supported chromia catalysts by kinetic measurements, X-ray photoelectron spectroscopy analysis and transmission FTIR spectroscopy. (author) figs., tabs., refs.

196

Process for removing acid components from waste gases. Verfahren zum Entfernen saurer Komponenten aus Abgasen  

The invention concerns a simple and economic process for removing acid components from waste gases, preferably from existing coal-fired or oil fired power stations with dust extraction, wet desulphurisation and spray drying of the washing solution occurring in wet desulphurisation, in which a part flow is taken from the waste gases before dust extraction, is taken to spray drying and is reunited with the main gas flow before wet desulphurisation and/or before dust extraction. According to the invention with waste gases from boiler plant with air preheating, the part flow is taken before the air preheating. The part of the waste gas taken before the air preheating has a high temperature, so that only a small quantity of exhaust gas is required for evaporating the washing solution from the desulphurisation plant. The small quantity of exhaust gas results in small dimensions of the spray drier and the separator. A quantity of waste gas of 2 to 15% relative to the total quantity of waste gas is sufficient for spray drying of the washing solution. If the process according to the invention is used for a new powerstation, the air preheater and the electrostatic filter after the air preheater are reduced in size.

197

Temperature measurements in fluid flows (eventually reactive, multi-phase...) using optical methods; Mesure des temperatures dans les ecoulements (eventuellement reactifs, multiphasiques...) par methodes optiques  

This conference day was organized by the `radiations` section of the French association of thermal engineers. This book of proceedings contains 8 papers entitled: `simultaneous temperature and NO concentration measurements in a hydrogen-air turbulent flame`; `application of iodine laser induced fluorescence to temperature, pressure and velocity measurements`; `Doppler phase measurement of refractive index and temperature`; `experimental and numerical study of temperature fields of particulates in plasma jets`; `measurement and determination of temperatures and concentrations of hot exhaust gases with FTIR emission spectroscopy`; `combustion control in gas turbines using CO{sub 2} emission spectroscopy`; `analysis of gases temperature fields and particulate jets. Application to hydrogen-air, kerosene stato-reactors and to solid propellant jets`; `restitution of temperature and species profiles in pre-mixing flames by inversion of transmission and IR emission data. (J.S.)

198

Effect of water gas shift reaction on the reduction of wustite pellets in a fixed bed with H sub 2 -CO and H sub 2 CO sub 2 gas mixtures. H sub 2 -CO oyobi H sub 2 -CO sub 2 kongo gas ni yoru wustite koteiso no kangen ni oyobosu suisei gas shift hanno no eikyo  

The industrial hematite is prereduced to wustite and again reduced with H{sub 2}-CO and H{sub 2}-CO{sub 2} gas mixtures at 900{degree}C, and the effect of water gas shift reaction on the reduction is investigated theoretically and experimentally using unequal temperature model. The effect of oxygen diffusion in dense phase, the effect of high void fraction in the periphery of the reaction tube wall on the gas flow, reaction temperature, effect of gas compositions on parameters and others are also studied, and for all effects the experimental results have agreed with the theoretical values. In the reduction with H{sub 2}-CO, the effect of water shift reaction on the reduction curves or on the change of exhaust gas composition in bed with time has not been so significant, but there has been higher decrease in temperature than that of decrease in temperature by reduction reaction as a result of slight temperature difference inside the bed. In the reduction with H{sub 2}-CO{sub 2}, the effect of water shift reaction on the reduction has been significant with the increase of CO{sub 2} concentration in the bed inlet gas, and the temperature in the bed has been lowered remarkably. 30refs., 7 figs.

199

Low-temperature selective catalytic reduction of NOx with NH3 over metal oxide and zeolite catalysts-A review  

The removal of NOx by catalytic technology at low temperatures (100-300^oC) is significant for flue gas of industry and exhaust gas of diesel engine; however, to develop the low-temperature catalyst (LTC) for selective catalytic reduction of NOx with ammonia (NH3-SCR) is still a challenge especially at temperature below 200^oC. This study reviews two types of LTC, the metal oxide catalyst and metal exchanged zeolite catalyst. The performances of Mn-based metal oxide with and without supports have been attempted to correlate with preparation method, precursor, and various supports. The role of manganese oxides with different phases as the most effective low temperature active component and the limitation of stability in the presence of H2O and SO2 are discussed. Fe, Cu exchanged zeolites as...

200

Temperature control system for pyrolysis furnace  

This patent describes a batch-type pyrolysis furnace having a main chamber, a main gas burner to directly heat air ducted into the chamber, and a throat near the top of the main chamber through which throat organic vapor volatilized by pyrolysis of polymerbonded metal parts leave the main chamber. It also has an afterburner chamber provided with an afterburner to incinerate the organic vapor downstream of the throat, and, an exhaust stack through which incinerated vapor is vented. The improvement described here comprises: a first temperature sensing means, located within the main chamber, near the top thereof, to sense the instantaneous ambient temperature of gases above the metal parts therewithin; a second temperature sensing means, located in the exhaust stack downstream of the afterburner operatively connected to the main burner for attenuated or on/off operation thereof; a third temperature sensing means, located in the throat upstream of the afterburner the throat having an area, and the main chamber having a volume which are related such that their ratio is always greater than the critical vent number 0.005/ft. and water spray means responsive only to the first and/or third temperature sensing means when either the temperature in the main chamber exceeds a predetermined critical ambient temperature in the range from about 600/sup 0/-900/sup 0/F, or the temperature in the throat is at least about 50/sup 0/F higher than the ambient temperature.

 
 
 
 
201

Superheating a low pressure turbine: Methods, data reduction and monitoring  

This work has indicated with proper benchmarking, that a Low Pressure (LP) turbine can be monitored for performance in real time. The work demonstrates by superheat testing of the LP exhaust that common heat balance programs, with upgrading of extraction models, can with high accuracy predict the Used-Energy-End-Point and isentropic efficiency. This paper presents methods, data reduction techniques and recommended on-line models useful for low pressure (LP) turbine thermal performance monitoring. This work was conducted at the Redondo Generating Station, Unit 7, a gas-fired plant rated at 450 MWe. The objective of the testing was to benchmark a turbine cycle computer simulator when the LP was in a superheated exhaust condition. LP superheat was achieved by reducing circulatory water flow, thus raising condenser pressure, and dropping load such that the LP`s used-energy-end-point was driven to superheat. Such benchmarking was not intended to establish `correction factors` applicable at full load operation, but rather only to assure that analytical models could track LP performance throughout the load range. A method of plotting a family of curves which indicates all possible operational conditions was established. A quick look at this curve would indicate for any LP inlet condition and for any condenser pressure, the possibility of superheated exhaust and the degree of that superheat given measured temperatures. The usefulness of this curve was clearly demonstrated during the test. The paper also discusses methods used to measure exhaust temperature (within basket tips, etc.), isolation of feedwater heaters, and other methods. Results indicated outstanding agreement between measured LP generation and predicted, while superheated. Details in the data indicated differential velocity profiles across the rotor axis. In addition, results indicated that the vendor`s exhaust loss curve was not applicable at low loads. Discussion and recommendations are offered.

202

Textile dryer heat recovery system  

A textile dryer heat recovery system includes a textile dryer and a heat exchanger. A duct is provided for directing dryer exhaust gas to the heat exchanger for preheating dryer input air. A cleaning system within the heat exchanger removes dryer exhaust gas contaminants deposited in the heat exchanger.

203

Rotary positive displacement engine  

A co-rotor engine and valving system is described. By means of the valve system, gas under pressure is admitted to and exhausted from motor chambers defined between the rotor vanes in a controlled manner. The rotor members are caused to be rotated under power through the admission and exhausting of the gas. (UK)

204

Reduction of noise emitted from exhaust paths of gas turbine units equipped with heat recovery boilers  

The values by which noise emitted from exhaust paths of different gas-turbine units equipped with heat recovery boilers exceeds the levels prescribed by sanitary standards are calculated. Measures to reduce noise emitted from the exhaust paths of gas-turbine units with heat recovery boilers are discussed, and design solutions developed at the Moscow Power Engineering Institute for suppressing this noise are described.

205

Combined cycle power plant incorporating coal gasification  

A combined cycle power plant incorporating a coal gasifier as the energy source. The gases leaving the coal gasifier pass through a liquid couplant heat exchanger before being used to drive a gas turbine. The exhaust gases of the gas turbine are used to generate both high pressure and low pressure steam for driving a steam turbine, before being exhausted to the atmosphere.

206

Apparatus for purifying exhaust gases of internal combustion engines  

Apparatus for purifying the exhaust gases of internal combustion engines is disclosed that is comprised of a pair of upstream exhaust pipes, a catalytic converter, and a downstream exhaust pipe. The catalytic converter comprises a cylindrical shell having an inlet chamber, a catalyst chamber, an outlet chamber, and a monolithic catalyst element in the catalyst chamber. The inlet chamber has inlet ports communicating with the upstream exhaust pipes respectively and axial lines of the inlet ports cross each other in the inlet chamber. In the inlet chamber, a diffusion means is provided to diffuse the exhaust gas for uniformly distributing it to the catalyst element.

207

Planned Operation of Tritium Recovery System Based on Investigation of LHD Exhaust System  

To understand the conditions of exhaust gas treatment at the transition point between the Large Helical Device (LHD) vacuum pumping system and the exhaust gas tritium recovery system, the gas flow rate and hydrogen concentration were measured. Simultaneous measurement of the exhaust gas flow rate and hydrogen concentration was made possible by applying two types of hydrogen monitors: a thermal conductivity sensor and a combustible gas sensor. The obtained results have led to remodeling of the LHD vacuum pumping system and an optimised plan of operation for the tritium recovery system.   

208

Planned Operation of Tritium Recovery System Based on Investigation of LHD Exhaust System  

To understand the conditions of exhaust gas treatment at the transition point between the Large Helical Device (LHD) vacuum pumping system and the exhaust gas tritium recovery system, the gas flow rate and hydrogen concentration were measured. Simultaneous measurement of the exhaust gas flow rate and hydrogen concentration was made possible by applying two types of hydrogen monitors: a thermal conductivity sensor and a combustible gas sensor. The obtained results have led to remodeling of the LHD vacuum pumping system and an optimised plan of operation for the tritium recovery system.

209

Advanced turbine systems program conceptual design and product development Task 8.3 - autothermal fuel reformer (ATR). Topical report  

Autothermal fuel reforming (ATR) consists of reacting a hydrocarbon fuel such as natural gas or diesel with steam to produce a hydrogen-rich {open_quotes}reformed{close_quotes} fuel. This work has been designed to investigate the fuel reformation and the product gas combustion under gas turbine conditions. The hydrogen-rich gas has a high flammability with a wide range of combustion stability. Being lighter and more reactive than methane, the hydrogen-rich gas mixes readily with air and can be burned at low fuel/air ratios producing inherently low emissions. The reformed fuel also has a low ignition temperature which makes low temperature catalytic combustion possible. ATR can be designed for use with a variety of alternative fuels including heavy crudes, biomass and coal-derived fuels. When the steam required for fuel reforming is raised by using energy from the gas turbine exhaust, cycle efficiency is improved because of the steam and fuel chemically recuperating. Reformation of natural gas or diesel fuels to a homogeneous hydrogen-rich fuel has been demonstrated. Performance tests on screening various reforming catalysts and operating conditions were conducted on a batch-tube reactor. Producing over 70 percent of hydrogen (on a dry basis) in the product stream was obtained using natural gas as a feedstock. Hydrogen concentration is seen to increase with temperature but less rapidly above 1300{degrees}F. The percent reforming increases as the steam to carbon ratio is increased. Two basic groups of reforming catalysts, nickel - and platinum-basis, have been tested for the reforming activity.

210

Seawater pre-deaerator for open-cycle ocean thermal energy conversion applications  

This patent describes a seawater deaerator. It comprises a water reservoir, a low pressure gas chamber above the water reservoir, a vacuum pump connected to the gas chamber for evacuating the gas chamber, gas injectors near a bottom of the water reservoir for injecting gas in the water reservoir, a conduit connected to an exhaust of the vacuum pump for recycling exhaust gas from the vacuum pump to the gas injectors, means in the gas injectors for releasing gas into the reservoir in fine seed bubble nuclei.

211

Turbocharger, particularly exhaust gas turbo-charger for internal combustion engines. Turbolader, insbesondere Abgasturbolader fuer Brennkraftmaschinen  

The invention deals with a turbocharger, in particular with an exhaust gas turbocharger for an internal combustion engine, provided with a turbine and exhaust gas channels. It is intended to improve the performance of the turbocharger with simple means. This problem has been resolved by an injector nozzle for accelerating the exhaust gases. The static pressure in the exhaust channel decreases, effected by the nozzle system. Thus the pressure difference between inlet and outlet of the turbine is increased which results in a higher performance. The injection nozzle is formed as a ring, enclosing the exhaust channel. By this arrangement it is possible to construct a small exhaust gas turbocharger with the same performance. The start and running behaviour could be improved.

212

Real-time Measurement of the Water Concentration in the Exhaust Gases of a PEFC for Water Transport Analysis  

Water management is essential for high performance operation of PEFCs (Polymer Electrolyte Fuel Cells). In this study, a single cell of PEFC was operated for 180 seconds with various current densities, and at the same time, the water vapor concentrations in the anode and the cathode exhaust gases were measured in high accuracy. The water transport, concentration distribution, and the formation of liquid phase water in the cell were estimated based on the experimental data. The effects of gas flow rate, current density and humidity temperatures of the inlet gases on the behaviors of the water were also investigated. The cell current at which the condensation of the water in the cell begins was determined by extrapolating the water concentration change in the exhaust gases.   

213

Numerical model of a thermoelectric generator with compact plate-fin heat exchanger for high temperature PEM fuel cell exhaust heat recovery International Journal of Hydrogen Energy  

This paper presents a numerical model of an exhaust heat recovery system for a high temperature polymer electrolyte membrane fuel cell (HTPEMFC) stack. The system is designed as thermoelectric generators (TEGs) sandwiched in the walls of a compact plate-fin heat exchanger. Its model is based on a finite-element approach. On each discretized segment, fluid properties, heat transfer process and TEG performance are locally calculated for higher model precision. To benefit both the system design and fabrication, the way to model TEG modules is herein reconsidered; a database of commercialized compact plate-fin heat exchangers is adopted. Then the model is validated against experimental data and the main variables are identified by means of a sensitivity analysis. Finally, the system configuration is optimized for recovering heat from the exhaust gas. The results exhibit the crucial importance of the model accuracy and the optimization on system configuration. Future studies will concentrate on heat exchanger structures.

214

Prediction on the base pressure for an axisymmetric body  

The physics of the flow field surrounding an engine nacelle afterbody is very complex. A high pressure jet from the nozzle interacts with the external flow and causes upstream influence on the afterbody surface field. At certain conditions, the nozzle boundary layer can separate, either by shock wave interaction or by adverse pressure gradient effect, resulting in a severe drag penalty. Furthermore, a finite afterbody base implies a recirculating flow region. A flow modeling method has been developed to analyze the flow in the annular base(rear-facing surface) of a circular engine nacelle flying at subsonic speed but with a supersonic exhaust jet. Real values of exhaust gas properties and temperature are included. (author). 4 refs., 11 figs.

215

Real-time control oriented HCCI engine cycle-to-cycle dynamic modelling  

For homogeneous charge compression ignition (HCCI) combustion, the auto-ignition process is very sensitive to in-cylinder conditions, including in-cylinder temperature, in-cylinder components and concentrations. Therefore, accurate control is required for reliable and efficient HCCI combustion. This paper outlines a simplified gasoline-fueled HCCI engine model implemented in Simulink environment. The model is able to run in real-time and with fixed simulation steps with the aim of cycle-to-cycle control and hardware-in-the-loop simulation. With the aim of controlling the desired amount of the trapped exhaust gas recirculation (EGR) from the previous cycle, the phase of the intake and exhaust valves and the respective profiles are designed to vary in this model. The model is able to anticip...

216

Better Enzymes for Carbon Capture: Low-Cost Biological Catalyst to Enable Efficient Carbon Dioxide Capture  

IMPACCT Project: Codexis is developing new and efficient forms of enzymes known as carbonic anhydrases to absorb CO2 more rapidly and under challenging conditions found in the gas exhaust of coal-fired power plants. Carbonic anhydrases are common and are among the fastest enzymes, but they are not robust enough to withstand the harsh environment found in the power plant exhaust steams. In this project, Codexis will be using proprietary technology to improve the enzymes’ ability to withstand high temperatures and large swings in chemical composition. The project aims to develop a carbon-capture process that uses less energy and less equipment than existing approaches. This would reduce the cost of retrofitting today’s coal-fired power plants.

217

A dynamical instability of spark-ignited engines.  

A simple model for spark-ignited engines is proposed in which the residual exhaust gases of a combustion event affect ignition of the subsequent charge. The model is an example of a one-dimensional, discrete, nonlinear mapping of an interval. Laminar flame correlations incorporated within models for ignition exhibit Arrhenius kinetics. Small variations of the ignition time with respect to the expansion cycle alter the work produced by each cycle, thereby altering the exhaust-gas temperature. It is shown that the mixing of hot residual gases with a fresh charge is a sufficient mechanism to produce an instability of the ignition process, resulting in oscillatory behavior. When this instability is compounded with the effects of mixture turbulence, one obtains a novel picture of the well-known phenomenon of "cyclic dispersion" exhibited by such engines. PMID:17819493

218

Dynamical instability of spark-ignited engines  

A simple model for spark-ignited engines is proposed in which the residual exhaust gases of a combustion event affect ignition of the subsequent charge. The model is an example of a one-dimensional, discrete, nonlinear mapping of an interval. Laminar flame correlations incorporated within models for ignition exhibit Arrhenius kinetics. Small variations of the ignition time with respect to the expansion cycle alter the work produced by each cycle, thereby altering the exhaust-gas temperature. It is shown that the mixing of hot residual gases with a fresh charge is a sufficient mechanism to produce an instability of the ignition process, resulting in oscillatory behavior. When this instability is compounded with the effects of mixture turbulence, one obtains a novel picture of the well-known phenomenon of cyclic dispersion exhibited by such engines.

219

Feasibility of blending karanja vegetable oil in petro-diesel and utilization in a direct injection diesel engine  

Karanja (Pongamia pinnata) oil, a non-edible high viscosity (27.84cSt at 40degreeC) straight vegetable oil, was blended with conventional diesel in various proportions to evaluate the performance and emission characteristics of a single cylinder direct injection constant speed diesel engine. Diesel and karanja oil fuel blends (5%, 10%, 15%, and 20%) were used to conduct short-term engine performance and emission tests at varying loads (0%, 20%, 40%, 60%, 80%, and 100%). Tests were carried out over the entire range of engine operation and engine performance parameters such as fuel consumption, thermal efficiency, exhaust gas temperature, and exhaust emissions (smoke, CO, CO2, HC, NOx, and O2) were recorded. The brake specific energy consumption (BSEC), brake thermal efficiency (BTE), and ex...

220

Implementation of an experimental pilot reproducing the fouling of the exhaust gas recirculation system in diesel engines  

The European emission standards EURO 5 and EURO 6 define more stringent acceptable limits for exhaust emissions of new vehicles. The Exhaust Gas Recirculation (EGR) system is a partial but essential solution for lowering the emission of nitrogen oxides and soot particulates. Yet, due to a more intensive use than in the past, the fouling of the EGR system is increased. Ensuring the reliability of the EGR system becomes a main challenge. In partnership with PSA Peugeot Citroën, we designed an experimental setup that mimics an operating EGR system. Its distinctive features are (1) its ability to reproduce precisely the operating conditions and (2) its ability to measure the temperature field on the heat exchanger surface with an Infra Red camera for detecting in real time the evolution of the fooling deposit based on its thermal resistance. Numerical codes are used in conjunction with this experimental setup to determine the evolution of the fouling thickness from its thermal resistance.

 
 
 
 
221

Some environmental considerations relating to the interaction of the solid rocket motor exhaust with the atmosphere: Predicted chemical composition of exhaust species and predicted conditions for the formation of HCl aerosol  

The exhaust products of a solid rocket motor using as propellant 14% binder, 16% aluminum, and 70% (wt) ammonium perchlorate consist of hydrogen chloride, water, alumina, and other compounds. The equilibrium and some frozen compositions of the chemical species upon interaction with the atmosphere were computed. The conditions under which hydrogen chloride interacts with the water vapor in humid air to form an aerosol containing hydrochloric acid were computed for various weight ratios of air/exhaust products. These computations were also performed for the case of a combined SRM and hydrogen-oxygen rocket engine. Regimes of temperature and relative humidity where this aerosol is expected were identified. Within these regimes, the concentration of HCL in the aerosol and weight fraction of aerosol to gas phase were plotted. Hydrochloric acid aerosol formation was found to be particularly likely in cool humid weather.

222

Hot exhaust gases with passive FTIR emission spectroscopy  

Passive FTIR emission spectroscopy using a commercial medium resolution instrument with a telescope has been applied to analyze the hot exhaust gases of various combustion sources, such as industrial and building smoke stacks, aircraft engines, flares, and forest fires. To interpret the remotely measured spectra a multi-layer, line-by-line spectra retrieval software using the molecular spectral databases HITRAN and HITEMP has been developed, validated and successfully used to determine the exhaust gas temperatures and the concentrations of CO2, H2O, CO, N2O, CH4, NO, NO2, SO2, and HCl for different combustion conditions of the sources. In this paper the feasibility and the setup of passive IR measurements, the basic theory of radiative transfer and special features of the commercially available spectra analysis code are described. In addition, the results of the different measurement applications are summarized.

223

Indium oxide-based gas sensor for selective detection of CO  

A compact solid-state CO sensor has been eagerly desired for detecting incomplete combustion of gas appliances, because continuous monitoring of CO in combustion exhausts can prevent a serious CO poisoning accident from occurring. The relevant sensor should be not only highly sensitive to CO but also selective to CO against various coexistent gases such as H{sub 2}, CH{sub 4}, C{sub 3}H{sub 6}, CO{sub 2}, NO and water vapor. In addition it should at the temperature of the exhausts (200-400 {degrees}C). In order to develop such a CO sensor, an extensive search was carried out for semiconducting oxides and modifiers. As a result, an In{sub 2}O{sub 3}-based sensor modified with Rb{sub 2}O was found to be sensitive and selective to CO at 300-400 {degrees}C, as described below.

224

High-temperature erosion-corrosion of alloys. Final report. [Haynes 188; Inconel MA754; Haynes 8077 and EB  

In a fluidized-bed combustion system, the combustion gases will normally pass over various heat exchange surfaces and other components before being exhausted. In conventional pulverized coal-fired boilers, erosion of the gas-pass heat exchangers may occur, and such boilers are designed to maximum nominal gas velocities which depend, to some extent, on the ash content and type. There is little understanding of the mechanism of the erosion processes or the basis for the empirically derived maximum velocity. This study has developed an apparatus for the study of erosion processes at elevated temperatures and has examined the erosion of a wide range of alloys by 15 ..mu..m alumina particles at 63 and 170 fps (19 and 53 m/s) at temperatures up to 1600/sup 0/F (871/sup 0/C) in argon a simulated combustion gas, and a simulated gasifier atmosphere.

225

Development of new smoke exhaust system for an underground parking lot; Chika chushajo wo taisho to shita takino haiki system no kaihatsu  

An experiment was made to develop an exhaust/fume system for an underground parking lot. The system was capable of watering cooling/watering gas suction as needed and reduced fume temperature and prevent the fume fan from stopping on fire and exhausted air normally. In the experiment, watering was made to three steel meshes in the duct to cool fire/smoke. Water film due to watering was formed on the mesh but the water film was damaged when a certain wind velocity was exceeded. The air flow temperature in the duct decreased in the process where air flowed in the duct from the outer surface of duct to external air due to cooling. The cooling effect due to watering was clear and the air flow temperature inside duct was maintained to be 280{degree}C or less on fire. The cooling effect was improved due to increase in the amount of watering and the thinning of mesh. An experiment on the elimination of pollutants on daily exhaust was performed. The concentration of CO and CO2 was maintained to be constant regardless of watering. Watering was effective to the elimination of dust (elimination rate of 80%) and was effective to NOx and SO2 to some extent. 1 ref., 10 figs., 3 tabs.

226

CFD modeling of thermoelectric generators in automotive EGR-coolers  

A large amount of the waste heat in the exhaust gases from diesel engines is removed in the exhaust gas recirculation (EGR) cooler. Introducing a thermoelectric generator (TEG) in an EGR cooler requires a completely new design of the heat exchanger. To accomplish that a model of the TEG-EGR system is required. In this work, a transient 3D CFD model for simulation of gas flow, heat transfer and power generation has been developed. This model allows critical design parameters in the TEG-EGR to be identified and design requirements for the systems to be specified. Besides the prediction of Seebeck, Peltier, Thomson and Joule effects, the simulations also give detailed insight to the temperature gradients in the gas-phase and inside the thermoelectric (TE) elements. The model is a very valuable tool to identify bottlenecks, improve design, select optimal TE materials and operating conditions. The results show that the greatest heat transfer resistance is located in the gas phase and it is critical to reduce this in order to achieve a large temperature difference over the thermoelectric elements without compromising on the maximum allowable pressure drop in the system. Further results from an investigation of the thermoelectric performance during a vehicle test cycle is presented.

227

Prevention of phosphoric acid corrosion of fuel cell and its system; Nenryo denchi no rinsan fushoku boshi hoho oyobi rinsan fushoku boshi sochi  

In the conventional phosphoric acid fuel cell, the selective corrosion due to phosphoric acid takes place at the inlet of the air preheater, since the high temperature exhaust gas from the air electrode containing phosphoric acid is supplied to the air preheater. This invention solves the problem. Spray devices which spray water mist into the gases coming out of the air electrode and the fuel electrode of the phosphoric acid fuel cell. When the water mist is sprayed into the exhaust gas from the fuel cell, the gas temperature is so lowered that the phosphoric acid corrosion does not take place any more, and that the phosphoric acid vapor or the acid mist is absorbed in the residual spray water mist which does not vaporize to be discarded as the drainage from the system. So that the corrosion of equipment by phosphoric acid can be effectively prevented. In order to increase the gas liquid contact efficiency of the spray water, it is preferable to use the demister or buffer plate in the passage. 7 figs.

228

Surface treatment device and surface treatment method for first wall of thermonuclear reactor  

In a device for a surface treatment of removing hydrocarbon compound containing tritium deposited on an armor of a first wall of a thermonuclear reactor, there is disposed a means for supplying a gas for oxidizing the hydrocarbon compounds to the first wall, recovering tritium water and oxidation reaction products from generated exhaustion gases and sending the oxidizing gas in the exhaust gases to an oxidizing gas regeneration means. The hydrocarbon compounds on the surface of the armor material are oxidized at a low temperature by an oxidizing gas with high reactivity. Accordingly, since tritium on the surface can be removed and recovered by heating as a tritium water without diffusing tritium on the surface to the inside of the armor material, the temperature elevation of the mother material of the armor can be reduced. As a result, the amount of tritium diffused to the inside of the armor can greatly be reduced, to increase the amount of tritium which can be reutilized effectively. Further, since the tritium oxidizing means can be saved, tritium can be recovered only by disposing an ordinary adsorption tower. (N.H.).

229

Heavy-Duty Waste Hauler with Chemically Correct Natural Gas Engine Diluted with EGR and Using a Three-Way Catalyst: Final Report, 24 February 2004 -- 23 February 2006  

This report discusses the development of a E7G 12-liter, lean-burn natural gas engine--using stoichiometric combustion, cooled exhaust gas recirculation, and three-way catalyst technologies--for refuse haulers.

230

49 CFR 192.169 - Compressor stations: Pressure limiting devices.  

...2010-10-01 false Compressor stations: Pressure...TRANSPORTATION OF NATURAL AND OTHER GAS BY PIPELINE: MINIMUM... § 192.169 Compressor stations: Pressure...line that exhausts gas from the pressure relief valves of a compressor station must...

231

NO.sub.x sensor and process for detecting NO.sub.x  

This invention is a process for detecting low levels of nitrogen oxides (NO.sub.x) in a flowing gas stream (typically an exhaust gas stream) and a catalytic NO.sub.x sensor which may be used in that process.

232

Selective NOx Recirculation for Stationary Lean-Burn Natural Gas Engines. Annual Technical Progress Report.  

The research program conducted at the West Virginia University Engine and Emissions Research Laboratory (EERL) is working towards the verification and optimization of an approach to remove nitric oxides from the exhaust gas of lean burn natural gas engine...

233

Development of new surface treatments for improving oxidation resistance of TiAl; TiAl no taisanka hyomen shoriho no kaihatsu  

The TiAl intermetallic compound having excellent low density and high temperature strength is expected to be used for driving system valves or gas exhaust system parts of automobile engines. But, even though the TiAl compound has the high temperature strength for a structural compound, it does not have such good oxidation resistance at temperatures higher than 800degC in comparison with a heat resistance steel or Ni based super alloys. Therefore, the authors of the paper have made accumulated studies on surface treatment technologies aiming at improving the high temperature oxidation resistance of the TiAl and have developed two kinds of surface treatments (FB treatment; fluidized bed furnace method and SB treatment; shot blast method) by which the TiAl may obtain in a simple and cheaper way an oxidation resistance in excess of the Ni based super alloys. Each of the developed surface treatments endows the TiAl with repeated oxidation resistance at 950degC, in atmosphere or in exhaust gas. WO3-FB treatment can treat a mass of products in a very short time. As it is possible to carry out the WO3-SB treatment at room temperature, it can endow the product with the oxidation resistance after the last finishing process. 6 refs., 6 figs.

234

Spark ignition engine control: estimation and prediction of the in-cylinder mass and chemical species; Controle moteur a allumage commande: estimation / prediction de la masse et de la composition du melange enferme dans le cylindre  

Spark ignition engine control has become a major issue regarding compliance with emissions legislation while ensuring driving comfort. The objective of this thesis was to estimate the mass and composition of gases inside the cylinder of an engine based on physics in order to insure better control of transient phases taking into account residual gases as well as exhaust gas recirculation. Residual gas fraction has been characterized using two experiments and one CFD code. A model has been validated experimentally and integrated into an observer which predicts pressure and temperature inside the manifold. The predictions of the different gas flows and the chemical species inside the cylinder are deduced. A closed loop observer has been validated experimentally and in simulation. Moreover, an algorithm estimating the fresh and burned gas mass from the cylinder pressure has been proposed in order to obtain the information cycle by cycle and cylinder by cylinder. (author)

235

Optical observation of self-gas-flow in GCB  

The generation of self gas flow in a model SF/sub 6/ gas circuit breaker without puffer action is observed by high speed photography, shadow photography using a Q-switch ruby laser and time- and space-resolved spectrography. The model breaker is specially designed for observation of gas flow in all the spaces from the cylinder to the exhaust space. The results of the observations are compared with a free burning arc and show that the self gas flow to the arc in the breaker reduces the diameter of the arc, and raises the temperature of the arc core. This model breaker interrupts the current of 3 kArms with a transient recovery voltage of 2 kV/..mu..sec, though the pressure rise of the cylinder is less than 0.3 x 10/sup 5/ Pa.

236

Development of a new hybrid burner generation initial experience in the Siemens V84.2 and V94.2 gas turbines  

Following to the trend of increasing turbine inlet temperature and aggravated limitations of the emission of NO{sub x} in the exhaust gas the development of an improved hybrid burner became necessary. The paper presents the steps of development of this revised Siemens hybrid burner (HR3) as well as the experience on site in the V84.2 and V94.2 gas-turbines. Besides in both types of turbines the HR3 burner showed an excellent performance regarding to trouble free operation, low emissions and no combustion driven oscillations. During the tests in the Siemens V84.2 gas turbine NO{sub x} - emission clearly in the single digit range and in the V94.2 gas turbine an emission level well below 25 ppmv was demonstrated. (au)

237

Euler-Lagrange/DEM simulation of wood gasification in a bubbling fluidized bed reactor  

We present an Euler-Lagrange method for the simulation of wood gasification in a bubbling fluidized bed. The gas phase is modeled as a continuum using the 2D Navier-Stokes equations and the solid phase is modeled by a Discrete Element Method (DEM) using a soft-sphere approach for the particle collision dynamic. Turbulence is included via a Large-Eddy approach using the Smagorinsky sub-grid model. The model takes into account detailed gas phase chemistry, zero-dimensional modeling of the pyrolysis and gasification of each individual particle, particle shrinkage, and heat and mass transfer between the gas phase and the particulate phase. We investigate the influence of wood feeding rate and compare exhaust gas compositions and temperature results obtained with the model against experimental ...

238

Experimental and computational study of methane mixtures pyrolysis in a flow reactor under atmospheric pressure  

A study of the pyrolysis of methane mixtures in a laboratory reactor, exploring the influence of the bath gas used (N2 and CO2) and the presence of small amounts of ethane to simulate natural gas, has been carried out at atmospheric pressure and the 1250-1500 K temperature range. Exhaust gaseous species analysis was realized using a gas chromatographic system and total soot was determined by collecting and weighing it. The study can be useful for understanding and optimizing the performance of modern engines, gas turbines and some fuel cell systems where the syngas feed is obtained from the partial oxidation of different mixtures with possible formation of soot and other undesired products. Model simulations using two detailed kinetic mechanisms have been performed. Overall, experimental a...

239

Gas separation technology; Gas bunri gijutsu  

The gas separation technology, generally, includes liquefaction separation (distillation), absorption, adsorption, and membrane separation. The gas separation method is determined due to the mixed gas properties, role of separation during the process, and specifications of products. This paper reviews the distillation process, absorption process, adsorption process, and membrane separation process. For the distillation process, a production process of nitrogen and oxygen by the low temperature processing is illustrated. Recently, nitrogen with a purity of 99.99% and oxygen with 99.95% can be obtained by the low temperature processing. For the gas absorption process, the soluble component in gas is dissolved in a liquid by contacting gas with the liquid. The gas absorption is applied to the purification of raw gases, and the recovery of effective components or removal of harmful components in the exhaust gases. Porous solids, such as activated carbon, permutite, alumina, and silica, are used for gas adsorbents. Industrial applications of adsorption operation are illustrated. Furthermore, industrial applications of membrane gas separation are also introduced. 12 refs., 1 fig., 9 figs.

240

CO2 separation/recovery technology from exhaust gas of boiler. Boiler hai gas kara no CO2 bunri kaishu gijutsu  

Explanation is made of technology to separate/recover CO2 in the exhaust gas from the thermal power generation boiler. The chemical absorption method is a method in which chemical reaction is utilized between the absorbent liquid and CO2. That method is represented by alkanol amine method and thermal potassium carbonate method. In the former method, the CO2 absorbed under the condition of ordinary temperature and ordinary pressure can be recovered by heating. However, it has the disadvantage of needing thermal energy for the CO2 emission and degrading the plant with sulfide. The latter method is appropriate to the high pressure absorption, and advantageous in thermal efficiency and against degradation. In the physical absorption method, utilized is the difference in solubility of CO2 depending upon the condition of temperature and pressure. Though small in thermal loss, it has the disadvantage of also absorbing other foreign components. The physical adsorption method is a dry method in which zeolite is utilized as a adsorbent. Therefore, measures are unnecessary against the corrosion but the enrichment factor is low. In the film separation method, utilized is the differ ence in permeation speed of gas. Development is needed of the film which excels in selectivity. In the low temperature separation method, exhaust gas is liquefied, fractionated and enriched. The thermal loss is large. In the oxygen combustion method, fossil fuel is burned with oxygen. Separation from nitrogen is unnecessary but the oxygen cost must be lowered. 6 refs., 7 figs., 3 tabs.

 
 
 
 
241

Install Waste Heat Recovery Systems for Fuel-Fired Furnaces (English/Chinese) (Fact Sheet)  

Chinese translation of ITP fact sheet about installing Waste Heat Recovery Systems for Fuel-Fired Furnaces. For most fuel-fired heating equipment, a large amount of the heat supplied is wasted as exhaust or flue gases. In furnaces, air and fuel are mixed and burned to generate heat, some of which is transferred to the heating device and its load. When the heat transfer reaches its practical limit, the spent combustion gases are removed from the furnace via a flue or stack. At this point, these gases still hold considerable thermal energy. In many systems, this is the greatest single heat loss. The energy efficiency can often be increased by using waste heat gas recovery systems to capture and use some of the energy in the flue gas. For natural gas-based systems, the amount of heat contained in the flue gases as a percentage of the heat input in a heating system can be estimated by using Figure 1. Exhaust gas loss or waste heat depends on flue gas temperature and its mass flow, or in practical terms, excess air resulting from combustion air supply and air leakage into the furnace. The excess air can be estimated by measuring oxygen percentage in the flue gases.

242

Novel Gas Sensors for High-Temperature Fossil Fuel Applications  

SRI International (SRI) is developing ceramic-based microsensors to detect exhaust gases such as NO, NO{sub 2}, and CO in advanced combustion and gasification systems under this DOE NETL-sponsored research project. The sensors detect the electrochemical activity of the exhaust gas species on catalytic electrodes attached to a solid state electrolyte and are designed to operate at the high temperatures, elevated pressures, and corrosive environments typical of large power generation exhausts. The sensors can be easily integrated into online monitoring systems for active emission control. The ultimate objective is to develop sensors for multiple gas detection in a single package, along with data acquisition and control software and hardware, so that the information can be used for closed-loop control in novel advanced power generation systems. This report details the Phase I Proof-of-Concept, research activities performed from October 2003 to March 2005. SRI's research work includes synthesis of catalytic materials, sensor design and fabrication, software development, and demonstration of pulse voltammetric analysis of NO, NO{sub 2}, and CO gases on catalytic electrodes.

243

Evaluation of exhaust emissions from a Bi-fueled vehicle operating on liquid and gaseous fuels. Topical report, June-July 1995  

Exhaust emissions were characterized from a bi-fueled vehicle operating on compressed natural gas and two gasolines over a heavy acceleration/high speed driving cycle and during cold temperature operation. The test fuels included compressed natural gas (CNG) meeting California Air Resources Board emissions certification specifications, industry average gasoline formulated to the specifications of Reference Fuel A (RF-A) used in the CRC/Auto Oil program, and Federal reformulated gasoline (RFG) purchased at a commercial service station in metropolitan Houston. Exhaust emissions were evaluated over the light-duty chassis dynamometer portion of the Federal Test Procedure at 75 deg F and at 20 deg F, and the REP05 - a hot, stabilized, high speed, high acceleration driving cycle developed by the EPA to be representative of non-FTP, in-use driving. In addition, CNG emissions were evaluated over the US06 driving cycle. Average regulated exhaust emissions (total hydrocarbons, methane, carbon monoxide, and oxides of nitrogen) were evaluated in a manner consistent with the Code of Federal Regulations.

244

Corrosion in the off-gas system of a radioactive-waste incinerator  

Corrosion in a low-level radioactive-waste incinerator off-gas system at the Department of Energy's Savannah River Plant is discussed. Severe corrosive attack and failure of an alloy 600 part exposed to high-temperature (>1000/sup 0/C) gases was observed. Rapid attack of carbon steel components, and cracking of austenitic stainless steel parts also occurred at locations where lower gas temperatures and periodic condensate exposure occurred. Investigation showed HCl, SO/sub 2/, SO/sub 3/ and phosphorus-oxides were present and contributed to the failures. Mechanisms of high-temperature failure include alloy separation and reactions with phosphorus. Coupons placed in the exhaust stream have provided information for selection of future materials of construction for system components. Several nickel- and iron-base alloys, and a stainless steel with an aluminum-diffusion coating were investigated.

245

Ammonium bisulfate formation temperature in a bench-scale single-channel air preheater  

Ammonium bisulfate (ABS) forms in coal-fired power plant exhaust systems when ammonia slip from the NOx control system reacts with the sulfur oxides and water in the flue gas. The critical temperature range for ABS formation occurs in the air preheater, where ABS is known to cause corrosion and pluggage that can require unplanned outages and expensive cleaning. To develop mitigation strategies for the deleterious effects of ABS in air preheaters, it is important to know its formation temperature and deposition process. This paper describes a bench-scale experimental simulation of a single-channel air preheater, with the appropriate temperature gradient, used in conjunction with simulated coal combustion flue gas, including sulfur oxides, ammonia, and water vapor, to investigate the formati...

246

Theoretical and Experimental Study of Thermoelectric Generators for Vehicles  

The general physical laws for reaching the maximum efficiency of a generator using vehicular exhaust heat have been studied. Based on the physical models of a generator with lumped and distributed parameters, the optimal gas temperature at the outlet of the thermoelectric generator (TEG) and the optimal distribution of gas temperature in the heat exchanger have been found. The basic generator parameters, namely the voltage, power, and efficiency, have been calculated in the steady-state and dynamic modes. The possibility of efficiency improvement by a factor of 1.5 through use of an exponential as compared with an isothermal distribution of heat exchanger temperature has been revealed. Calculations are confirmed by results from testing a prototype vehicular thermoelectric generator.

247

Energy recovery from textile dryer operations. Phase 1  

A two-step approach to conserving energy in the textile industry by decreasing gas consumption in dryer operations involves 1) the automatic control of dryer dampers to minimize the flow of exhaust heat and 2) the recovery and use of the exhaust heat to preheat incoming air. These measures could reduce natural gas consumption by 45-65%. Decreasing the exhaust flow rates entails increasing the dryer humidity to a maximum level (about 0.1 lb water/lb dry air) and controlling it by the stack dampers. Three types of air-to-air heat exchangers appear suitable for preheating the dryer air by the sensible exhaust heat.

248

Combined particle emission reduction and heat recovery from combustion exhaust - A novel approach for small wood-fired appliances  

Replacing fossil fuels by renewable sources of energy is one approach to address the problem of global warming due to anthropogenic emissions of greenhouse gases. Wood combustion can help to replace fuel oil or gas. It is advisable, however, to use modern technology for combustion and exhaust gas after-treatment in order to achieve best efficiency and avoid air quality problems due to high emission levels often related to small scale wood combustion. In this study, simultaneous combustion particle deposition and heat recovery from the exhaust of two commercially available wood-fired appliances has been investigated. The experiments were performed with a miniature pipe bundle heat exchanger operating in the exhaust gas lines of a fully automated pellet burner or a closed fireplace. The system has been characterised for a wide range of aerosol inlet temperatures (135-295 {sup circle} C) and flow velocities (0.13-1.0ms{sup -1}), and particle deposition efficiencies up to 95% have been achieved. Deposition was dominated by thermophoresis and diffusion and increased with the average temperature difference and retention time in the heat exchanger. The aerosols from the two different appliances exhibited different deposition characteristics, which can be attributed to enhanced deposition of the nucleation mode particles generated in the closed fire place. The measured deposition efficiencies can be described by simple linear parameterisations derived from laboratory studies. The results of this study demonstrate the feasibility of thermophoretic particle removal from biomass burning flue gas and support the development of modified heat exchanger systems with enhanced capability for simultaneous heat recovery and particle deposition. (author)

249

Combined particle emission reduction and heat recovery from combustion exhaust-A novel approach for small wood-fired appliances  

Replacing fossil fuels by renewable sources of energy is one approach to address the problem of global warming due to anthropogenic emissions of greenhouse gases. Wood combustion can help to replace fuel oil or gas. It is advisable, however, to use modern technology for combustion and exhaust gas after-treatment in order to achieve best efficiency and avoid air quality problems due to high emission levels often related to small scale wood combustion. In this study, simultaneous combustion particle deposition and heat recovery from the exhaust of two commercially available wood-fired appliances has been investigated. The experiments were performed with a miniature pipe bundle heat exchanger operating in the exhaust gas lines of a fully automated pellet burner or a closed fireplace. The system has been characterised for a wide range of aerosol inlet temperatures (135-295 deg. C) and flow velocities (0.13-1.0ms{sup -1}), and particle deposition efficiencies up to 95% have been achieved. Deposition was dominated by thermophoresis and diffusion and increased with the average temperature difference and retention time in the heat exchanger. The aerosols from the two different appliances exhibited different deposition characteristics, which can be attributed to enhanced deposition of the nucleation mode particles generated in the closed fire place. The measured deposition efficiencies can be described by simple linear parameterisations derived from laboratory studies. The results of this study demonstrate the feasibility of thermophoretic particle removal from biomass burning flue gas and support the development of modified heat exchanger systems with enhanced capability for simultaneous heat recovery and particle deposition.

250

TWRS hydrogen mitigation portable standard hydrogen monitoring system platform design and fabrication engineering task plan  

The primary function of portable gas monitoring is to quickly determine tank vapor space gas composition and gas release rate, and to detect gas release events. Characterization of the gas composition is needed for safety analysis. The lower flammability limit, as well as the peak burn temperature and pressure, are dependent upon the gas composition. If there is little or no knowledge about the gas composition, safety analysis utilize compositions that yield the worst case in a deflagration or detonation. This conservative approach to unknowns necessitates a significant increase in administrative and engineering costs. Knowledge of the true composition could lead to reductions in the assumptions and therefore contribute to a reduction in controls and work restrictions. Also, knowledge of the actual composition will be required information for the analysis that is needed to remove tanks from the Watch List. Similarly, the rate of generation and release of gases is required information for performing safety analysis, developing controls, designing equipment, and closing safety issues. To determine release rate, both the gas concentrations and the dome space ventilation rates (exhauster flow rate or passive dome/atmosphere exchange rate) are needed. Therefore, to quickly verify waste tank categorization or to provide additional characterization for tanks with installed gas monitoring, a temporary, portable standard hydrogen monitoring system is needed that can be used to measure gas compositions at both high and low sensitivities.

251

Variable geometry gas turbines for improving the part-load performance of marine combined cycles - Gas turbine performance  

The part-load performance of gas and steam turbine combined cycles intended for naval use is of great importance, and it is influenced by the gas turbine configuration and load control strategy. This paper is aimed at quantifying the effects of variable geometry on the gas turbine part-load performance. Subsequently, in another paper, the effects of variable geometry on the part-load performance for combined cycles used for ship propulsion will be presented. Moreover, this paper is aimed at developing methodologies and deriving models for part-load simulations suitable for energy system analysis of various components within gas turbines. Two different gas turbine configurations are studied, a two-shaft aero-derivative configuration and a single-shaft industrial configuration. When both gas turbine configurations are running in part-load using fuel flow control, the results indicate better part-load performance for the two-shaft gas turbine. Reducing the load this way is accompanied by a much larger decrease in exhaust gas temperature for the single-shaft gas turbine than for the two-shaft configuration. As used here, the results suggest that variable geometry generally deteriorates the gas turbine part-load performance.

252

Investigations on operation of CI engine using producer gas and rice bran oil in mixed fuel mode  

A naturally aspirated multi cylinder diesel genset (DG) was operated successfully with mixed fuels (fossil-diesel (FD), refined rice bran oil (RRBO) and producer gas from a wood gasifier). Performance of DG set in FD, dual fuel mode (FD+RRBO in different proportion and FD+producer gas) and mixed fuels mode (with preheated blend of 75% RRBO+FD and producer gas) at different engine load conditions are presented in this paper. Performance of DG was evaluated in terms of specific energy consumption (SEC), brake thermal efficiency, exhaust gas temperature and exhaust gas composition. Study revealed that blends containing up to 75% RRBO with FD could be used as engine fuel without any adverse effect on the engine. The blend of RRBO and FD was preheated to 60 C before use in the compression ignition (CI) engine. In general, exhaust gas temperature and SEC increased in all the three modes compared to FD. However, break thermal efficiency decreased. It may be due to lower calorific value of RRBO and producer gas. It was observed that at 84% engine load having 18.4:1 compression ratio (CR) and operating in dual fuel mode (FD+producer gas), the concentration of pollutants like carbon monoxide (CO), carbon dioxide (CO{sub 2}), nitric oxide (NO), nitrogen dioxide (NO{sub 2}) reduced by 55%, 19.7%, 82% and 83%, respectively, while hydrocarbon (HC) increased by 67.2% as compared to FD. Similarly at 84% engine load having 17:1 CR and operating in dual fuel mode (FD+RRBO), the concentration of pollutant like CO, CO{sub 2} and HC reduced by 60%, 0.86% and 91%, respectively. However, NO{sub x} increased by 23.48% as compared to FD. In mixed fuel mode (preheated blends of RRBO+FD in the proportion of 3:1 and producer gas) at 84% engine load having 18.4:1 CR, the concentration of pollutants like HC, NO and NO{sub 2} reduced by 48.28%, 61.57% and 80.48%, respectively, while CO increased by 16.31% as compared to FD. In addition to the findings on environmental aspects, the study also proved that the diesel engine could be run safely in mixed fuel mode (53% producer gas, rest RRBO and FD at the ratio of 3:1 and heated at 60 C). (author)

253

Bench-scale biofilter for removing ammonia from poultry house exhaust.  

A bench-scale biofilter was evaluated for removing ammonia (NH3) from poultry house exhaust. The biofilter system was equipped with a compost filter to remove NH3 and calcium oxide (CaO) filter to remove carbon dioxide (CO2). Removal of NH3 and CO2 from poultry house exhaust could allow treated air with residual heat to be recirculated back into the poultry house to conserve energy during winter months. Apart from its use as a plant nutrient, NH3 removal from poultry house exhaust could lessen the adverse environmental impacts of NH3 emissions. Ammonia and CO2 were measured daily with gas detector tubes while temperatures in the poultry pen and compost filter were monitored to evaluate the thermal impact of the biofilter on treated air. During the first 37 days of the 54-day study, exhaust air from 33 birds housed in a pen was treated in the biofilter; for the final 17 days, NH3-laden exhaust, obtained by applying urea to the empty pen was treated in the biofilter. The biofilter system provided near-complete attenuation of a maximum short-term NH3 concentration of 73 ppm. During the last 17 days, with a mean influent NH3 concentration of 26 ppm, the biofilter provided 97% attenuation. The CaO filter was effective in attenuating CO2. Compared with a biofilter sized only for NH3 removal, an oversized biofilter would be required to provide supplemental heat to the treated air through exothermic biochemical reactions in the compost. The biofilter could conserve energy in poultry production and capture NH3 for use as plant nutrient. Based on this study, a house for 27,000 broilers would require a compost filter with a volume of approximately 34 m3. PMID:12602826

254

Automatic temperature control method of shipping can  

The present invention provides a method of rapidly and accurately controlling the temperature of a shipping can, which is used upon shipping inspection for a nuclear fuel assembly. That is, a measured temperature value of the shipping can is converted to a gas pressure setting value in a jacket of the shipping can by conducting a predetermined logic calculation by using a fuzzy logic. A gas pressure control section compares the pressure setting value of a fuzzy estimation section and the measured value of the gas pressure in the jacket of the shipping can, and conducts air supply or exhaustion of the jacket gas so as to adjust the measured value with the setting value. These fuzzy estimation section and gas pressure control section control the gas pressure in the jacket of the shipping can to control the water level in the jacket. As a result, the temperature of the shipping can is controlled. With such procedures, since the water level in the jacket can be controlled directly and finely, temperature of the shipping can is automatically controlled rapidly and accurately compared with a conventional case. (I.S.).

255

Performance of a diesel engine with thermally insulated combustion chamber  

The main objective of this work was to study the performance of a diesel engine with insulated combustion chamber surfaces. The piston of the test engine was insulated by incorporating an air-gap between the crown made of nimonic and the piston body. The cylinder liner was coated externally with partially stabilized zirconia (PSZ). The cylinder head and valves were insulated by coating them with a layer of PSZ. Due to this semi-adiabatic nature of the engine, the average gas and metal surface temperatures were higher. It was also studied whether these high temperatures allowed the use of fuels of low cetane number. Tests with adiabatic engine indicated higher levels of energy in the engine exhaust which could be utilized by employing exhaust heat recovery methods. The cycle average gas temperatures and metal surface temperatures increased substantially with insulation of the combustion chamber. This enabled the use of low cetane fuels in this engine. Lower volumetric efficiency and higher frictional losses were observed.

256

TransCanada PipeLines` operations monitoring system  

TransCanada PipeLines` operations monitoring system (OPSMON) which went into effect in 1995 was discussed. OPSMON is a system of seven interrelated modules of historical, real time and forecasted data that allows for better operations and maintenance management of its pipelines and gas turbines. Currently, TransCanada uses about 2131 MW of compression power, of which 96 per cent is supplied by gas turbines. TransCanada has a large fleet of 34 Rolls Royce Industrial AVONS and 32 RB211s. It also has a fleet of 11 LM1600s and 8 LM2500s. TransCanada PipeLines uses OPSMON to manage its fleet of 128 turbine driven compressor units as efficiently as possible. OPSMON is a remote control system which monitors the units and schedules overhauls. It is also capable of tracking and analyzing shutdown causes. OPSMON focuses on the operation of the pipeline without interfering with the gas transmission or the control process. The system is based on gas turbine process measurements such as gas turbine speeds, gas generator exhaust gas temperature, gas turbine output power, inlet air temperature and barometric pressure.

257

Selective catalytic reduction of nitrogen oxides from exhaust of lean burn engine over in-situ synthesized Cu-ZSM-5/cordierite.  

ZSM-5 zeolite was in-situ synthesized successfully on the surface of honeycomb cordierite substrate, certified by XRD and SEM techniques. Good thermal and hydrothermal stability of ZSM-5/cordierite could be obtained because of the in-situ synthesis method. Copper ion-exchanged ZSM-5/cordierite was studied as catalyst for selective catalytic reduction of nitrogen oxides. For practical reasons, the catalytic testing experiments were preformed on a real lean burn engine. Unburned hydrocarbons and carbon monoxide in the exhaust were directly used as reductants for NOx reduction. Cu-ZSM-5/cordierite exhibited high catalytic activity, and at 673 K the maximal NOx conversion to N2 could reach 50% at gas hourly space velocity (GHSV) of about 25 000 h(-1). Hydrocarbons and carbon monoxide in the exhaust could also be purified at the same time. As expected, Cu-ZSM-5/cordierite catalyst exhibited good duration and antipoison properties. When traces of lanthanum were introduced to Cu-ZSM-5/cordierite catalyst as a modifier, the activated temperature of the catalyst could be decreased and the temperature window with high NOx conversions broadened. Cu-ZSM-5/ cordierite and LaCu-ZSM-5/cordierite were thought as promising automobile exhaust catalysts under lean conditions. Copper is the main active component in the Cu-ZSM-5/ cordierite catalyst and Cu(II), which was found in the catalyst during the proceeding of reaction by XPS, is thought to be essential. On the basis of this, deNOx process over Cu-ZSM-5/cordierite is also discussed. PMID:15884384

258

Catalyst for the reduction of the ignition temperature of diesel soot  

This patent describes a catalytic composite effective in reducing the ignition temperature of diesel soot in an exhaust gas from a diesel engine. The composite consists essentially of a diesel soot filter selected from the group consisting of ceramic foam filter, monolithic honeycomb ceramic wall-flow filter, metallic mesh filter and metallic ribbon filter having deposited thereon at least one sulfur resistant refractory inorganic oxide selected from the group consisting of titania, zirconia, alumina treated with titania, alumina treated with zirconia, and mixtures thereof having deposited thereon at least one catalytic metal selected from the group consisting of Pt, Pd and Rh.

259

Method which controls the fuel metering in a diesel engine. Verfahren zur Steuerung der Kraftstoffzumessung bei einer Dieselbrennkraftmaschine  

The invention concerns a method and a device which generates a fuel metering signal M in a diesel engine based on parameters such as position of the accelerator, speed, lambda, exhaust gas temperature and torque. Depending on the accelerator position a fuel quantity request MW is set. This request and a second signal is transferred to a minimum selector whose output signal M will determine the quantity of metered fuel. The second signal comes from a pilot family of characteristics and depends on the speed. Under certain operational conditions the output signal of the pilot family of characteristics MW will be influenced by a regulator output signal MR.

260

The performance of current oxy-fuel combustion technology for secondary aluminum melting  

Higher thermal efficiency, lower exhaust gas flows, and lower superstructure temperatures have contributed to more widespread cost-effective use of oxygen-based firing. Operating characteristics of oxy-fuel firing are compared with air-fuel firing for the secondary melting of aluminum scrap. Typical performance gains resulting from oxy-fuel firing are established for rotary, reverberatory and well-type aluminum furnaces. Representative examples are presented in detail. The improvements in thermal performance of a non-axisymmetric self-cooling oxy-fuel burner providing uniform heat transfer to larger melt areas are demonstrated for aluminum furnaces.

 
 
 
 
261

Electrically heated DPF start-up strategy  

An exhaust system that processes exhaust generated by an engine has a diesel particulate filter (DPF) that is disposed downstream of the engine and that filters particulates in the exhaust. An electrical heater is disposed upstream of the DPF and selectively heats the exhaust to initiate combustion of the particulates. Heat generated by combustion of particulates in the heater induces combustion of particulates within the DPF. A control module selectively enables current flow to the electrical heater for an initial period of a DPF regeneration cycle, and limits exhaust flow while the electrical heater is heating to a predetermined soot combustion temperature.

262

Mathematical modelling of flue gas tempered flames produced from pulverised coal fired with oxygen  

The combustion of pulverised coal in conventional utility boilers contributes significantly to global CO{sub 2} emissions. Because atmospheric air is used as the combustion medium, the exhaust gases of conventional pulverised coal fired utility boilers contain approximately 15 % CO{sub 2}. This relatively low concentration makes separating and recovering CO{sub 2} a very energy-intensive process. This process can be simplified if N{sub 2} is eliminated from the comburent before combustion by firing the pulverised coal with pure oxygen. However, this concept will result in very high flames temperatures. Flue gas recirculation can be used to moderate the flame temperature, whilst generating a flue gas with a CO{sub 2} concentration of 95 %. In this presentation, both experimental and modelling work will be described. The former deals with identifying the issues related to the combustion of pulverised coal in simulated turbine exhaust gas, particularly with respect to stability, burnout and pollutant emissions. The second part of this presentation describes mathematical modelling of type 2 as well as type 1 swirling pulverised coal flames. Future work will concentrate on high CO{sub 2} levels environments. (orig.)

263

Waste oil heater  

An improved waste oil heater is disclosed that includes a vaporizer pan having a mounting ring, a replaceable aluminum foil piece mounted on the ring to form the bottom of the pan and a member mounted on the ring to provide threads, a tool threadingly engageable with the threaded ring member for breaking the pan loose from the bottom wall of a burner pot and removing the ring with caked residue thereon for purposes of cleaning, the burner pot having a novel arrangement of apertures for flow of air into the pot, and solid state electronic control apparatus to control the feed of waste oil that automatically compensates for variations in viscosities and caloric values found in a variety of used oils and automatically discontinues the feed in the event the flame in the burner pot goes out. A thermocouple in the exhaust gas stream in the heater or in the stack senses the exhaust gas temperature and the control circuit operates the motor of the pump to feed oil to the pan at a fast or slow rate as determined by a room thermostat and the sensed stack gas temperature. The feeding of oil by the pump is controlled by the thermostat which alters the effect of the thermocouple by requiring a higher thermocouple voltage to produce slow feeding when the thermostat calls for more heat to be produced.

264

Propagation of 632.8 nm and 4.67 µm laser beams in a turbulent flow containing CO2 and H2O at high temperatures  

Laser based missile defence systems (DIRCM) are being increasingly employed on aircraft. In certain circumstances the laser must pass through the exhaust gases of the aircraft engine. In order to predict the degree of divergence and dispersion of the laser, an understanding of the exhaust gas structure and its influence is required. Specifically the effect of parameters such as temperature, carbon dioxide, turbulence intensity and length scales as well as the laser beam wavelength and beam diameter. A parametric study under laboratory controlled conditions was undertaken to examine these effects. The results of beam propagation through high temperature turbulent flows and for various CO2 and H2O concentrations are presented in this paper for wavelengths 632.8 nm and 4.67 ?m. It was found that the beam displacement showed an approximate inverse square relationship to temperature. At high combustion temperatures the 632.8 nm beam was significantly broken-up and dispersed. Displacement of both beams appeared to be asymptotic above 600°C. Carbon dioxide absorption effects were found not to significantly influence the beam displacement at the wavelengths and temperatures studied. Quantifying these effects at high temperatures will assist with the development of a parametrically based laser beam propagation model.

265

Solid-waste burning in the SWIFT. [Solid Waste Incineration Facility for Testing  

The Solid Waste Incineration Facility for Testing (SWIFT) has operated for 400 hours and burned 25,000 lb of waste. After the facility startup in October 1981, three week-long campaign runs were conducted. During these tests, the incinerator processed a wide variety of simulated (nonradioactive) waste at rates of 300 to 400 lb/h. The resulting ash reduced the storage volume of the waste by a factor of 20. The off-gas treatment successfully cooled the exhaust from 1000 to 180/sup 0/C and filtered particulates from the gas stream. Cleaned off-gas was released to the atmosphere at 100/sup 0/C. Monitoring of the exhaust gas determined that pollutant and particulate concentrations were below South Carolina and Federal limits. A few areas need improvement, such as more adequate ash removal, better temperature control, and reduced air in-leakage. Performance of the equipment and materials of concentration was very good with only minor exceptions. This report contains extensive information on incinerator operation and data from burning tests.

266

Radioactive gas measuring device  

The radioactive gas measuring device comprises an introducing means for introducing radioactive gas, a sampling vessel, a measuring device for introducing and measuring radioactive gas, a gas bag for storing the radioactive gas after the measurement, an exhaustion device for exhausting the inside of the gas bag and containing the exhausted gas in a tank and a sensor for operating the exhaustion device upon reaching a predetermined value. The radioactive gas is stored in a gas bag after the measurement, and the pressure of the radioactive gas is kept stable, to improve the accuracy of the measurement. Further, when the amount of the stored radioactive gas is increased after the measurement, and the volume of the gas bag reaches a predetermined value, since the exhaustion device is operated by the sensor, the operation of the measuring device can be simplified. Then, the measurement for the radioactive gas can be conducted stably at high accuracy, thereby enabling to measure an absolute value of the impurity. The measurement for the impurity of the radioactive gas can be remarkably facilitated in the site of medical therapy. (N.H.).

267

Hydrogen-or-Fossil-Combustion Nuclear Combined-Cycle Systems for Base- and Peak-Load Electricity Production  

A combined-cycle power plant is described that uses (1) heat from a high-temperature nuclear reactor to meet base-load electrical demands and (2) heat from the same high-temperature reactor and burning natural gas, jet fuel, or hydrogen to meet peak-load electrical demands. For base-load electricity production, fresh air is compressed; then flows through a heat exchanger, where it is heated to between 700 and 900 C by heat provided by a high-temperature nuclear reactor via an intermediate heat-transport loop; and finally exits through a high-temperature gas turbine to produce electricity. The hot exhaust from the Brayton-cycle gas turbine is then fed to a heat recovery steam generator that provides steam to a steam turbine for added electrical power production. To meet peak electricity demand, the air is first compressed and then heated with the heat from a high-temperature reactor. Natural gas, jet fuel, or hydrogen is then injected into the hot air in a combustion chamber, combusts, and heats the air to 1300 C-the operating conditions for a standard natural-gas-fired combined-cycle plant. The hot gas then flows through a gas turbine and a heat recovery steam generator before being sent to the exhaust stack. The higher temperatures increase the plant efficiency and power output. If hydrogen is used, it can be produced at night using energy from the nuclear reactor and stored until needed. With hydrogen serving as the auxiliary fuel for peak power production, the electricity output to the electric grid can vary from zero (i.e., when hydrogen is being produced) to the maximum peak power while the nuclear reactor operates at constant load. Because nuclear heat raises air temperatures above the auto-ignition temperatures of the various fuels and powers the air compressor, the power output can be varied rapidly (compared with the capabilities of fossil-fired turbines) to meet spinning reserve requirements and stabilize the electric grid. This combined cycle uses the unique characteristics of high-temperature reactors (T>700 C) to produce electricity for premium electric markets whose demands can not be met by other types of nuclear reactors. It may also make the use of nuclear reactors economically feasible in smaller electrical grids, such as those found in many developing countries. The ability to rapidly vary power output can be used to stabilize electric grid performance-a particularly important need in small electrical grids.

268

Exhaust gas purification device  

The exhaust gas purification device includes an exhaust manifold , a purification cylinder connected with the exhaust manifold through a first honey-comb shaped catalyst, and a second honeycomb shaped catalyst positioned at the rear portion of the purification cylinder. Each catalyst is supported by steel wool rings including coarse and dense portions of steel wool. The purification device further includes a secondary air supplying arrangement.

269

D0 Vent Stacks  

There are two nitrogen/argon exhaust headers in the D0 cryogenic piping system, one for the liquid argon dewar and another for the three argon calorimeters. These headers serve two functions, venting both nitrogen exhaust from the cooling loops and cold argon gas should any argon vessel blow a relief. These headers are vacuum jacketed until they exit the building. At that point, uninsulated exhaust stacks direct the flow into the atmosphere. This note deals with the these stacks.

270

Power recovery from waste heat in modern turboexpander plants  

The object of this study is to determine the feasibility and cost of installing a power recovery system in an existing gas processing plant. The power generated by the system is to be used to drive a residue gas compressor, a refrigeration compressor and the heat medium circulating pump, each having its own expander driver. For this purpose the heat from the exhaust of a number of gas turbines is to be combined to provide a total 75 MM Btu/hr. heat energy. Because of safety reasons, Freon 12 has been chosen for the working fluid. The condensing media is water at a design temperature of 80 degrees F. The process conditions for the cycle and the duties of the major equipments are described.

271

An integrated system combining chemical looping hydrogen generation process and solid oxide fuel cell/gas turbine cycle for power production with CO2 capture  

In this paper, the solid oxide fuel cell/gas turbine (SOFC/GT) cycle is integrated with coal gasification and chemical looping hydrogen generation (CLHG) for electric power production with CO2 capture. The CLHG-SOFC/GT plant is configurated and the schematic process is modeled using Aspen Plus software. Syngas, produced by coal gasification, is converted to hydrogen with CO2 separation through a three-reactors CLHG process. Hydrogen is then fueled to SOFC for power generation. The unreacted hydrogen from SOFC burns in a combustor and drives gas turbine. The heat of the gas turbine exhaust stream is recovered in HRSG for steam bottoming cycle. At a system pressure of 20 bar and a cell temperature of 900 degreeC, the CLHG-SOFC/GT plant has a net power efficiency of 43.53% with no CO2 emissio...

272

Development of Micro Gas Turbine Combustor with a Recirculation Zone Induced by an Upward Swirl  

A new low NOx combustor for kerosene-fueled micro gas turbine was proposed, and the combustion characteristics of prototype combustor were investigated. The new combustor consisted of a primary and a secondary combustion zones, and they were connected by a throat. In order to enhance the recirculation flow in a primary combustion zone, a swirler was set between the primary and secondary combustion zones. Combustion air was introduced through the swirler and forced to flow upward to the combustor bottom, from which the fuel spray was supplied through a nozzle. To achieve high combustion stability and low emission in wide fuel-air ratio, the optimum configuration of the primary combustion zone were investigated. The optimum one was found out by measuring the fundamental combustion characteristics such as lean combustion limit, flame luminosity, exhaust gas composition and combustion gas temperature.   

273

Energy conservation technologies based on thermodynamic principles  

In order to reduce CO{sub 2} emission to prevent global warming, the most promising way for electric generation in the Northeast Asia is to introduce cogeneration and {open_quotes}repowering{close_quotes} technologies based on high temperature gas turbines fueled by natural gas. Especially the old type coal burning boiler-steam turbine plants should be retrofit by introducing gas turbines to become highly efficient combined cycle. Same technologies should be applied to the old garbage incineration plants and/or even to the nuclear power plants. The exhaust heat or steam should become much increased and it should be utilized as the process heat for industries or heat supply as the distinct heating or cooling for residential area. This paper introduces a brief survey of these new technologies.

274

Method of halting operation of fuel cell  

As a fuel cell installation becomes large in scale, excessive differential pressure is implied to its electrodes, inviting a high degree of danger of troubles resulting in damaging the electrodes or scattering phosphate. In this invention, it was arranged that an exhaust gas supply valve and an exhaust gas discharge valve were installed in exhaust gas supply lines from an anode chamber to a turbine in order to eliminate the imbalance between the exhaust gas discharge from the anode chamber and that from the cathode chamber which was a major cause of the imbalance of gas pressure and the exhaust gas supply valve was closed and the exhaust gas discharge valve was opened at the time when the operation was halted. Furthermore, an oxidizer discharge valve was installed in a compressor discharge line for opening the oxidizer discharge valve at the time when the operation was halted and by this, it was arranged that damage of the compressor was prevented through releasing quickly the exhaust pressure of the compressor which was still running to some extent even after halting the operation. (2 figs)

275

Turbo-supercharger for internal combustion engines, particularly multiple exhaust gas turbo-supercharger for vehicle engines. Turbolader fuer Brennkraftmaschinen, insbesondere mehrflutiger Abgasturbolader fuer Motoren von Kraftfahrzeugen  

The invention refers to a turbo-supercharger for internal combustion engines, particularly a multiple exhaust gas turbo-supercharger for vehicle engines, with a radial turbine wheel and exhaust gas inlets surrounding the turbine wheel in the turbine housing spirally. Further, a control device is provided to ensure an optimum turbine loading for different conditions of the engine. When the engine load is high, part of the exhaust gas is taken past in the bypass on the turbine wheel. The purpose of the invention is to create such an exhaust gas turbo-supercharger so that correct regulation of the charging system is guaranteed in all speed ranges. The invention solves this problem by providing a bypass duct concentrically surrounding the spiral exhaust gas inlet in the turbine housing, and fitting a valve control at the end of the bypass, which is actuated by the amount of the charging pressure or the amount of the exhaust gas pressure. This makes it possible to take the quantity of exhaust gas past in the bypass without affecting the 'floods' loading the turbine, by simple means.

276

Skutterudite Thermoelectric Generator for Electrical Power Generation from Automotive Waste Heat  

Filled skutterudites are state-of-the- art thermoelectric (TE) materials for electrical power generation from waste heat. They have suitable intrinsic transport properties as measured by the thermoelectric figure of merit ZT = S^2?T/? (S = Seebeck coefficient, ? = electrical conductivity, T = temperature, and ? = thermal conductivity) and good mechanical strength for operation at vehicle exhaust gas temperatures of >550 C. We have demonstrated TE electrical power generation on a production test vehicle equipped with a fully functional prototype TE generator (TEG). It was assembled with TE modules fabricated from filled skutterudites synthesized at GM. Our results and analysis show that improvement in total power generated can be achieved by enhanced thermal and electrical interfaces and contacts. A substantial T decrease along the exhaust gas flow results in a large variation of voltage, current, and power output for each TE module depending on its position in the module array. Total TEG output power depends directly on the position-dependent T profile via the temperature dependence of both ZT and Carnot efficiency. Total TEG power output also depends on how the modules are connected in parallel or series combinations because mismatch in output voltage and/or internal resistance among the modules degrades the performance of the entire array. Uniform T profiles and consistent TE module internal resistances improve overall TEG performance.

277

Effect of EGR on spray development, combustion and emissions in a 1.9L direct-injection diesel engine  

The spray development, combustion and emissions in a 1.9L optical, four-cylinder, direct-injection diesel engine were investigated by means of pressure analysis, high-speed cinematography, the two-color method and exhaust gas analysis for various levels of exhaust gas recirculation (EGR), three EGR temperatures (uncontrolled, hot and cold) and three fuels (diesel, n-heptane and a two-component fuel 7D3N). Engine operating conditions included 1,000 rpm/idle and 2,000 rpm/2bar with EGR-rates ranging from 0 to 70%. Independent of rate, EGR was found to have a very small effect on spray angle and spray tip penetration but the auto-ignition sites seemed to increase in size and number at higher EGR-rates with associated reduction in the flame luminosity and flame temperature, by, say, 100K at 50% EGR. The emission tests confirmed that for different intake temperatures and three fuels, increasing the EGR-rate leads to reduced NO{sub x} and O{sub 2} levels but increased soot, CO, CO{sub 2}, and HC concentrations. Cold EGR resulted in lower NO{sub x} emissions at EGR-rates below 30% but at higher rates hot EGR seems to offer marginal improvements relative to cold EGR and significant NO{sub x} reduction compared to the uncontrolled EGR case.

278

Direct Measurement of EGR Cooler Deposit Thermal Properties for Improved Understanding of Cooler Fouling  

Exhaust gas recirculation (EGR) cooler fouling has become a significant issue for compliance with NOX emissions standards. This paper reports results of a study of fundamental aspects of EGR cooler fouling. An apparatus and procedure were developed to allow surrogate EGR cooler tubes to be exposed to diesel engine exhaust under controlled conditions. The resulting fouled tubes were removed and analyzed. Volatile and non-volatile deposit mass was measured for each tube. Thermal diffusivity of the deposited soot cake was measured by milling a window into the tube and using the Xenon flash lamp method. The heat capacity of the deposit was measured at temperatures up to 430 C and was slightly higher than graphite, presumably due to the presence of hydrocarbons. These measurements were combined to allow calculation of the deposit thermal conductivity, which was determined to be 0.041 W/mK, only ~1.5 times that of air and much lower than the 304 stainless steel tube (14.7 W/mK). The main determinant of the deposit thermal conductivity is density, which was measured to be just 2% that of the density of the primary soot particles (or 98% porous). The deposit layer thermal resistance was calculated and compared with estimates of the thermal resistance calculated from gas temperature data during the experiment. The deposit properties were also used to further analyze the temperature data collected during the experiment.

279

The effects of detoxification of domestic gas on suicide in the United States  

As domestic gas was detoxified in the United States, the rate of suicide by domestic gas decreased. During this time period (1950-60), there was a parallel increase in the per capita ownership of cars and an accompanying increase in the rate of suicide by motor vehicle exhaust. However, displacement of suicide method from domestic gas to car exhaust occurred only for males and not for females.

280

Hydromethane: A bridge towards the hydrogen economy or an unsustainable promise?  

Last decade enthusiasm about hydrogen-based economy on FC has partially been lost and spotlight is now back on using pure hydrogen or hydrogen mixtures in ICE. Pure hydrogen use in spark ignition (SI) ICE requires a dedicated engine design to optimize the high speed flame and the high pressure and temperature inside the combustion chamber. But, on the other end, may lead to high exhaust emissions of nitrogen oxides NOx. Moreover, hydrogen fueled vehicles also suffer of a very low mileage due to the very low energy density of the fuel, since hydrogen as a compressed gas at 200 atmospheres and ambient temperature has around 5% of the energy of gasoline of the same volume. All these motivations, together with the now capillary diffusion of natural gas (NG) distribution for residential and tra...

 
 
 
 
281

Computer Program for Calculation of a Gas Temperature Profile by Infrared Emission: Absorption Spectroscopy  

A computer program to calculate the temperature profile of a flame or hot gas was presented in detail. Emphasis was on profiles found in jet engine or rocket engine exhaust streams containing H2O or CO2 radiating gases. The temperature profile was assumed axisymmetric with an assumed functional form controlled by two variable parameters. The parameters were calculated using measurements of gas radiation at two wavelengths in the infrared. The program also gave some information on the pressure profile. A method of selection of wavelengths was given that is likely to lead to an accurate determination of the parameters. The program is written in FORTRAN IV language and runs in less than 60 seconds on a Univac 1100 computer.

282

Phase change thermal energy storage methods for combat vehicles. Final report on Phase 1  

Three alternative cooling methods, based on latent heat absorption during phase changes, were studied for potential use in combat vehicle microclimate temperature control. Metal hydrides absorb heat as they release hydrogen gas. Plastic crystals change from one solid phase to another, absorbing heat in the process. Liquid air boils at cryogenic temperature and absorbs additional sensible heat as the cold gas mixes with the microclimate air flow. System designs were prepared for each of the three microclimate cooling concepts. These designs provide details about the three phase change materials, their containers and the auxiliary equipment needed to implement each option onboard a combat vehicle. The three concepts were compared on the basis of system mass, system volume, and the energy required to regenerate them after use. Metal hydrides were found to be the lightest and smallest option by a large margin. The energy needed to regenerate a hydride thermal-storage system can be extracted from the vehicle's exhaust gases.

283

Validation of a blowby model using experimental results in motoring condition with the change of compression ratio and engine speed  

Blowby and gas flow through the cylinder-piston-ring crevices are phenomena that affect the engine performance and exhaust emissions. Also these phenomena influence the cylinder pressure and temperature and the charge amount during a cycle. The study and validation of a sub-model for these phenomena in the absence of engine combustion deducts all effects arisen from the combustion event. During the current study, blowby sub-model and gas flow through crevices under motoring conditions has been noticed using a volume-orifice theory and the experimental results measured from a research engine. Blowby geometric parameters, consisting of a few critical cross-section areas (orifice areas) and volumes (top land and inter-ring crevice volumes), were measured in ambient temperature and corrected f...

284

Development of a Pellet Catalytic Combustor for a Small Scale Generation System Using Near Infrared Ray Irradiation  

Several geometric types of the small scale catalytic combustors applying the pellet catalysts as both the heat source and the emitter for infrared ray generation were developed in order to investigate the catalytic combustion phenomenon and the effective operation conditions for the TPV generation system. The results of temperature measurements and exhaust gas analyses showed that there were the optimal width and length of the combustor geometry for the high combustion efficiency and the reduction of the residual CO concentration. The ultraviolet and visible spectral measurements showed that the surface chemical reaction was predominant in the catalytic combustion and the gas phase reaction which causes higher temperature and higher reaction rate than those of the surface reaction scarcely occurred in the developed combustor. The near infrared spectral measurements showed that the pellet catalysts in the combustor could play the role of the emitter for the TPV generation system.   

285

Effect of water injection on nitric oxide emissions of a gas turbine combustor burning natural gas fuel  

The effect of direct water injection on the exhaust gas emissions of a turbojet combustor burning natural gas fuel was investigated. The results are compared with the results from similar tests using ASTM Jet-A fuel. Increasing water injection decreased the emissions of oxides of nitrogen (NOX) and increased the emissions of carbon monoxide and unburned hydrocarbons. The greatest percentage decrease in NOX with increasing water injection was at the lowest inlet-air temperature tested. The effect of increasing inlet-air temperature was to decrease the effect of the water injection. The reduction in NOX due to water injection was almost identical to the results obtained with Jet-A fuel. However, the emission indices of unburned hydrocarbons, carbon monoxide, and percentage nitric oxide in NOX were not.

286

Laser-induced breakdown spectroscopy of alkali metals in high-temperature gas  

Laser-induced breakdown spectroscopy (LIBS) measurements of alkali in the high-temperature exhaust of a glass furnace show an attenuation of the Na and K LIBS signals that correlates with the stoichiometry of the bath gas surrounding the spark. The results are explained as being due to (1) a strong increase in the concentration of atomic Na and K, resulting in neutral line signal absorption by these atoms, and to (2) a change of phase of the major Na- and K-containing species from an aerosol to a gaseous phase when the gas mixture becomes fuel rich, resulting in a reduced LIBSemission intensity. LIBS sampling at lower temperatures, or in a consistently oxidizing environment, or both are suggested strategies for circumventing these difficulties.

287

Chimney reconstruction systems. New heating systems and old chimneys do not harmonize. Schornstein-Sanierungssysteme. Neue Heizungen und alte Schornsteine vertragen sich nicht  

New burner systems with lower exhaust gas temperatures resulted in increased reconstruction of chimneys within the last years. The traditional materials for reconstruction such as leight weight concrete shells or flexible special steel pipes proved to be insufficient. Nowadays rigid special steel pipes with and without heat insulating shell as well as fire-clay pipes, which are applied with acid-resisting cement and backfilled with insulating layer. Recusist special glass is regarded as a relatively new, efficient reconstructional material. In addition to their corrosion resistance, Recusist is gas- and condensate tight resistant to temperature change, favorable with regard to flow, non-porous (and thus, easily to clean) as well as not harmful to the environment. (orig.).

288

Thermally integrated fuel processor design for fuel cell applications  

Effective thermal integration could enable the use of compact fuel processors with PEM fuel cell-based power systems. These systems have potential for deployment in distributed, stationary electricity generation using natural gas. This paper describes a concept wherein the latent heat of vaporization of H"2O is used to control the axial temperature gradient of a fuel processor consisting of an autothermal reformer (ATR) with water gas shift (WGS) and preferential oxidation (PROX) reactors to manage the CO exhaust concentration. A prototype was experimentally evaluated using methane fuel over a range of external heat addition and thermal inputs. The experiments confirmed that the axial temperature profile of the fuel processor can be controlled by managing only the vapor fraction of the pre...

289

High-temperature burner-duct-recuperator (HTBDR) system low-pressure seal development: Final report  

Development has been completed of a ceramic recuperator and its companion high-temperature preheated combustion air burner. The system is designed to operate in a variety of industrial flue gas streams with exhaust temperatures up to 2500/sup 0/F. The ceramic recuperator provides combustion air preheated up to 2000/sup 0/F to the high-temperature burner. Development of low-pressure seals to join the ceramic recuperator components was performed as an integral part of the program. While operating at high temperatures, the recuperator requires seals effective in minimixing both leakage and stress concentrations in the joints between ceramic components. Seal design, composition, leakage performance, and seal characterization were evaluated for cement, glass, and fiber packing seals. Laboratory studies have demonstrated that effective, low-leakage seals were developed and incorporated into the HTBDR industrial design.

290

Device for controlling the supercharging air pressure in an internal combustion engine provided with an exhaust gas turbo-supercharger. Vorrichtung zur Regelung des Ladeluftdruckes bei einer mit einem Abgas-Turbolader versehenen Brennkraftmaschine  

The purpose of the invention is to create a device for controlling the supercharging air pressure on an internal combustion engine provided with an exhaust gas turbosupercharger, which responds directly and quickly to excessive temperatures in the combustion space and reduces the supercharging pressure accordingly. According to the invention, the problem is solved by the control device being controlled by the cylinder head temperature of the internal combustion engine. It is detected by a temperature dependent resistor and adjusts a setting device, by which the control device can be adjusted in the sense of increasing or reducing the maximum supercharging air pressure. A differential amplifier is interposed between the temperature-dependent resistor and the setting motor, from which a potentiometer situated in the control device is controlled. The control system is included in an integrated circuit.

291

Highly efficient heat recovery system for phosphoric acid fuel cells used for cooling telecommunication equipment  

To protect the global environment by using energy more efficiently, NTT is developing a phosphoric acid fuel cell (PAFC) energy system for telecommunication cogeneration systems. Fuel cells are used to provide electrical power to telecommunication equipment and the heat energy is used by absorption refrigerators to cool the telecommunication rooms throughout the year. We have recently developed a highly efficient system for recovering heat and water from the exhaust gases of a 200-kW (rated power) fuel cell. It is composed of a shell-and-tube type heat exchanger to recover high-temperature heat and a direct-contact cooler to recover the water efficiently and simply. The reformer and cathode exhaust gases from the fuel cell are first supplied to the heat exchanger and then to the cooler. The high-temperature (85-60 C) heat can be recovered, and the total efficiency including the heat recovered from the fuel-cell stack coolant can be improved by supplying the recovered heat to the dual-heat-input absorption refrigerator. The water needed for operating the fuel cell is also recovered from the exhaust gases. We are currently applying this heat and water recovery system to the PC25C-type fuel cell. Maximum total efficiency including electrical power efficiency is estimated to be 78% at the rated power of 200 kW: composed of 17% heat recovery for the fuel-cell stack coolant, 21% from the exhaust gas by improving the heat exchanger, and 40% from electrical conversion. Next, we plan to evaluate the usefulness of this heat recovery system for cooling telecommunication equipment. (orig.)

292

Experimental Investigation on Effect of Smoke Management System in a High-large Atrium  

In an atrium measured 120 m by 180 m by 36.5 m high, fire tests were conducted under 'natural filling' and 'mechanical exhaust' conditions by hot smoke test method. The fire size was 8 MW released by an ethanol pool of 3.6 m in diameter. The distribution of vertical temperature profiles above the fire source and the gas layer temperatures were measured. From these measurements, it was shown that the fans successfully exhausted hot smoke to control descending of hot smoke layer and temperature rising rate. The hot smoke layer can be maintained at about 30 m which was almost 2 times of hot layer height in 'natural filling' condition. The temperature risings in both conditions were too low to cause thermal damage to the structure, only 18.6 K and 12 K. The centerline temperature above the fire source and the height of hot smoke layer were calculated using the plume models. The calculated results agreed well with the conclusions obtained from the experiment results.

293

Analysis of Exhaust Gas Visibility in Iron Ore Sintering Plant  

Visible smoke of exhaust gas from iron ore sintering plants spoil the scenery around the works. In this paper, the mechanism of formation of visible smoke is discussed by detailed analysis of the exhaust gas components and dust in the Oita No. 1 sintering plant. The main substance of visible smoke was mist condensing in the air during the cooling of exhaust gas that contained 0.1 ppm of sulfuric acid (SO3). Sulfuric acid is considered to raise the dew point and so facilitate mist condensation, and to lower the vaporization of visible mist containing sulfuric acid solution. Dust in the exhaust gas is also considered to act as nucleation sites for mist condensation. This proposed mechanism was confirmed by the test remixing SOx-rich gas with desulfurization gas in the Nagoya No. 3 sintering plant. Long trails of visible smoke were observed by remixing SOx-rich gas with exhaust gas. In conclusion, in order to make exhaust gas invisible, it is not sufficient to enhance the dust collecting system: desulfurization equipment in the sintering plant is necessary.   

294

How to operate the fuel cell operating at a high temperature; Koon sadogata nenryo denchi no unten hoho  

The conventional composite power generation system consisting of coal gasification system and high temperature fuel cell has such disadvantage that the permanent catalyst poisoning of fuel electrode takes place, resulting in gradual decrease in cell voltage during the cell operation. This is due to a high concentration of H2S gas in the fuel at the inlet of the high temperature fuel cell. This invention solves the problem. The fuel gas produced by coal gasification is desulfurized by a dry type desulfurization system and then furthermore treated with the regeneration type desulfurization system before being fed to the high temperature fuel cell as the fuel. At the same time, the high temperature oxygen-containing exhaust gas from the cell is used for generating the desulfurizing agent in the regeneration type desulfurization system. Coal gas which was desulfurized by the dry system desulfurizer employing such desulfurizer as iron oxide to reduce H2S content to about 80 ppm is furthermore treated with the regeneration type desulfurization system employing Ni-type desulfurizer to lower the H2S content as low as 1 ppm. Resultingly the permanent catalyst poisoning of Ni electrode by H2S in the high temperature fuel cell can be prevented. So that the decrease in performance and durability can be minimized. 5 figs.

295

Studies on exhaust-gas-cleaning from wood chip driers  

Studies on cleaning the exhaust gas of chip driers were carried out employing water and aqueous soidum hydroxide as scrubbing solutions. In addition exhaust gas cleaning through indirect cooling was investigated. The decrease of the total carbon content in the exhaust gas through water-scrubbing was 55%, through aqueous sodium hydroxide 70% and through indirect cooling 18%. Investigations on the change in concentration of the terpenes ..cap alpha..-pinene, ..beta..-pinene, myrcene, ..delta../sup 3/-carene and camphene showed that these compounds followed closely the reduction efficiency measured for the total carbon content.

296

Corner heating in rectangular solid oxide electrochemical cell generators  

Disclosed is an improvement in a solid oxide electrochemical cell generator 1 having a rectangular design with four sides that meet at corners, and containing multiplicity of electrically connected fuel cells 11, where a fuel gas is passed over one side of said cells and an oxygen containing gas is passed into said cells, and said fuel is burned to form heat, electricity, and an exhaust gas. The improvement comprises passing the exhaust gases over the multiplicity of cells 11 in such a way that more of the heat in said exhaust gases flows at the corners of the generator, such as through channels 19.

297

Thermal chemical recuperation method and system for use with gas turbine systems  

A system and method for efficiently generating power using a gas turbine, a steam generating system (20, 22, 78) and a reformer. The gas turbine receives a reformed fuel stream (74) and an air stream and produces shaft power and exhaust. Some of the thermal energy from the turbine exhaust is received by the reformer (18). The turbine exhaust is then directed to the steam generator system that recovers thermal energy from it and also produces a steam flow from a water stream. The steam flow and a fuel stream are directed to the reformer that reforms the fuel stream and produces the reformed fuel stream used in the gas turbine.

298

Reaction kinetics and reactor modelling in the design of catalytic reactors for automotive exhaust gas abatement  

The tightening environmental legislation and technological development in automotive engineering form a challenge in reactor design of catalytic reactors for automotive exhaust gas abatement. The catalytic reactor is the heart of the exhaust aftertreatment processes, but it can be seen als...

299

Deaerator heat exchanger for combined cycle power plant  

This patent describes a combined cycle power plant. It comprises a steam turbine including an inlet portion for receiving motive steam and an exhaust portion for exhausting the motive steam that is spent by the steam turbine; a condenser connected to the exhaust portion of the steam turbine for receiving the spent motive steam and for condensing the spent motive steam to a supply of condensate; a gas turbine including an exhaust portion for exhausting waste heat that is produced by the gas turbine in the form of exhaust gases; a heat recovery steam generator connected between the exhaust portion of the gas turbine and the steam turbine, for receiving the waste heat exhausted by the gas turbine, for generating the motive steam from a supply of feedwater heated by the waste heat, and for supplying the motive steam to the steam turbine; a deaerator connected to the condenser for receiving the supply of condensate and for deaerating the condensate to provide the supply of feedwater to the heat recovery steam generator; and a heat exchanger.

300

Two stage sorption of sulfur compounds  

A two stage method for reducing the sulfur content of exhaust gases is disclosed. Alkali- or alkaline-earth-based sorbent is totally or partially vaporized and introduced into a sulfur-containing gas stream. The activated sorbent can be introduced in the reaction zone or the exhaust gases of a combustor or a gasifier. High efficiencies of sulfur removal can be achieved.

 
 
 
 
301

DEVELOPMENT OF A PROPORTIONAL SAMPLER FOR AUTOMOBILE EXHAUST EMISSIONS TESTING  

The report describes the development of a device that is capable of sampling gaseous emissions from automobiles. The device samples exhaust gases at a mass rate that is proportional to the total exhaust gas mass flow rate, which is measured using an ultrasonic vortex flowmeter. T...

302

ffmorm of 1~ Md C  

Jan 1, 1979 ... relation to the current energy situation, existing supply systems, and conservation ...... Use Direct Air Supply to Exhaust. Hoods. Use Exhaust Heat from Buildings for ...... lines, process fluid lines, air or gas ducts and other process ...... The north side is a good location for a kitchen, hall, stairway, closet, or ...

303

Hot-gas ingestion investigation of large-scale jet VTOL fighter-type ...  

The model was constructed almost entirely of stainless steel to withstand the high .... rolling take-off, in which case higher forward speeds would be involved. .... edge where they are not well shielded by the wing from the recirculating hot exhaust ... low-wing configuration forced the fountain of hot exhaust gas flowing upward ...

304

Selective NOx Recirculation for Stationary Lean-Burn Natural Gas Engines  

Nitric oxide (NO) and nitrogen dioxide (NO2) generated by internal combustion (IC) engines are implicated in adverse environmental and health effects. Even though lean-burn natural gas engines have traditionally emitted lower oxides of nitrogen (NOx) emissions compared to their diesel counterparts, natural gas engines are being further challenged to reduce NOx emissions to 0.1 g/bhp-hr. The Selective NOx Recirculation (SNR) approach for NOx reduction involves cooling the engine exhaust gas and then adsorbing the NOx from the exhaust stream, followed by the periodic desorption of NOx. By sending the desorbed NOx back into the intake and through the engine, a percentage of the NOx can be decomposed during the combustion process. SNR technology has the support of the Department of Energy (DOE), under the Advanced Reciprocating Engine Systems (ARES) program to reduce NOx emissions to under 0.1 g/bhp-hr from stationary natural gas engines by 2010. The NO decomposition phenomenon was studied using two Cummins L10G natural gas fueled spark-ignited (SI) engines in three experimental campaigns. It was observed that the air/fuel ratio ({lambda}), injected NO quantity, added exhaust gas recirculation (EGR) percentage, and engine operating points affected NOx decomposition rates within the engine. Chemical kinetic model predictions using the software package CHEMKIN were performed to relate the experimental data with established rate and equilibrium models. The model was used to predict NO decomposition during lean-burn, stoichiometric burn, and slightly rich-burn cases with added EGR. NOx decomposition rates were estimated from the model to be from 35 to 42% for the lean-burn cases and from 50 to 70% for the rich-burn cases. The modeling results provided an insight as to how to maximize NOx decomposition rates for the experimental engine. Results from this experiment along with chemical kinetic modeling solutions prompted the investigation of rich-burn operating conditions, with added EGR to prevent preignition. It was observed that the relative air/fuel ratio, injected NO quantity, added EGR fraction, and engine operating points affected the NO decomposition rates. While operating under these modified conditions, the highest NO decomposition rate of 92% was observed. In-cylinder pressure data gathered during the experiments showed minimum deviation from peak pressure as a result of NO injections into the engine. A NOx adsorption system, from Sorbent Technologies, Inc., was integrated with the Cummins engine, comprised a NOx adsorbent chamber, heat exchanger, demister, and a hot air blower. Data were gathered to show the possibility of NOx adsorption from the engine exhaust, and desorption of NOx from the sorbent material. In order to quantify the NOx adsorption/desorption characteristics of the sorbent material, a benchtop adsorption system was constructed. The temperature of this apparatus was controlled while data were gathered on the characteristics of the sorbent material for development of a system model. A simplified linear driving force model was developed to predict NOx adsorption into the sorbent material as cooled exhaust passed over fresh sorbent material. A mass heat transfer analysis was conducted to analyze the possibility of using hot exhaust gas for the desorption process. It was found in the adsorption studies, and through literature review, that NO adsorption was poor when the carrier gas was nitrogen, but that NO in the presence of oxygen was adsorbed at levels exceeding 1% by mass of the sorbent. From the three experimental campaigns, chemical kinetic modeling analysis, and the scaled benchtop NOx adsorption system, an overall SNR system model was developed. An economic analysis was completed, and showed that the system was impractical in cost for small engines, but that economies of scale favored the technology.

305

5th international exhaust gas and particulate emissions forum. Proceedings; 5. Internationales Forum Abgas- und Partikelemissionen. Beitraege  

The Proceedings of the 5th International Exhaust Gas and Particulate Emissions Forum contains 22 printed contributions as well as a CD-ROM. The titles of them are: (1) Diesel Emissions Control in the United States - 2010 and Beyond; (2) The MBE90 commercial vehicle engine for EPA '07 emissions regulations; (3) Concepts for engines and exhaust-gas cleaning systems for heavy duty trucks of the future; (4) HD Engine Technology for Near-Zero Emissions and Lowest Cost of Ownership; (5) (Partially-) Homogeneous Diesel Combustion; (6) Exhaust gas sensors for NOx storage catalysts and ammonia-SCR systems; (7) Sensors for modern exhaust gas after-treatment systems; (8) New reducing agents for low NOx-SCR Techno-logy; (9) Exhaust gas Aftertreatment on Lean Burn Gasoline Direct Injection Engines: The System of TWC and NOx-Storage Catalyst; (10) New Platinum/Palladium based catalyzed filter technologies for future passenger car applications; (11) Development of a Roadway Hydrocarbon Sorption Model and Characterization of a Novel PM Generator; (12) Requirements for current and future particulate measurement instrumentation from the point of view of the Physikalisch-Technische Bundesanstalt; (13) Standardized dilution conditions for gravimetric PM sampling - measures to assure results that correlate; (14) Particle Counting according PMP; (15) Future high-confidence measurement of diesel particulate emissions for approval and development; (16) New developments in optical instrumentation for exhaust gas; (17) Simultaneous Detection of Gaseous and Particulate Exhaust Components by Photoacoustic Spectroscopy; (18) Boundaries of modern exhaust gas instrumentation; (19) Raising quality and reducing application effort through efficient data input to the particulate filter load model for a EURO5 diesel car; (20) Stop-start operation of diesel engines - modified require-ment for exhaust gas after-treatment?; (21) Particulates emission with Biodiesel B30 impact on CSF management; (22) Diesel engine soot and NOx emission modelling. (orig)

306

Research on air intake an exhaust nozzle in HYPR project; HYPR project ni okeru intake nozzle no kenkyu  

This paper describes the research on air intake and exhaust nozzle in HYPR (Super/Hyper-Sonic Transport Propulsion System) project. HYPR project adopts the concept of CCE (combined cycle engine) composed of a turbojet engine and a ramjet engine. The air intake for flight in a mach range of 0-5 adopts a shock wave system composed of 6 shock waves to keep a total pressure recovery more than 81% at Mach 3 and more than 51% at Mach 5 under the condition of minimum bleed air flow rate. Since stable operation, high profitability and high environment adaptivity are required for CCE at Mach 0-5, the exhaust nozzle with a high thrust efficiency (more than 95% at Mach 5, more than 97% at Mach 3), and its moving mechanism and cooling structure (for maximum gas temperature of 1900 degrees C) are adopted, satisfying ICAO standard on exhaust jet noise. Study was made on aerodynamics of the nozzle at Mach 3 and 5, and its moving mechanism and cooling structure. Further development is indispensable for SST in the 21st century. (NEDO)

307

Application of Argonne's Glass Furnace Model to longhorn glass corporation oxy-fuel furnace for the production of amber glass.  

The objective of this project is to apply the Argonne National Laboratory's Glass Furnace Model (GFM) to the Longhorn oxy-fuel furnace to improve energy efficiency and to investigate the transport of gases released from the batch/melt into the exhaust. The model will make preliminary estimates of the local concentrations of water, carbon dioxide, elemental oxygen, and other subspecies in the entire combustion space as well as the concentration of these species in the furnace exhaust gas. This information, along with the computed temperature distribution in the combustion space may give indications on possible locations of crown corrosion. An investigation into the optimization of the furnace will be performed by varying several key parameters such as the burner firing pattern, exhaust number/size, and the boost usage (amount and distribution). Results from these parametric studies will be analyzed to determine more efficient methods of operating the furnace that reduce crown corrosion. Finally, computed results from the GFM will be qualitatively correlated to measured values, thus augmenting the validation of the GFM.

308

Gas-solid chromatographic analysis of automobile tailpipe emissions as a function of different engine and exhaust system modifications  

The authors developed a single, relatively short gas-solid chromatographic PLOT column and used it to separate aliphatic hydrocarbons, aromatic hydrocarbons and some inorganic gases (O{sub 2}, N{sub 2}, CO and CO{sub 2}) found in automobile exhaust. In the case of hydrocarbons, both aliphatic and aromatic components (up through alkylated-benzenes) were done in one run. Subambient temperature was needed for the oxygen-nitrogen separation, but they were easily resolved from each other and the other compounds present. The effects of different engine and exhaust system modifications on the level of compounds in the exhaust were tested. The concentrations of the emission gases varied considerably with changes in air/fuel ratio, coil voltage, use of catalytic converters and so forth. The results showed that the use of catalytic converter and a higher voltage coil tended to produce the most pronounced decreases in emissions of hydrocarbons and the catalytic converter produced the significant decrease in carbon monoxide concentrations. The results of the GSC analyses were compared to those of a commercial emission analyzer (i.e., sniffer). They showed similar trends and relative concentrations but somewhat different absolute concentrations. This may have been due to differences in the calibration of these methods.

309

The effects of Al{sub 2}O{sub 3}-TiO{sub 2} coating in a diesel engine on performance and emission of corn oil methyl ester  

Today, as a result of increase in oil prices, limited fossil fuel resources, environmental consideration and global warming, the methyl ester fuels have been focused on alternative fuels. Methyl ester fuels can be used more efficiently in low heat rejection engines (LHR), in which the temperature of combustion chamber is increased by creating a thermal barrier. In this study, the piston, cylinder head, exhaust and inlet valves of a diesel engine were coated with the ceramic material Al{sub 2}O{sub 3}-TiO{sub 2} by the plasma spray method. Thus, a thermal barrier was provided for the parts of the combustion chamber with these coatings. The effects of corn oil methyl ester that produced by the transesterification method, and No. D2 fuels' performance and exhaust emissions' rate were studied by using equal in every respect coated and uncoated engines. Tests were performed on the uncoated engine, and then repeated on the coated engine and the results were compared. A decrease in engine power and specific fuel consumption, as well as significant improvements in exhaust gas emissions (except NOx), were observed for all test fuels used in the coated engine compared with that of the uncoated engine. (author)

310

75 FR 35619 - Airworthiness Directives; Piper Aircraft, Inc. Models PA-32R-301T and PA-46-350P Airplanes  

...Directives; Piper Aircraft, Inc. Models...certain Piper Aircraft, Inc. Models...spot-welded, V-band exhaust coupling with...high-temperature gases inside the engine...2010-13-07 Piper Aircraft, Inc.: Amendment...Code 78: Engine Exhaust. Unsafe Condition...high-temperature gases inside the...

311

Charcoal/LPG cooker, oven, and boiler  

An insulated hot plate cooker that conserves heat in the exhaust of burning charcoal or domestic gas (LPG) and redirects said heat to do additional cooking, or baking, barbecuing, food preservation by drying, toasting, etc., and then redirecting exhaust heat from this compartment to a boiler that produces boil water, coffee, tea, etc.; thus, an energy-saving multi-purpose cooker with oven and boiler that has 80% efficiency. Combustion chamber of cooker is well ventilated and needs no fan or blower. Boiler has good heat conducting exhaust pipes that are submerged in water, and heat in the exhaust is extracted by the pipe to heat the surrounding water. (author) figs.

312

On-board ammonia generation and exhaust after treatment system using same  

Often NOx selective catalysts that use ammonia to reduce NOx within exhaust to a harmless gas require on-board storage of ammonia which can be hazardous and inconvenient. In order to generate ammonia in exhaust, the present disclosure increases a NOx concentration in exhaust from at least one combustion chamber, at least in part, by injecting fuel in a predetermined increased NOx generation sequence that includes a first injection during non-auto ignition conditions and a second injection during auto ignition conditions. At least a portion of the NOx is converted to ammonia by passing at least a portion of the exhaust with the increased NOx concentration over an ammonia-producing catalyst.

313

Evaluation of Technical Feasibility of Homogeneous Charge Compression Ignition (HCCI) Engine Fueled with Hydrogen, Natural Gas, and DME  

The objective of the proposed project was to confirm the feasibility of using blends of hydrogen and natural gas to improve the performance, efficiency, controllability and emissions of a homogeneous charge compression ignition (HCCI) engine. The project team utilized both engine simulation and laboratory testing to evaluate and optimize how blends of hydrogen and natural gas fuel might improve control of HCCI combustion. GTI utilized a state-of-the art single-cylinder engine test platform for the experimental work in the project. The testing was designed to evaluate the feasibility of extending the limits of HCCI engine performance (i.e., stable combustion, high efficiency and low emissions) on natural gas by using blends of natural gas and hydrogen. Early in the project Ricardo provided technical support to GTI as we applied their engine performance simulation program, WAVE, to our HCCI research engine. Modeling support was later provided by Digital Engines, LLC to use their proprietary model to predict peak pressures and temperatures for varying operating parameters included in the Design of Experiments test plan. Digital Engines also provided testing support for the hydrogen and natural gas blends. Prof. David Foster of University of Wisconsin-Madison participated early in the project by providing technical guidance on HCCI engine test plans and modeling requirements. The main purpose of the testing was to quantify the effects of hydrogen addition to natural gas HCCI. Directly comparing straight natural gas with the hydrogen enhanced test points is difficult due to the complexity of HCCI combustion. With the same air flow rate and lambda, the hydrogen enriched fuel mass flow rate is lower than the straight natural gas mass flow rate. However, the energy flow rate is higher for the hydrogen enriched fuel due to hydrogen's significantly greater lower heating value, 120 mJ/kg for hydrogen compared to 45 mJ/kg for natural gas. With these caveats in mind, an analysis of test results indicates that hydrogen enhanced natural gas HCCI (versus neat natural gas HCCI at comparable stoichiometry) had the following characteristics: (1) Substantially lower intake temperature needed for stable HCCI combustion; (2) Inconclusive impact on engine BMEP and power produced; (3) Small reduction in the thermal efficiency of the engine; (4) Moderate reduction in the unburned hydrocarbons in the exhaust; (5) Slight increase in NOx emissions in the exhaust; (6) Slight reduction in CO2 in the exhaust; and (7) Increased knocking at rich stoichiometry. The major accomplishments and findings from the project can be summarized as follows: (1) A model was calibrated for accurately predicting heat release rate and peak pressures for HCCI combustion when operating on hydrogen and natural gas blends. (2) A single cylinder research engine was thoroughly mapped to compare performance and emissions for micro-pilot natural gas compression ignition, and HCCI combustion for neat natural gas versus blends of natural gas and hydrogen. (3) The benefits of using hydrogen to extend, up to a limit, the stable operating window for HCCI combustion of natural gas at higher intake pressures, leaner air to fuel ratios or lower inlet temperatures was documented.

314

SST-1 Gas feed and Gas Exhaust system  

SST-1 tokamak is a long pulse tokamak designed for the plasma operation up to 1000 sec duration. Gas feed system and gas exhaust management will play a very crucial role during plasma discharge. During the different type of operations of tokamak like wall conditioning, diverter operation and neutral beam injection, a large amount of gas will be fed into the vacuum chamber at different locations. Also during plasma operations, the gas will be fed both in continues and pulse mode. Gas feed will be carried out mainly using piezo-electric valves controlled by PXI based data acquisition and control system. Such operations will lead to a huge amount gas exhaust by the main system which requires good exhaust facility to searches, great care should be taken in constructing both. Also initial pumping of cryostat and vacuum vessel of SST-1 will release a large amount of gas. Exhausted gases from SST -1 will be Hydrogen, Nitrogen, Mixture gases or some toxic gases. Dedicated exhaust system controlling the different gases are installed. Special treatment of hazardous/explosive gases is done before releasing to the atmosphere. This paper describes design and implementations of the complete gas feed and exhaust system of SST-1.

315

Analytical and numerical models for estimating the effect of exhaust ventilation on radon entry in houses with basements or crawl spaces  

Mechanical exhaust ventilation systems are being installed in newer, energy-efficient houses and their operation can increase the indoor-outdoor pressure differences that drive soil gas and thus radon entry. This thesis presents simplified models for estimating the pressure driven flow of radon into houses with basements or crawl spaces, due to underpressures induced by indoor-outdoor temperature differences, wind, or exhaust ventilation. A two-dimensional finite difference model is presented and used to calculate the pressure field and soil gas flow rate into a basement situated in soil of uniform permeability. A simplified analytical model is compared to the finite difference model with generally very good agreement. Another simplified model is presented for houses with a crawl space. Literature on radon research is also reviewed to show why pressure driven flow of soil gas is considered to be the major source of radon entry in houses with higher-than-average indoor radon concentrations. Comparisons of measured vs. calculated indoor radon concentrations for a house with a basement showed the simplified basement model underpredicting on average by 25%. For a house with a crawl space the simplified crawl space model overpredicted by 23% when the crawl space vents are open and 48% when the crawl space vents are sealed.

316

Analysis of Indirectly Fired Gas Turbine for Wet Biomass Fuels Based on commercial micro gas turbine data  

The results of a study of a novel gas turbine configuration is being presented. In this power plant, an Indirectly Fired Gas Turbine (IFGT), is being fueled with very wet biomass. The exhaust gas is being used to dry the biomass, but instead of striving to recover as much as possible of the thermal energy, which has been the practice up to now, the low temperature exhaust gases after having served as drying agent, are lead out into the environment; a simple change of process integration that has a profound effect on the performance. Four different cycles have been studied. These are the Simple IFGT fueled by dry biomass assuming negligible pressure loss in the heat exchanger and the combustion chamber, the IFGT fueled with wet biomass (Wet IFGT) assuming no pressure losses, and finally both the Simple and the Wet IFGT incorporating typical data for pressure losses of commercially available micro turbines. The study shows that the novel configuration, in which an IFGT and a drying unit have been combined, has considerable merit, in that its performance exceeds that of the currently available methods converting wet biomass to electric power by a factor of five. The configuration also has clear advantages with respect to corrosion and to the environmental friendliness and the quantity of the waste products and their usefulness.

317

Turbomachines for application in LOTHECO powerplants (turbomachines for LOTHECO)  

The improvement of the technical and economic performance of electric power generation is a continuous effort. An example is the step from simple-cycle (open-cycle) gas turbines to combined-cycle powerplants. Later, STIG and HAT cycles were introduced and, more recently, the LOTHECO concept was proposed. This concept unites features of the standard combined-cycle powerplant and of the HAT cycle by using low-temperature external heat - and not the exhaust energy of the gas turbine - to humidify the high pressure combustion air. (LOTHECO is the acronym for 'combined-cycle powerplant with integrated low-temperature heat'.) An obstacle to the introduction of LOTHECO plants is the fact that in their simplest configuration they require newly designed or at least extensively modified gas turbines. This is because the compressor and the turbine mass flow rates, when adjusted to the LOTHECO conditions, are quite different. To improve this situation, alternatives to the original LOTHECO plant concept must be developed. It is found that combinations of standard gas turbines and expanders are solutions almost equivalent in terms of efficiency and specific work to the original LOTHECO plant with an adjusted gas turbine. Less desirable possibilities appear to be combinations of industrial compressors and expanders because of the relatively low inlet temperature of expanders currently available on the market. (Author)

318

ABB extends gas turbine line down to 2.6 MW  

ABB has recently announced the addition of two new models to the company`s gas turbine product line. The new small gas turbines, rated 2.6 MW and 5.7 MW, are particularly well-suited for small CHP (combined heat and power) plants. For these new models, the company is acting as a packager of the gas turbine system, using engines developed in the Ukraine and Japan and engineered for CHP applications by ABB-PBS, based in Brno, Czech Republic. The GT5 gas turbine is a single-shaft gas turbine featuring a nine-stage axial compressor followed by a radial stage and a three-stage expansion turbine. The compression ratio is 12:1 and the exhaust mass flow is 15.2 kg/s at a maximum temperature of 470{degree}C. The first stage of the expansion turbine uses air-cooled rotor and stator blading. The combustion system is based on two parallel combustion cans placed vertically over the turbine casing. These provide a hot gas at a temperature of 950{degree}C at the turbine inlet. The present combustion chambers produce 88 ppm of NO{sub x} (15% O{sub 2}) that can be reduced to less than 37 ppm with steam injections. Design and operating experience are discussed.

319

New MSW incineration technologies comming up next; Jisedaigata ni yoru gomi nensho setsubi  

The intermediate process in the waste treatment system is taken up, and the development of the gasification melting furnace now regarded as a promising new technology is described. The targets to attain in the development of a gasification melting furnace include the simultaneous reduction in dioxins and nitrogen oxides, and detoxification of fly ash and burned ash; utilization of iron, aluminum, and fused slag, and return to the site of fly ash; improvement on power generation efficiency; reduction in the area required for construction and in the construction and maintenance costs; and reduction in the waste treatment cost. That is, the gasification furnace and the melting furnace will be integrated for the elimination of heat loss, and the combustion in the melting furnace will be a low-air-ratio high-temperature combustion to realize a 30% reduction in the amount of exhaust gas to be generated. The high temperature combustion also reduces the formation of dioxins. The reduction in the amount of exhaust gas results in the reduction of heat loss, in the enhancement of the boiler heat recovery rate, and in the improvement on power generation efficiency. The development of effective use for slag will lead to enhanced slag compaction. The characters of, and problems to be solved for, the coke bed vertical shaft kiln, fluidized bed shaft kiln, fluidized gasification melting furnace, and the rotary drum gasification melting furnace are stated. 7 refs., 8 figs., 1 tab.

320

Engine performance and emission characteristics of marine fish-oil biodiesel produced from the discarded parts of marine fish  

Biodiesel is recognized as a clean alternative fuel or as a fuel additive to reduce pollutant emissions from combustion equipment. Because cultivated land is too limited to grow seed-oil plants sufficient to produce both food and biodiesel, non-land-based oleaginous materials have been considered important sources for the production of the latter. In this study, the discarded parts of mixed marine fish species were used as the raw material to produce biodiesel. Marine fish oil was extracted from the discarded parts of mixed marine fish and refined through a series of pretreatment processes. The refined marine fish oil was then transesterified with methyl alcohol to produce biodiesel, which was used thereafter as engine fuel to investigate its engine performance and emission characteristics. The experimental results show that, compared with commercial biodiesel from waste cooking oil, marine fish-oil biodiesel has a larger gross heating value, elemental carbon and hydrogen content, cetane index, exhaust gas temperature, brake fuel conversion efficiency, NO{sub x} and O{sub 2} emissions, and black smoke opacity and a lower elemental oxygen content, fuel consumption rate, brake-specific fuel consumption rate, equivalence ratio, and CO emission. Compared with ASTM No. 2D diesel, both marine fish-oil and waste cooking-oil biodiesels appear to have a lower gross heating value, cetane index, exhaust gas temperature, equivalence ratio, black smoke opacity, elemental carbon content, and CO emission and a higher fuel consumption rate and elemental oxygen content. (author)

 
 
 
 
321

Corrosion aspects in the design and operation of ODS indirect fired heat exchangers  

ODS alloys are candidate materials for the critical section in the high temperature heater for indirect fired coal conversion systems, although little has been published on their corrosion characteristics in this situation. Salient features of indirect fired systems are described. Under a European Union COST 501 program, a natural gas fired ODS alloy heater has been built and operated for a short period as part of a Closed Cycle Gas Turbine Demonstrator. Although the planned environment was clean, a number of critical oxidation related problems emerged during development work associated with the program. These included scale spallation, breakaway corrosion due to aluminium exhaustion, and nitridation. With respect to the material, oxidation led to porosity induced growth, due to the Kirkendall effect, and low temperature embrittlement. The effect of these can be controlled by establishing criteria for the levels of oxide growth and aluminium exhaustion during service. Tentative limits are suggested. Providing that direct attack from coal ashes and slags is eliminated by good furnace design, as seems possible, current alloys should permit the construction of an indirect coal fired system with an efficiency of around 50%.

322

Initial experiences with digital control for steam turbines  

Digital controls for steam turbines were introduced commercially during the mid 1980`s. Because of their versatility compared to their analogue counterparts they quickly became established as a recognised standard of control not only for speed, but for pressure, temperature, power or any parameter connected with steam turbine control systems. The contract for a steam turbine driven alternator at a CCGT CHP plant in Sweden was awarded to Peter Brotherhood Ltd. in 1990. Steam for the turbine is from a peat fired boiler and the gas turbine exhaust waste heat superheater. The steam turbine exhausts into a condenser, the cooling water outlet from which provides hot water. Turbine speed is 7 000 rpm and a gearbox gives a speed reduction down to the alternator speed of 1 500 rpm. The plant cannot operate in island mode as the power output from both the gas and steam turbine driven alternators is supplied only to the Swedish grid. Power for the plant is imported from the grid. To control the steam turbine, the decision was taken to use the then relatively new Woodward 505 digital controller. The requirement for the control system was for speed regulation when running with the generator breaker open. After synchronising with the Swedish grid, bumpless transfer to steam inlet pressure (and hence boiler pressure) control was required together with an optional limitation on the temperature of the cooling water leaving the condenser. (Author)

323

Application of concentrated solar radiation to high temperature detoxification and recycling processes of hazardous wastes  

In many cases, hazardous wastes are subject to thermal treatment at elevated temperatures. Some types of wastes do not have a sufficient calorific value to cover the heat demand of the high temperature process. For thermal treatment of e.g. filter residues, dusts, sulfuric acid, aluminium dross, foundry sand, or waste water, supplementary energy supply is needed. The specific energy demand ranges from 0.5 to 2.5 kWh/kg (2-10 MJ/kg). An important aim of process optimisation is the reduction of (fossil) energy consumption and exhaust gas flow. Concentrated solar energy promises advantages when applied to high energy consuming waste treatment processes with regard to substitute fossil or electric energy consumption, to reduce CO{sub 2} emissions, and exhaust gas flow. In parallel to conceptional studies, a solar-heated rotary kiln mini-plant has been designed and constructed for tests in the DLR solar furnace. The tests will give indications of boundary conditions for solar thermal treatment or conversion of selected hazardous materials. (author)

324

Methodologies for predicting the part-load performance of aero-derivative gas turbines  

Prediction of the part-load performance of gas turbines is advantageous in various applications. Sometimes reasonable part-load performance is sufficient, while in other cases complete agreement with the performance of an existing machine is desirable. This paper is aimed at providing some guidance on methodologies for predicting part-load performance of aero-derivative gas turbines. Two different design models – one simple and one more complex – are created. Subsequently, for each of these models, the part-load performance is predicted using component maps and turbine constants, respectively. Comparisons with manufacturer data are made. With respect to the design models, the simple model, featuring a compressor, combustor and turbines, results in equally good performance prediction in terms of thermal efficiency and exhaust temperature as does a more complex model. As for part-load predictions, the results suggest that the mass flow and pressure ratio characteristics can be well predicted with both methods. The thermal efficiency and exhaust temperature, however, are not well predicted below 60–70% load when using turbine constants and assuming constant efficiencies for turbomachinery.

325

Development of rotary heat storing type burner. Kaiten chikunetsugata burner no kaihatsu  

This paper describes a rotary heat storing type burner under development. This burner has a fuel nozzle consisted of a shaft common to a ceramic heat storing material of a round column honeycomb and a cylindrical duct, the duct being halved at a point contacting the heat storing material to form passages for exhaust gases and combustion air. Rotating the duct around the shaft of the fixed heat storing material makes the high-temperature exhaust gas from the furnace to give heat to the heat storing material when passing by it, and discharged, whereas the combustion air at a normal temperature is pre-heated and guided into the furnace. This burner was installed in a test furnace to test for burning an LPG at about 6.5{times} 10{sup 4} kcal/h at a furnace temperature of about 750{degree} C or 950{degree} C. According to the result, the heat efficiency with this burner is calculated tentatively at about 90% including the heat loss at the furnace walls. Its NO{sub X} generation was low for its high pre-heated air temperature. 8 figs., 1 tab.

326

Bigger and cleaner  

Shell Technology's fuel cell plans have been proceeding quickly. The first 250 kW fuel cell is already under construction in Kollsnes outside Bergen, Norway, and will be completed in two years. Now the oil company, along with Statkraft and Aker Kvaerner, has launched plans for a much bigger fuel cell of between 10 and 20 MW. This is a so-called solid oxide fuel cell (SOFC). Such a fuel cell has an operating temperature of about 1,000 degrees and can use natural gas as a fuel. Most other fuel cell technologies have lower operating temperatures and are based on hydrogen. SOFC technology is not new. Although Siemens Westinghouse in the USA has been producing such fuel cells for many years, the commercial market has yet to take off. What is unique about Shell's technology is that it is fitted with an afterburner. This special afterburner is constructed in a manner similar to the main cell, but is equipped with a special exhaust manifold that separates the CO{sub 2} gas from the nitrogen. In a normal solid oxide fuel cell, CO{sub 2} gas is emitted along with the nitrogen into the atmosphere. In addition, the afterburner increases the total efficiency by increasing the electricity yield. In a large-scale plant, the hot exhaust gases can drive a gas turbine, which will bring the electricity yield up to 70 per cent. This is about 10 percent more than from a conventional gas fired plant, and it has a natural CO{sub 2} recovery system to boot.

327

Cycle analysis of an integrated solid oxide fuel cell and recuperative gas turbine with an air reheating system  

Cycle simulation and analysis for two kinds of SOFC/GT hybrid systems were conducted with the help of the simulation tool: Aspen Custom Modeler. Two cycle schemes of recuperative heat exchanger (RHE) and exhaust gas recirculated (EGR) were described according to the air reheating method. The system performance with operating pressure, turbine inlet temperature and fuel cell load were studied based on the simulation results. Then the effects of oxygen utilization, fuel utilization, operating temperature and efficiencies of the gas turbine components on the system performance of the RHE cycle and the EGR cycle were discussed in detail. Simulation results indicated that the system optimum efficiency for the EGR air reheating cycle scheme was higher than that of the RHE cycle system. A higher pressure ratio would be available for the EGR cycle system in comparison with the RHE cycle. It was found that increasing fuel utilization or oxygen utilization would decrease fuel cell efficiency but improve the system efficiency for both of the RHE and EGR cycles. The efficiency of the RHE cycle hybrid system decreased as the fuel cell air inlet temperature increased. However, the system efficiency of EGR cycle increased with fuel cell air inlet temperature. The effect of turbine efficiency on the system efficiency was more obvious than the effect of the compressor and recuperator efficiencies among the gas turbine components. It was also indicated that improving the gas turbine component efficiencies for the RHE cycle increased system efficiency higher than that for the EGR cycle. (author)

328

Combined cogeneration equipment containing gas turbine using low sulphur heavy stock as fuel  

This paper describes the combined cogeneration in Chemical and Plastics Co. Madras (India) which uses low sulphur heavy stock (LSHS) as a fuel. By the combined cogeneration of gas turbine and boiler steam turbine power generation, the exhaust from the steam turbine is supplied to the factory as a process steam. This equipment has a capacity of 4835 kW in overall generation power and 23.5 tons/hrs. in steam evaporation. The gas turbine system is equipped with an axial-flow, 11 step compressor, an axial flow, 4 step turbine, and a single-can back flow combustor fixed to the intermediate casing. The temperature of the exhaust from the gas turbine is 542/sup 0/C. Low quality LSHS when burned exerts no influence on the service life of the turbine blades. The boiler is a horizontal bent pipe, forced circulation type, and the steam turbine is a back pressure control type. The fuel is treated with a horizontal, two drum, electrostatic separator to which a demulsifier is supplied, to be separated into oil and water. As to the vanadium salts contained in the fuels, a chemical liquid containing MgO as a major ingredient is added to the fuel prior to the combustion. Thereby, the melting temperature of the vanadium oxide is enhanced, which serves for prevention of the melting and adhesion of the vanadium oxide to the gas turbine. LSHS is a residual oil produced by the ordinary pressure distillation of India-produced crude oil, has a sulphur content of 1.75%, and is solid at room temperature. Attention should be paid to clogging of the pipings. The overall efficiency is 80%. The combined cogeneration can be coordinated with load variations of 10 - 20%. (12 figs, 1 tab)

329

Development of deNOx technology for diesel engine exhaust. 1; Diesel engine hai gas NOx teigen gijutsu no kaihatsu. 1  

With the use of an alumina catalyst with methanol as reducing agent, in which high denitrification activity was found, as a catalyst to purify diesel engine exhaust gas, the development of a compact diesel exhaust gas purification system has been proceeded with. In this paper, the following were conducted: endurance test using diesel exhaust gas as element test on the catalyst toward verification, study of influences of exhaust composition and honeycomb shape on exhaust pressure loss and activity, etc. It was confirmed in the diesel actual gas experiment that the alumina-methanol catalyst has high NOx removing ability and steam resistance, and excellent SOx resistance, and the execution of a 200 kW class large-scale verification test was in sight. It was made clear that in the honeycomb shape of the catalyst, there exists the optimum pitch size which has less influence also on exhaust components of dust/soot, etc., and that the system is applicable to a wide range of exhaust gas NOx concentration. It was additionally made clear that the installation of oxidation catalyst in the rear step made easy treatment of incombustibles possible. 8 refs., 7 figs., 3 tabs.

330

Biogas upgrade to syn-gas (H2-CO) via dry and oxidative reforming  

Fuel reforming processes are primarily used to generate hydrogen for fuel cells and in automotive internal combustion engines to improve combustion characteristics and emissions. In this study, biogas is used as the fuel source for the reforming process as it has desirable properties of being both renewable and clean. Two reforming processes (dry reforming and combined dry/oxidative reforming) are studied. Both processes are affected by the gas stream temperature and reactor space velocity with the second process being affected by O2/CH4 ratio as well. Our results imply that oxidative reforming is the dominant process at low exhaust temperatures. This provides heat for the dry reforming of biogas and the overall reforming is exothermic. Increase in O2/CH4 ratio at low temperature promotes ...

331

Reducing the viscosity of Jojoba Methyl Ester diesel fuel and effects on diesel engine performance and roughness  

An experimental investigation has been carried out to test two approaches to reduce the viscosity of the Jojoba Methyl Ester (JME) diesel fuel. The first approach is the heating of the fuel to two temperatures of 50 and 70 C as compared to the base ambient temperature and to diesel fuel too. The second approach is adding one chemical which is considered by its own as alternative and renewable fuel which is Diethyl Ether (DEE). The viscosity has been reduced by both methods to close to diesel values. The performance of a diesel engine using those fuels has been tested in a variable compression research engine Ricardo E6 with the engine speed constant at 1200 rpm. The measured parameters included the exhaust gas temperature, the ignition delay period, the maximum pressure rise rate, maximum pressure, and indicated mean effective pressure and maximum heat release rate. The engine performance is presented and the effects of both approaches are scrutinized. (author)

332

Reducing the viscosity of Jojoba Methyl Ester diesel fuel and effects on diesel engine performance and roughness  

An experimental investigation has been carried out to test two approaches to reduce the viscosity of the Jojoba Methyl Ester (JME) diesel fuel. The first approach is the heating of the fuel to two temperatures of 50 and 70degreeC as compared to the base ambient temperature and to diesel fuel too. The second approach is adding one chemical which is considered by its own as alternative and renewable fuel which is Diethyl Ether (DEE). The viscosity has been reduced by both methods to close to diesel values. The performance of a diesel engine using those fuels has been tested in a variable compression research engine Ricardo E6 with the engine speed constant at 1200rpm. The measured parameters included the exhaust gas temperature, the ignition delay period, the maximum pressure rise rate, maxi...

333

Establishment of an installation process of a valve seat to a cylinder head using the cae technique  

Valve seats press-fitted in the cylinder head function to hold exhaust gas inside the ignition chamber and to transfer heat to the coolant moving in the water jacket of the head. The press-fitting of the valve seats to the head at ambient temperature has been widely spread out due to its many advantages over pressing with frozen valve seats or with a heated head. The benefits include lower equipment costs, lower running costs, and fewer installation faults during the press-fitting. Nevertheless, a systematic approach for pressing at ambient temperature (ATP; ambient temperature press-fitting) has not been studied and analyzed to date. A technique to check the reliability of the press-fitting by measuring hoop strain inside the valve seat and the FEM procedure to simulate ATP is developed i...

334

Comparison of operating characteristics of a 34-kW diesel engine fueled with low-energy gas, biogas, and diesel fuel  

Diesel engines can be operated in a dual-fuel mode with low-energy gas, also called LEG, from thermal gasification or with biogas from anaerobic digestion. This article compares the operating characteristics of a 34-kW diesel engine operating in dual-fuel modes with the operating characteristics of the same engine fueled with diesel oil. Performance curves comparing torque, speed, power, air ratio, effective efficiency, and exhaust temperature are presented for each mode of operation. In the low-energy gas, dual-fuel mode, the engine was supplied with low-energy gas from a batch-fed, downdraft gasifier fueled with densified solid waste. The filtered and cooled low-energy gas was fed to the diesel engine through a mixing chamber. In the biogas dual-fuel mode, the engine was supplied with synthetic biogas obtained by mixing natural gas with compressed carbon dioxide. The synthetic biogas was fed to the engine by a carburetor. Pilot diesel fuel was injected into the engine for ignition of both the low-energy gas and biogas. In both dual-fuel modes, 15 to 24% of the input fuel was diesel oil. It was found that the practical power output in the dual-fuel modes was 30 kW (86%) with biogas, and 25 kW (71%) with low-energy gas, as compared to 34 kW (100%) with normal diesel operation.

335

Comparison of diamond growth with different gas mixtures in microwave plasma asssited chemical vapor deposition (MWCVD)  

Abstract in english In this work we study the influence of oxygen addition to several halocarbon-hydrogen gas systems. Diamond growth have been performed in a high power density MWCVD reactor built in our laboratory. The growth experiments are monitored by argon actinometry as a reference to plasma temperature and atomic hydrogen production, and by mass spectrometry to compare the exhaust gas composition. Atomic hydrogen actinometry revealed that the halogen presence in the gas phase is resp (more) onsible for a considerable increase of atomic hydrogen concentration in the gas phase. Mass spectrometry shows similar results for all gas mixtures tested. Growth studies with oxygen addition to CF4/H2, CCl4/H2, CCl2F2/H2 and CH3Cl/H2 reveals that oxygen increases the carbon solubility in the gas phase but no better diamond growth conditions were found. Halogens are not, per se, eligible for diamond growth. All the possible advantages, as the higher production of atomic hydrogen, have been suppressed by the low carbon solubility in the gas phase, even when oxygen is added. The diamond growth with small amount of CF4 added to CH4/H2 mixture is not aggressive to the apparatus but brings several advantages to the process.

336

A comparative study of using simple and ejector-absorption refrigeration for inlet air cooling of simple and regenerative gas turbine  

A study was conducted in which the effect of inlet air cooling on the performance of a gas turbine was investigated. Compared to steam turbines, gas turbines have lower capital cost, are compact in size, and offer better environmental performance with fast starts and loading. They require less manpower for operating and do not need water sources. However, they have lower efficiency than steam turbines and have a strong influence on climatic conditions. In addition, thermal energy in the form of exhaust gases is delivered to, and wasted in, the environment. In order to increase the power and efficiency of gas turbine plants, this low grade thermal energy can be put to beneficial use in a heat exchanger of a regenerative gas turbine (RGT) or in the generator of an absorption refrigeration cycle (ARC). This paper focused on ways to increase the performance of gas turbine plants by using an ARC for inlet air cooling. The authors studied the feasibility of installing an ARC at the gas turbine inlet. The work showed that the net work and the efficiency will increase by 6-10 per cent and 1-5 per cent respectively for every 10 degrees C decrease of inlet temperature. Since the coefficient of performance (COP) of ARC is low, the thermal energy of exhaust gases cannot supply all the needed thermal energy for the refrigeration cycle. The results showed that when an ejector is included in the refrigeration cycle, the need for external energy source required for refrigeration cycle is reduced. 22 refs., 8 tabs., 18 figs.

337

Atmospheric environmental implications of propulsion systems  

Three independent studies have been conducted for assessing the impact of rocket launches on the earth`s environment. These studies have addressed issues of acid rain in the troposphere, ozone depletion in the stratosphere, toxicity of chemical rocket exhaust products, and the potential impact on global warming from carbon dioxide emissions from rocket launches. Local, regional, and global impact assessments were examined and compared with both natural sources and anthropogenic sources of known atmospheric pollutants with the following conclusions: (1) Neither solid nor liquid rocket launches have a significant impact on the earth`s global environment, and there is no real significant difference between the two. (2) Regional and local atmospheric impacts are more significant than global impacts, but quickly return to normal background conditions within a few hours after launch. And (3) vastly increased space launch activities equivalent to 50 U.S. Space Shuttles or 50 Russian Energia launches per year would not significantly impact these conclusions. However, these assessments, for the most part, are based upon homogeneous gas phase chemistry analysis; heterogeneous chemistry from exhaust particulates, such as aluminum oxide, ice contrails, soot, etc., and the influence of plume temperature and afterburning of fuel-rich exhaust products, need to be further addressed. It was the consensus of these studies that computer modeling of interactive plume chemistry with the atmosphere needs to be improved and computer models need to be verified with experimental data. Rocket exhaust plume chemistry can be modified with propellant reformulation and changes in operating conditions, but, based upon the current state of knowledge, it does not appear that significant environmental improvements from propellant formulation changes can be made or are warranted.

338

Fuel cell power generation system; Nenryo denchi hatsuden sochi  

When liquid fuel is used in the fuel cell power generation system, an evaporator is employed for the necessity of supplying the gas fuel to the fuel cell. Electric heater type or fun type evaporators are conventionally employed. The power used for the heater or fun is generally supplied from other source than the fuel cell. In the invented fuel cell power generation system, a warm water supply system or exhaust gas supply system is adopted for evaporating the liquid fuel. In the warm water supply system, the exhaust gas from air electrode is supplied to a heat exchanger through exhaust gas pipe, and the heat is supplied to the evaporator by means of circulation pump. The power driving the circulation pump is about one tenth of the power required for the electric heater type evaporator. In the exhaust gas supply system, the exhaust gas is supplied directly to the evaporator through the branch pipe for exhaust gas pipe from the air electrode. In this way, a system which needs not at all the power from outside can be constructed. 3 figs.

339

Determining the fatigue of superheated steam-carrying, thick-walled old plant components and the consequential measures necessary for extending their service life. Ermittlung der Erschoepfung von heissdampffuehrenden, dickwandigen Altanlagenkomponenten und daraus resultierende Massnahmen zur Verlaengerung der Lebensdauer  

This paper deals mainly with the procedure for determining life spans (static and dynamic), computerized methods for determining exhaustion, fault assessment during varying operating conditions and the consequences for the operator when a high degree of exhaustion of plant components exists. In addition the paper provides an example of how to minimize dynamic exhaustion of superheated steam-carrying, thick-walled components by optimization of pressure and temperature rise during start-up. (orig.).

340

4  

tain the properties of strength and ductility after expo- sure to an 1800 F ... ( Nonweldable, Cast Alloy) . . 25 ... nitriding. This was achieved by a dual-wall, exhaust gas regenerative design ... rials were selec'ed for use in the evaluation program.

 
 
 
 
341

Investigation of High Gas Temperature Utilization for Advanced Tip Turbine Fans.  

Studies made of cooling systems for tip-turbine cruise fans are discussed. These studies include a review of planned and predicted core engine exhaust gas conditions; the conceptual design and evaluation of several turbine bucket-carrier cooling systems; ...

342

CIG (Italy) standards for the exhaust of combustion products  

The paper examines different kinds of gas appliances and their systems for smoke exhausting. The relevant technical regulations issued by CIG (Italy) are also discussed including the contents of the draft revision at present under public inquiry.

343

l  

Report Date. COOLING OF A PLATE INSERTED IN THE EXHAUST .... sumed that the hot-gas convective-heat-transfer coefficient with film cooling is identical ..... The leading edge of the test section was flame sprayed with Rockite (an alumina ...

344

notice this document has been reproduced from microfiche ...  

oxides of nitrogen, the exhaust gas was sampled for carbon monoxide, ... gated the effects of two-stage combustion operating conditions and fuel prop- .... in the design and operation of the research fuel system. .... Both fuel oils came from the ...

345

Combustion Engine Research  

the Army's Research and Technology Laboratories for the early 1990's .... Although the present "oil vanced ..... nology, a two-stage series system .... core along with a directlygeared exhaust gas tur- ..... GATE Studies," NASA TM-79073, 1979.

346

Larry A. Diehl and James D. Holdeman Lewis Research Center ...  

Gaseous emissions from a JT8D-109 turbofan engine were measured in an altitude .... all tests. Exhaust gas samples were obtained with a single-point traversing ..... Oxides-of- analyzer nitrogen analyzer. Water separator. Vent. Hydrocarbon ...

347

Catalyst for treatment of exhaust gases from internal combustion engines, and method for manufacturing of the catalyst. Katalysatorenhet foer behandling av avgaser fraan foerbraenningsmotor samt saett foer tillverkning av katalysatorenheten  

This innovation describes a catalyst for exhaust gas cleaning. It consists of a carrier body and a number of metal strips which are spirally wounded with a cylindrical outer surface and a gap between the band edges

348

77 FR 23987 - Approval and Promulgation of Implementation Plans; State of Montana; State Implementation Plan...  

...295\\ The plant is rated at 65 MW gross output and includes two identical CFB boilers that are fired on petroleum coke and cooker gas; exhaust exits through a common stack. The boilers and emission controls were installed in...

349

Tim e  

The NASA STI Program Office is operated ... continuing reference value. ..... aluminum droplet is gradually consumed by oxidation unless it and its oxide cap ( or lobe) are .... exhaust gas and particulates into and out of this reservoir has been ...

350

Turbo-supercharger, particularly for motorcycles. Turbolader, insbesondere fuer Motorraeder  

A turbo-supercharger has an exhaust gas turbine and a compressor, which are connected by an interposing shaft. The exhaust gas turbine is situated in an exhaust gas duct, which is situated upstream of an outlet manifold, which is situated in front of an engine and is connected to the engine outlet. The compressor is situated in an inlet duct, which is connected to an engine inlet. The outlet and inlet openings are situated on the front and back of the engine. The exhaust gas turbine and the compressor are situated side by side and are transverse to the motorcycle frame. The axis of rotation of the turbo-supercharger is such that it turns downwards on the side of the engine, and the compressor has a spiral opening, which is directed upwards. Further, the outlet manifold is covered by a cover, which is situated at a distance from the manifold.

351

library copy  

clinker cooler applications where the exhaust .... gas-sidefouling in cement plant applications. However ...... pores of the dolomite brick could have initiatedformationof the deposit. Initiallythe ...... and the development of cogeneration schemes.

352

Ozone Pollution  

... are produced primarily when fossil fuels like gasoline, oil or coal are burned or when some chemicals, ... as mowing your lawn or refilling your gas tank during daylight hours. Lawn mower exhaust and gasoline ...

353

Hydrogen Storage for Aircraf:t Applications Overview  

content which tend to saturate the reforming catalyst. This poisoning of the catalyst needs to be addressed ... the gasification of the hydrocarbon ... steam and exhaust gas reforming, are ... consists of a catalyst filled cylinder. As fuel and water ...

354

Added gas turbines invigorate lignite veteran  

Exhaust from two gas turbines will be used for feed water heating at a German lignite fuelled plant, bringing efficiency gains, on top of increased generating capacity and greater ability to meet grid requirements. 3 figs., 1 tab.

355

New Alloy Could Improve Gas Mileage, Lower Emissions  

... Ala., promises to lower engine emissions and could improve gas mileage in cars, ... in the automotive, aerospace, marine and recreational vehicle industries. ... today's high-performance gasoline and diesel engines meet tougher exhaust ...

356

Engineering development of coal-fired high-performance power systems. Technical progress report 1, July through September 1995  

In phase 1 of the project, a conceptual design of a coal-fired high performance power system was developed, and small scale R&D was done in critical areas of the design. The current Phase of the project includes development through the pilot plant stage, and design of a prototype plant that would be built in Phase 3. Goals have been identified that relate to the efficiency, emissions, costs and general operation of the system. The base case arrangement of the HIPPS cycle is shown in Figure 1. It is a combined cycle plant. This arrangement is referred to as the All Coal HIPPS because it does not require any other fuels for normal operation. A fluidized bed, air blown pyrolyzer converts coal into fuel gas and char. The char is fired in a high temperature advanced furnace (HITAF) which heats both air for a gas turbine and steam for a steam turbine. The air is heated up to 1400F in the HITAF, and the tube banks for heating air are constructed of alloy tubes. The fuel gas from the pyrolyzer goes to a topping combustor where it is used to raise the air entering the gas turbine to 2350F. In addition in the HITAF, steam duty is achieved with a heat recovery steam generator in the gas turbine exhaust stream and economizers in the HITAF flue gas exhaust stream. An alternative HIPPS cycle is shown in Figure 2. This arrangement uses a ceramic air heater to heat the air to temperatures above what can be achieved with alloy tubes. This arrangement is referred as the 35% natural gas HIPPS. A pyrolyzer is used as in the base case HIPPS, but the fuel gas generated is fired upstream of the ceramic air heater instead of in the topping combustor. Gas turbine air is heated to 1400 F in alloy tubes the same as in the All Coal HIPPS. This air then goes to the ceramic air heater where it is heated further before going to the topping combustor. The temperature of the air leaving the ceramic air heater will depend on technological developments in that component.

357

Plasma Reforming And Partial Oxidation Of Hydrocarbon Fuel Vapor To Produce Synthesis Gas And/Or Hydrogen Gas  

Methods and systems are disclosed for treating vapors from fuels such as gasoline or diesel fuel in an internal combustion engine, to form hydrogen gas or synthesis gas, which can then be burned in the engine to produce more power. Fuel vapor, or a mixture of fuel vapor and exhaust gas and/or air, is contacted with a plasma, to promote reforming reactions between the fuel vapor and exhaust gas to produce carbon monoxide and hydrogen gas, partial oxidation reactions between the fuel vapor and air to produce carbon monoxide and hydrogen gas, or direct hydrogen and carbon particle production from the fuel vapor. The plasma can be a thermal plasma or a non-thermal plasma. The plasma can be produced in a plasma generating device which can be preheated by contact with at least a portion of the hot exhaust gas stream, thereby decreasing the power requirements of the plasma generating device.

358

Characteristics of soot formation and decomposition in turbulent diffusion flames  

Profiles of soot concentration together with gas species concentrations and temperature are measured in propane/air turbulent diffusion flames of two typically different air inlet temperatures of 50 and 500 C, paying special attention to the roles of gas temperature on the behavior of soot formation and burnout in the flames. Soot is most likely to be produced in the fuel-rich region just inside the flame front, where unburnt hydrocarbons such as CH/sub 4/, C/sub 2/H/sub 4/, C/sub 2/H/sub 6/, and C/sub 2/H/sub 2/ cracked from the original fuel of C/sub 3/H/sub 8/ observed. The soot burnout occurs mainly in the stoichiometric and fuel lean conditions near the flame front or in the downstream region. When the gas temperature is raised, both the soot formation and burnout rates increase. The final exhaustion of soot is determined by the combined effects of the formation and burnout, which are influenced by the temperature history through the flame.

359

The Effect of Temperature and Relative Humidity on the Flight Performance of Female AEDES Aegypti.  

The influence of temperature and r.h. on the flight performance of tethered virgin female Aedes aegypti was investigated. Mosquitoes of similar age were flown to exhaustion on flight mills at various temperatures and relative humidities. Parameters measur...

360

Catalytic Converter Exhaust System Temperature Tests.  

In June 1975, the Forest Service Equipment Development Center at San Dimas, Calif., conducted tests to determine exhaust system temperatures on late-model vehicles. Test results showed that for normal vehicle operation, only small temperature differences ...

 
 
 
 
361

Turbocharger design for electrical wastegate actuation to minimize leakage; Turboladerdesign fuer elektrische Waste-Gate-Betaetigung minimiert Leckage  

Exhaust gas turbochargers are a major part of current strategies for reducing CO{sub 2} emissions - especially in the gasoline engine. To optimally support downsizing and downspeeding, turbochargers must react as fast as possible, and the exhaust gas volumetric flow to the turbine must be exactly adjustable with a wastegate. Electric motor actuation is advantageous here. However, it places specific requirements on the wastegate which Continental has taken into account in its new generation of turbochargers. (orig.)

362

Muffler for exhaust gas from an internal combustion engine  

A muffler is described for the exhaust gas of an internal combustion engine, the muffler having an inlet and an outlet for exhaust gas and further compromising a casing and a cylindrical sound absorbing body comprising a fibrous material and extending through the casing and having an inner cylindrical surface, and a heat resistant paint formed on the inner cylindrical surface, the heat resistant paint having a thickness not in excess of 250 micrometers.

363

Predicting the dynamics of change in bed pressure with exhaustion of gas and gas-condensate formations based on the use of self-organizing models  

The use of the method of group calculation of arguments for predicting the dynamics in change in bed pressure with exhaustion of gas and gas-condensate formations is substantiated and suggested. It is indicated that the use of this method will make it possible to predict more reliably the dynamics of change in bed pressure under conditions of low and insufficiently accurate initial geological-field information, as well as diagnoses of the processes of mass transfer occurring in the beds during their exhaustion.

364

The role of thermophoresis in trapping of diesel and gasoline particulate matter  

Thermophoresis is the phenomenon by which sub-micron particles suspended in a gas move in the direction of decreasing temperature. It occurs naturally in automotive catalysts and is responsible for improved particle deposition during transient operation when a hot, particle-laden exhaust gas flows through a cool monolith. Although the time-averaged effects of thermophoresis are expected to be relatively small, it is possible that the effect can be enhanced by a properly designed aftertreatment system. In the current work, thermophoretic effects on particle deposition in automotive catalysts are studied by means of numerical simulations. The potential gain in deposition efficiency obtainable by employing thermophoresis is investigated for both laminar and turbulent flow in a standard monoli...

365

Syngas production from hydrocarbon-containing gas in ambient of water vapor plasma  

This study presents results of an experimental investigation on the development of water vapor plasma technology and its applications in environment-friendly processes. An experimental linear 55-69kW DC plasma torch operating at atmospheric pressure was developed, tested and employed to conduct an experimental research on the production of hydrogen-rich gas. The average temperature of water vapor plasma jet in the exhaust nozzle varied from 2000 to 3000K, and the plasma jet velocity was 210-350ms^-^1. Propane gas conversion into syngas by water vapor plasma technology was investigated; this process was found to proceed efficiently. Hydrogen and carbon monoxide gases were produced as the main products, and additionally also small amounts of CO2 and H2O and O2 were obtained. Propane conversi...

366

High resolution real time capable combustion chamber simulation; Zeitlich hochaufloesende echtzeitfaehige Brennraumsimulation  

The article describes a zero-dimensional model for the real time capable combustion chamber pressure calculation with analogue pressure sensor output. The closed-loop-operation of an Engine Control Unit is shown at the hardware-in-the-loop-simulator (HiL simulator) for a 4-cylinder common rail diesel engine. The presentation of the model focuses on the simulation of the load variation which does not depend on the injection system and thus the simulated heat release rate. Particular attention is paid to the simulation and the resulting test possibilities regarding to full-variable valve gears. It is shown that black box models consisting in the HiL mean value model for the aspirated gas mass, the exhaust gas temperature after the outlet valve and the mean indicated pressure can be replaced by calculations from the high-resolution combustion chamber model. (orig.)

367

Characterization of ceramic composite membrane filters for hot gas cleaning  

Novel composite ceramic membrane filters suitable for hot gas cleaning operations have been prepared form fly ash and titania particles on stainless steel woven mesh substrates. Both membranes had a structure like a solid packed bed with a thickness of less than 100 {mu}m. In the domain of laminar flow, significant differences in the pressure drop between experimental results and those predicted from the Kozeny-Carman relationship were found, particularly for flow through the titania membrane. Membrane filters with extremely small pores such as the titania membrane are greatly affected by slip up to 80% in permeability at elevated temperatures. Efficiencies of filtration of typical coal fired power station exhaust fly ashes were found to be greater than 99% for both titania and ash membranes, whilst there was greater variation in the pressure drops in the ash membrane than in the titania at typical gas flows. (orig.)

368

Surface tension measurements of coal ash slags under reducing conditions at elevated pressures  

The aim of limiting the amount of Formula Not Shown that is released together with other exhaust gases from power plants can be reached by technologies allowing for a systematic separation of this greenhouse gas. One such technology is the integrated gasification combined cycle power plant which makes use of a coal gasification step. For the gasification involving temperatures far higher than in typical pulverised combustion chambers, ash contained in the fuel is liquefied (slag) and must be removed from the cycle to guarantee safe operation of downstream equipment. To keep the efficiency of the power plant as high as possible, hot gas cleaning facilities are most desirable for this purpose. The design of these installations necessitates knowledge about thermophysical properties of coal as...

369

Adsorption isotherms for tritium on various adsorbents at liquid nitrogen temperature  

The cryosorption method is useful for extracting hydrogen isotopes from a helium gas stream with a small amount of hydrogen isotopes. Therefore, in fusion reactors, this method is expected to be applied for the helium glow discharge exhaust gas processing system and the blanket tritium recovery system. To design these systems, adsorption isotherms for each hydrogen isotope are needed, making it possible to estimate the amount of adsorption in a wide pressure range. The amount of tritium adsorption on molecular sieve 5A, molecular sieve 4A, and activated carbon, which are potential adsorbents in the cryosorption bed, at liquid nitrogen temperature were quantified using the volumetric method. It was found that adsorption isotherms of tritium were also expressed with the two-site Langmuir model and that the obtained isotherms were close to the reported isotherms, the Langmuir coefficients for which were estimated using a reduced mass of hydrogen isotopes.

370

Model of the expansion process for R245fa in an Organic Rankine Cycle (ORC)  

An Organic Rankine Cycle (ORC) is considered as one of the most environmental-friendly ways to convert different kinds of low temperature energies, i.e. solar, geothermal, biomass and thermal energy of exhaust gases into electrical energy. Two important facts about the ORC must be considered: An organic fluid is selected as the working fluid and a high expansion ratio is usually presented in the machinery due to thermodynamic and efficiency factors. In the past, the pre-design of turbomachinery has been based on the usage of ideal fluid laws, but the real gas effects have a significant influence in the ORC working condition, due to its proximity to the saturation vapor line. In this article, the Equations of State (EoS) (Ideal gas, Redlich-Kwong-Soave and Peng-Robinson) have been evaluated...

371

National Account Energy Alliance Final Report for the Ritz Carlton, San Francisco Combined Heat and Power Project  

Under collaboration between DOE and the Gas Technology Institute (GTI), UTC Power partnered with Host Hotels and Resorts to install and operate a PureComfort 240M Cooling, Heating and Power (CHP) System at the Ritz-Carlton, San Francisco. This packaged CHP system integrated four microturbines, a double-effect absorption chiller, two fuel gas boosters, and the control hardware and software to ensure that the system operated predictably, reliably, and safely. The chiller, directly energized by the recycled hot exhaust from the microturbines, could be configured to provide either chilled or hot water. As installed, the system was capable of providing up to 227 kW of net electrical power and 142 RT of chilled water at a 59F ambient temperature.

372

Thermoelectricity in Self-Contained Heating and Boiler Systems  

The use of thermoelectric generators (TEGs) in heating systems enables autonomous supply of power to automatic safety devices, creation of optimized gas mixtures, and automation and precise temperature control of exhaust gas and heat carriers. It is particularly important to make heating systems independent of the district electric grid. Results of research and development efforts on a TEG for supplying power to electric devices of self-contained heating and boiler systems are presented. A TEG physical model is proposed, and results of computer simulation and optimization of its basic power and design parameters are given. Two TEG design variants (single and double sided) are considered. Their advantages and shortcomings are discussed. On the basis of theoretical calculations, a prototype ...

373

LPG fueled diesel engine using diethyl ether with exhaust gas recirculation  

The present investigation was to study the effect of Exhaust Gas Recirculation (EGR) on homogeneous charge ignition engine. A stationary four stroke, single cylinder, direct injection (DI) diesel engine capable of developing 3.7 kW at 1500 rpm was modified to operate in HCCI mode. In the present work the diesel engine was operated on 100% Liquified Petroleum Gas (LPG). The LPG has a low cetane number Formula Not Shown , therefore Diethyl ether (DEE) was added to the LPG for ignition purpose. DEE is an excellent ignition enhancer (cetane number >125) and has a low auto ignition temperature (160 degreeC). Experimental results showed that by EGR technique, at part loads the brake thermal efficiency increases by about 2.5% and at full load, NO concentration could be considerably reduced to abo...

374

LPG fueled diesel engine using diethyl ether with exhaust gas recirculation  

The present investigation was to study the effect of Exhaust Gas Recirculation (EGR) on homogeneous charge ignition engine. A stationary four stroke, single cylinder, direct injection (DI) diesel engine capable of developing 3.7 kW at 1500 rpm was modified to operate in HCCI mode. In the present work the diesel engine was operated on 100% Liquified Petroleum Gas (LPG). The LPG has a low cetane number (<3), therefore Diethyl ether (DEE) was added to the LPG for ignition purpose. DEE is an excellent ignition enhancer (cetane number >125) and has a low auto ignition temperature (160 C). Experimental results showed that by EGR technique, at part loads the brake thermal efficiency increases by about 2.5% and at full load, NO concentration could be considerably reduced to about 68% as compared to LPG operation without EGR. However, higher EGR percentage affects the combustion rate and significant reduction in peak pressure at maximum load. (author)

375

Remarkable improvement of NOx-PM trade-off in a diesel engine by means of bioethanol and EGR  

In order to realize a premixed compression ignition (PCI) engine, the effects of bioethanol-gas oil blends and exhaust gas recirculation (EGR) on PM-NOx trade-off have been investigated focusing on ignition delay, premixed combustion, diffusion combustion, smoke, NOx and thermal efficiency. The present experiment was done by increasing the ethanol blend ratio and ethanol and by increasing the EGR ratio in a single cylinder direct injection diesel engine. It is found that a remarkable improvement in PM-NOx trade-off can be achieved by promoting the premixing based on the ethanol blend fuel having low evaporation temperature, large latent heat and low cetane number as well, in addition, based on a marked elongation of ignition delay due to the low cetane number fuel and the low oxygen intake...

376

Theoretical simulation and experimental research on the system of air source energy independence driven by internal-combustion engine  

Presents a new system of air source energy independence driven by internal-combustion engine (EIICE), which used natural gas or other fuels as an independent input energy, and could provide the heating, cooling and hot water for the buildings efficiently. It also could provide electricity for electric equipments of the system. The performance of air source EIICE system was investigated theoretically and experimentally. The experimental and simulation results indicated that the heat capacity of plate heat exchanger (P-HE), heat recovered from exhaust gas heat exchanger (EG-HE), input power of compressor, output power of engine and fuel consumption increased with the increase of the rotary speed, water flow rate of the P-HE and evaporation temperature. Heat recovered from the cylinder jacket...

377

Exhaust gas catalysts based on metal phthalocyanines. Pt. 1  

A large number of compounds have been investigated with a view to their suitability as catalysts for NOsub(x) reduction. One of the most recent developments is the use of zeolite catalysts for this purpose, while another line of research focuses on metal phthalocyanines (MPc). MPc of the first transition series have been found to be satisfactory catalysts for NO reduction with hydrogen at temperatures between 180 and 425/sup 0/C. MPc pretreated with NO or O/sub 2/ have much higher NO reduction activities than pure MPc. One should keep in mind, however, that these findings have been obtained in laboratory-scale gas chromatography studies on pure gases and high-purity MPc in pulsed operation. Using the example of a catalyst produced from CuPc, the authors describe the transfer of the results obtained in the basic studies to a functional model in which the catalytic processes can be studied under conditions close to those in exhaust gas.

378

Ignition and extinction in partial catalytic oxidation of methane/oxygen mixtures with large H{sub 2}O and CO{sub 2} dilution  

The catalytic partial oxidation (CPO) of methane/oxygen mixtures with large exhaust gas dilution has attracted increased attention in gas-turbines of new power generation cycles that aim at reduced NO{sub x} and CO{sub 2} emissions. In the present work, ignition and extinction of fuel-rich methane/oxygen mixtures diluted with H{sub 2}O and CO{sub 2} is investigated experimentally and numerically at 5 bar. Catalytic ignition (light-off) was well-reproduced by the numerical model. The chemical impact of H{sub 2}O dilution, although important during the time evolution of the light-off event, was shown to be minimal on the catalytic ignition delay times. A large hysterisis in the ignition/extinction curve was observed, allowing for stable reactor operation at temperatures as low as 470K. (orig.)

379

Study Pinpoints Sources of Polluting Vehicle Emissions (Fact Sheet)  

Unburned lubricant produces 60%-90% of organic carbon emissions. While diesel fuel is often viewed as the most polluting of conventional petroleum-based fuels, emissions from gasoline engines can more significantly degrade air quality. Gasoline exhaust is at least as toxic on a per-unit-mass basis as diesel exhaust, and contributes up to 10 times more particulate matter (PM) to the emission inventory. Because emissions from both fuels can gravely impact health and the environment, researchers at the National Renewable Energy Laboratory (NREL) launched a study to understand how these pollutants relate to fuels, lubricants, and engine operating conditions. NREL's Collaborative Lubricating Oil Study on Emissions (CLOSE) project tested a variety of vehicles over different drive cycles at moderate (72 F) and cold (20 F) temperatures. Testing included: (1) Normal and high-emitting light-, medium-, and heavy-duty vehicles; (2) Gasoline, diesel, and compressed natural gas (CNG)-powered vehicles; (3) New and aged lubricants representative of those currently on the market; and (4) Gasoline containing no ethanol, E10, Texas-mandated low-emission diesel fuel, biodiesel, and CNG. The study confirmed that normally functioning emission control systems for gasoline light-duty vehicles are very effective at controlling organic carbon (OC) emissions. Diesel vehicles without aftertreatment emission control systems exhibited OC emissions approximately one order of magnitude higher than gasoline vehicles. High-emitter gasoline vehicles produced OC emissions similar to diesel vehicles without exhaust aftertreatment emission control. Exhaust catalysts combusted or converted more than 75% of lubricating oil components in the exhaust gases. Unburned crankcase lubricant made up 60%-90% of OC emissions. This OC represented 20%-50% of emitted PM in all but two of the vehicles. Three-way catalysts proved effective at reducing most of the OC. With high PM emitters or vehicles with deteriorated aftertreatment, high-molecular-weight fuel components and unburned lubricant were emitted at higher rates than in vehicles in good repair, with functioning emissions systems. Light-duty gasoline, medium-duty diesel, and heavy-duty natural gas vehicles produced more particles with fresh oil than with aged oil. The opposite trend was observed in light- and medium-duty high PM emitters. This effect was not readily apparent with heavy-duty diesel vehicles, perhaps because the lubricant represented a much smaller fraction of the total PM in those trucks.

380

An experimental study on the effects of different opening ranges of waste-gate on the exhaust soot emission of a turbo-charged DI diesel engine  

This experimental study was conducted to investigate the effects of different opening ranges of waste-gate of a turbo-charged DI diesel engine on improving the exhaust soot emission. Different opening ranges of waste-gate were supplied using an adjustable spring to load the actuating rod of the waste-gate in which, increasing the opening range of the waste-gate decreases the inlet manifold pressure. In this study, the maximum inlet manifold pressures which were supplied by changing the opening range of waste-gate were 0.1 bar, 0.23 bar, 0.26 bar and 0.52 bar over atmosphere and experiments were conducted under the ECE-R49, 13 mode standard test. At each mode of the test, soot emission was recorded and then brake specific soot emission was calculated. Results indicate that, soot emission decreases with increasing the maximum inlet manifold pressure from 0.1 bar to 0.23 bar. This reduction may be due to increasing the intake-air temperature which results in reduction of ignition delay that prolongs the late combustion phase. This improves the soot burnout process because enough time and sufficient in-cylinder temperature are available at the late combustion phase prior to exhaust valve opening. While for the higher maximum inlet manifold pressures from 0.23 bar to 0.52 bar, although there are enough time at the late combustion phase, but the soot emission increases which could be due to more reduction of the in-cylinder gas temperature at the end of combustion before EVO. (author)

 
 
 
 
381

Transient characteristics of diesel emissions during starting; Shidoji ni okeru diesel emission no kato tokusei  

Transient characteristics of the exhaust gas emissions of THC, NO{sub x} and so on during starting operation in a DI diesel engine and the influence of engine operating parameters and fuel properties on them were investigated. The results indicated that THC concentration just after onset of starting increased until about 50th to 200th cycle after the starting when the fuel deposited on the combustion chamber showed the maximum, and then decreated to reach a steady state value after about 1000 cycles when the piston wall temperature became almost constant. NO{sub x} showed an initial higher peak at about 6th cycle after the starting, and increased to reach the steady state value after about 1000 cycles. Exhaust odor during starting had a strong correlation with the THC while the odor decreased much after reaching the maximum. Except just after the onset of starting, an increase in piston wall temperature resulted in a decrease in the THC concentration and an increase in the NO{sub x}. The THC increased significantly with increased fuel injection amount and with decreased cranking speeds while there was little effect of fuel injection timings. The THC during the starting increased with fuels with higher viscosity, higher 90% distillation temperature, and lower ignitability. (author)

382

Development and testing of a combustion system for low emission removal of exhaust gases containing hydrocarbons. Planning of a pilot combustion chamber and performance of combustion tests. Entwicklung und Erprobung eines Verbrennungssystems zur schadstoffarmen Beseitigung kohlenwasserstoffhaltiger Abgase. Planung einer Versuchsbrennkammer und Durchfuehrung von Brennversuchen  

Exhaust gases and exit air compositions with different hydro-carbon concentrations selected according to previous experience with combustion processes were burned in select performance ranges in an experimental set-up with installed exhaust gas dosage and their decomposition in the combustion system was studied. The tests served to further develop the dosage system and the technical control and monitoring concept including protective equipment and to adapt these to experimental conditions with ceramic flame ducts. The insights gained in the laboratory at a bench scale were then verified in a subsequent large-scale test in which the combustion equipment was adjusted to operating and exhaust gas conditions as they occur in practice. (orig./EF)

383

Exhaust gas afterburner  

This patent describes an exhaust gas afterburner device adapted for installation between an exhaust manifold and a corresponding portion of the engine block of an internal combustion engine. The device comprises: a spacer sandwiched between portions of two sheet metal members forming a gasket section of the device, the gasket section surrounding at least one exhaust gas port, a plenum section formed by remaining portions of the members, and wall sections defining passageways extending from the interior of the plenum section to the port and an air supply inlet on the plenum.

384

Exhaust systems for combustion products: solutions and innovations; Les systemes d'evacuation des produits de combustion: solutions et innovations  

This document summarizes the content of a conference-debate organized by Cegibat, the information service of Gaz de France (GdF) for building engineering professionals, about the exhaust systems for gas boilers: 1 - overview of airtight systems: horizontal suction-grip duct, vertical suction-grip duct, collective ducts for tight boilers, separate ducts; 2 - example of products: separate ducts; reuse of an individual smoke duct; 3 - overview of non-airtight exhaust systems: individual smoke ducts, collective smoke ducts, ventilation-gas systems; 4 - examples of non-airtight systems: diagnosis and rehabilitation of smoke ducts, low pressure mechanical exhaust system; 5 - works in progress and perspectives of evolution. (J.S.)

385

H gas turbine combined cycle  

A major step has been taken in the development of the Next Power Generation System--``H`` Technology Combined Cycle. This new gas turbine combined-cycle system increases thermal performance to the 60% level by increasing gas turbine operating temperature to 1,430 C (2,600 F) at a pressure ratio of 23 to 1. Although this represents a significant increase in operating temperature for the gas turbine, the potential for single digit NOx levels (based upon 15% O{sub 2}, in the exhaust) has been retained. The combined effect of performance increase and environmental control is achieved by an innovative closed loop steam cooling system which tightly integrates the gas turbine and steam turbine cycles. The ``H`` Gas Turbine Combined Cycle System meets the goals and objectives of the DOE Advanced Turbine System Program. The development and demonstration of this new system is being carried out as part of the Industrial/Government cooperative agreement under the ATS Program. This program will achieve first commercial operation of this new system before the end of the century.

386

A Refined Two-Zone Heat Release Model for Combustion Analysis in SI Engines  

A refined two-zone heat release model for combustion diagnostics in spark-ignition (SI) engines was developed and assessed. The novelty of the model includes the following improvements. A more general complex-variable formulation of Newton's convection law was applied for modeling the instantaneous surface-averaged heat flux so as to take the unsteadiness of gas-wall temperature difference into account. A CAD procedure was introduced to estimate the heat-transfer wall areas of the burned- and unburned-zone for assigned geometric features of the flame front. The energy conservation law was applied to the unburned-gas zone instead of the isentropic law that is commonly used to evaluate the temperature of the unburned gas. The calibration of the cumulative mass-fraction burned at the end of the flame propagation process was carried out through an overall energy balance of the whole cylinder charge during combustion. The unreleased energy predicted at the end of the flame propagation was related to the combustion efficiency stemming from the exhaust-gas composition. The new heat release model was shown to be an accurate means of combustion diagnostics for SI engines through its application to the analysis of combustion in a multivalve engine fueled by either natural gas or gasoline under a significant sample of operating conditions.   

387

DEVELOPMENT AND DEMONSTRATION OF A SUPERCRITICAL HELIUM-COOLED CRYOGENIC VISCOUS COMPRESSOR PROTOTYPE FOR THE ITER VACUUM SYSTEM  

As part of the vacuum system for the ITER fusion project, a cryogenic viscouscompressor (CVC) is being developed to collect hydrogenic exhaust gases from the toruscryopumps and compress them to a high enough pressure by regeneration for pumping tothe tritium reprocessing facility. Helium impurities that are a byproduct of the fusionreactions pass through the CVC and are pumped by conventional vacuum pumps andexhausted to the atmosphere. Before the development of a full-scale CVC, a representative,small-scale test prototype was designed, fabricated, and tested. With cooling provided bycold helium gas, hydrogen gas was introduced into the central column of the test prototypepump at flow rates between 0.001 g/s and 0.008 g/s. Based on the temperatures and flowrates of the cold helium gas, different percentages of hydrogen gas were frozen to the column surface wall as the hydrogen gas flow rate increased. Results from the measured temperatures and pressures will form a benchmark that will be used to judge future heattransfer enhancements to the prototype CVC and to develop a computational fluid dynamicmodel that will help develop design parameters for the full-scale CVC.

388

Development and demonstration of a supercritical helium-cooled cryogenic viscous compressor prototype for the iter vacuum system  

As part of the vacuum system for the ITER fusion project, a cryogenic viscouscompressor (CVC) is being developed to collect hydrogenic exhaust gases from the toruscryopumps and compress them to a high enough pressure by regeneration for pumping tothe tritium reprocessing facility. Helium impurities that are a byproduct of the fusionreactions pass through the CVC and are pumped by conventional vacuum pumps andexhausted to the atmosphere. Before the development of a full-scale CVC, a representative,small-scale test prototype was designed, fabricated, and tested. With cooling provided bycold helium gas, hydrogen gas was introduced into the central column of the test prototypepump at flow rates between 0.001 g/s and 0.008 g/s. Based on the temperatures and flowrates of the cold helium gas, different percentages of hydrogen gas were frozen to the column surface wall as the hydrogen gas flow rate increased. Results from the measured temperatures and pressures will form a benchmark that will be used to judge future heattransfer enhancements to the prototype CVC and to develop a computational fluid dynamicmodel that will help develop design parameters for the full-scale CVC.

389

Cooling facility of nuclear power plant  

In a cooling device of a nuclear power plant, an exhaust pipe for an incondensible gas is branched. One of the branched exhaust pipes is opened in a pressure suppression pool water in a suppression chamber containing pool water and the other is opened at a lower portion of a dry well incorporating a pressure vessel. In a state where the pressure in the dry well is higher than that in the suppression chamber, an off-gas is exhausted effectively by way of the exhaustion pipe in communication with the suppression chamber. In a state where there is no difference between the pressures and the opening end of the exhaustion pipe in communication with the suppression chamber is sealed with water, off-gas is exhausted by way of the exhaustion pipe in communication with the lower portion of the dry well. Then, since the incondensible gas in a heat transfer pipe is not accumulated, after-heat can be removed efficiently. Satisfactory cooling is maintained even after the coincidence of the pressures in the dry well with that in the suppression chamber, to decrease a pressure in a reactor container. (N.H.).

390

Combined split engine and closed loop mixture control operation with enriched fuel during partial cylinder mode  

A control system for a multi-cylinder internal combustion engine comprises a split engine control unit for operating the engine on partial cylinders when reduced engine power can adequately operate the vehicle, and first and second upstream exhaust conduits for directing exhaust gases from first and second group cylinders respectively to a common junction to which a downstream exhaust conduit is connected for emitting the gases to the atmosphere. A first set of an exhaust gas sensor and catalytic converter is disposed in the first conduit to be exposed to the stream of gases exhausted from the second group cylinders which are activated at all times and a second set of an exhaust gas sensor and catalytic converter is disposed in the common downstream conduit to be exposed to the stream of gases exhausted from the first group cylinders directed through the first conduit and to the gases passed through the upstream catalytic converter in the second conduit. A feedback control circuit is responsive selectively to a signal from the first gas sensor during the partial cylinder operation for correcting the mixture ratio to a rich side of stoichiometry to promote reduction of the nox component in the upstream converter and oxidation of hc and co components in the downstream converter, and to a signal from the second gas sensor during the full cylinder operation for correcting the mixture ratio to a point at or near stoichiometry to promote simultaneous reduction and oxidation processes in both of the converters.

391

Control system for closed loop mixture correction and split engine operation  

A control system for a multi-cylinder internal combustion engine comprises a split engine control unit for operating the engine on partial cylinders when reduced engine power can adequately operate the vehicle, and first and second exhaust conduits for directing exhaust gases from first and second group cylinders respectively to a common junction to which a common exhaust conduit is connected for directing the gases to the atmosphere. A first set of an exhaust gas sensor and catalytic converter is disposed in the first conduit to be exposed to the stream of gases exhausted from the second group cylinders which are activated at all times and a second set of an exhaust gas sensor and catalytic converter is disposed in the common conduit to be exposed to the stream of gases exhausted from the first group cylinders directed through the first conduit and to the gases passed through the upstream side catalytic converter in the second conduit. A feedback control circuit is responsive selectively to a signal from the first gas sensor during the partial cylinder operation for correcting the ratio of mixture supplied to the second group cylinders and to a signal from the second gas sensor during the full cylinder operation for correcting the ratio of mixture supplied to all the cylinders.

392

Development of supplementary firing burner for gas turbine cogeneration system; Mise au point d'un bruleur a deux niveaux de combustion pour un systeme a cogeneration d'une turbine a gaz  

This supplementary firing burner helps a waste heat boiler increase output by reheating gas turbine exhaust (O{sub 2}=15%) with no or little additional air. That is to say, this burner can raise the efficiency of gas turbine cogeneration. Here, we describe out newly developed supplementary firing burner which is high-performance in terms of down-sizing, low-NO{sub x} emission (< 60 ppm, at O{sub 2}=0%), low exhaust gas pressure loss (< 0.6 kPa) and high turndown ratio (>8:1). The burner has a three stage exhaust gas inlet so that both gas turbine exhaust and fresh air can be used. Further, we show two examples of cogeneration system in which the burner is used. One is an industrial gas turbine re-powering system. This system can raise efficiency (total = 95%) only by changing the existing power boiler's burner with the newly developed one. The burner can be operated even with fresh air, so when the gas turbine suddenly stops, the power boiler will work without a spare boiler or burner. The other is a Cheng Cycle gas turbine system. Its exhaust gas O{sub 2} content is lower ({approx} 10%), and the burner is fired by adding minimum fresh air. The burner structure is different from that in the other system, but it can burn with fresh air. We already installed the supplementary Finning Burner in 11 kinds of cogeneration systems. With these systems, we are contributing to energy conservation and environmental protection. (authors)

393

IGNITION IMPROVEMENT OF LEAN NATURAL GAS MIXTURES  

This report describes work performed during a thirty month project which involves the production of dimethyl ether (DME) on-site for use as an ignition-improving additive in a compression-ignition natural gas engine. A single cylinder spark ignition engine was converted to compression ignition operation. The engine was then fully instrumented with a cylinder pressure transducer, crank shaft position sensor, airflow meter, natural gas mass flow sensor, and an exhaust temperature sensor. Finally, the engine was interfaced with a control system for pilot injection of DME. The engine testing is currently in progress. In addition, a one-pass process to form DME from natural gas was simulated with chemical processing software. Natural gas is reformed to synthesis gas (a mixture of hydrogen and carbon monoxide), converted into methanol, and finally to DME in three steps. Of additional benefit to the internal combustion engine, the offgas from the pilot process can be mixed with the main natural gas charge and is expected to improve engine performance. Furthermore, a one-pass pilot facility was constructed to produce 3.7 liters/hour (0.98 gallons/hour) DME from methanol in order to characterize the effluent DME solution and determine suitability for engine use. Successful production of DME led to an economic estimate of completing a full natural gas-to-DME pilot process. Additional experimental work in constructing a synthesis gas to methanol reactor is in progress. The overall recommendation from this work is that natural gas to DME is not a suitable pathway to improved natural gas engine performance. The major reasons are difficulties in handling DME for pilot injection and the large capital costs associated with DME production from natural gas.

394

Analysis of oxygen-enhanced combustion of gas power cycle  

The majority of combustion processes use air as oxidant, roughly taken as 21% O{sub 2} and 79% N{sub 2}, by volume. In many cases, these processes can be enhanced by using an oxidant that contains higher proportion of O{sub 2} than in air. This is known as oxygen-enhanced combustion or OEC, and can bring important benefits like higher thermal efficiencies, lower exhaust gas volumes, higher heat transfer efficiency, reduction fuel consumption, reduced equipment costs and substantially pollutant emissions reduction. Within this scenario, this paper aims to investigate the influence of 21-30% oxygen concentration on the performance of a air-fired natural gas fueled power plant. This power plant operates under a Brayton cycle with models with the help of an air flow splitter after the compressor output in order to dose the oxygen rate of combustion and to keep the flue gas intake of the turbine at a prescribed temperature. Simulations shows that the enhancing of the oxidant stream reduced fuel consumption of about 10%, driven by higher adiabatic flame temperatures, which improves thermal and heat transfer efficiencies. A conclusion obtained is that the use of oxygen in higher proportions can be a challenge to retrofit existing air-fired natural gas power turbine cycles, because of the technological limitation of its materials with higher flame temperatures. (author)

395

Catalyst for utilization of methane in selective catalytic reduction of NO{sub x}, Task 2.6  

Selective catalytic reduction (SCR) of nitrogen oxides(NO{sub x}) in flue gas or engine exhaust gas with hydrocarbons as the reductant has great potential for less expense, less pollution, and easier operation than SCR with ammonia. Methane is the preferred reducing gas because of its low cost and low toxicity. Stable, low-cost catalysts for SCR with methane are required to demonstrate this technology for controlling NO{sub x} emissions. Several cobalt and nickel catalysts on synthetic clay and uranium oxide supports were investigated for their activities in reducing NO{sub x} with methane in the presence of air. The efficiency of the synthetic clay-supported nickel and cobalt catalysts for nitric oxide (NO) reduction with methane as the reducing gas was poor. The nickel oxide-uranium oxide catalyst, which was chosen for its high stability, was also ineffective. Results from the two-step experiments conducted at two-temperatures produced some interesting information on the reactions of methane with the catalysts and the reactivity of the carbonaceous intermediate. The carbonaceous material formed from methane dissociation at 450{degrees}C not only reduces NO to N{sub 2}O at lower temperatures, but also prevents oxidation of NO to NO{sub 2}. Unfortunately, the carbonaceous forms that reduce the NO are not available for reactions at 400{degrees}C in the presence of oxygen. A two-step process employing this chemistry would be difficult because the catalyst would have to be cycled between the two temperatures. Also the desired reduction to nitrogen is not very efficient.

396

Task 2.6 - Catalyst for Utilization of Methane in Selective Catalytic Reduction of NOx: Topical report, July 1, 1995  

Selective catalytic reduction (SCR) of nitrogen oxides (NO{sub x}) in flue gas or engine exhaust gas with hydrocarbons as the reductant has great potential for less expense, less pollution, and easier operation than SCR with ammonia. Methane is the preferred reducing gas because of its low cost and low toxicity. Stable, low-cost catalysts for SCR with methane are required to demonstrate this technology for controlling NO{sub x} emissions. Several cobalt and nickel catalysts on synthetic clay and uranium oxide supports were investigated for their activities in reducing NO{sub x} with methane in the presence of air. The efficiency of the synthetic clay-supported nickel and cobalt catalysts for nitric oxide (NO) reduction with methane as the reducing gas was poor. The nickel oxide-uranium oxide catalyst, which was chosen for its high stability, was also ineffective. Results from the two-step experiments conducted at two temperatures produced some interesting information on the reactions of methane with the catalysts and the reactivity of the carbonaceous intermediate. The carbonaceous material formed from methane dissociation at 450{degrees}C not only reduces NO to N{sub 2}O at lower temperatures, but also prevents oxidation of NO to NO{sub 2}. Unfortunately, the carbonaceous forms that reduce the NO are not available for reactions at 400{degrees}C in the presence of oxygen. A two-step process employing this chemistry would be difficult because the catalyst would have to be cycled between the two temperatures. Also the desired reduction to nitrogen is not very efficient.

397

Helium turbine power generation in high temperature gas reactor  

This paper presents studies on the helium turbine power generator and important components in the indirect cycle of high temperature helium cooled reactor with multi-purpose use of exhaust thermal energy from the turbine. The features of this paper are, firstly the reliable estimation of adiabatic efficiencies of turbine and compressor, secondly the introduction of heat transfer enhancement by use of the surface radiative heat flux from the thin metal plates installed in the hot helium and between the heat transfer coil rows of IHX and RHX, thirdly the use of turbine exhaust heat to produce fresh water from seawater for domestic, agricultural and marine fields, forthly a proposal of plutonium oxide fuel without a slight possibility of diversion of plutonium for nuclear weapon production and finally the investigation of GT-HTGR of large output such as 500 MWe. The study of performance of GT-HTGR reduces the result that for the reactor of 450 MWt the optimum thermal efficiency is about 43% when the turbine expansion ratio is 3.9 for the turbine efficiency of 0.92 and compressor efficiency of 0.88 and the helium temperature at the compressor inlet is 45degC. The produced amount of fresh water is about 8640 ton/day. It is made clear that about 90% of the reactor thermal output is totally used for the electric power generation in the turbine and for the multi-puposed utilization of the heat from the turbine exhaust gas and compressed helium cooling seawater. The GT-Large HTGR is realized by the separation of the pressure and temperature boundaries of the pressure vessel, the increase of burning density of the fuel by 1.4 times, the extention of the nuclear core diameter and length by 1.2 times, respectively, and the enhancement of the heat flux along the nuclear fuel compact surface by 1.5 times by providing riblets with the peak in the flow direction. (J.P.N.).

398

Muffler with catalyst for internal combustion engine  

A muffler for an internal combustion engine is described consisting of: a casing; a catalyst disposed within the casing to convert noxious components of exhaust gas received from the engine at an upstream side of the catalyst into harmless gases at a downstream side; an exhaust gas inlet pipe including an inlet pipe section having a venturi section means for introducing secondary air into the exhaust gas inlet pipe to mix with exhaust gas, and an extension pipe section coaxially connected with the inlet pipe section and extended downstream of the venturi section means for conveying the mixture of exhaust gas and secondary air in an original direction through the casing, the extension pipe section having a length of at least two times the inner diameter of the extension pipe section; first flow reversal and supply means for reversing the direction of flow of the mixture of exhaust gas and secondary air received from the extension pipe and supplying the mixture to the upstream side of the catalyst, second flow reversal and supply means at the downstream side of the catalyst for receiving and reversing the direction of flow of harmless gases to the original direction, and means communicating between the second flow reversal and supply means and the atmosphere for discharging the harmless gases.

399

Blowby control device of alcohol fuel engine  

The structure of an alcohol fuel engine is not basically different from that of a gasoline engine and from the viewpoint of preventing pollution caused by the exhaust gas, there is a type of alcohol fuel engine equipped with a blowby gas treatment device which makes the blowby gas return to the air intake passage of the engine concerned for its recombustion in the combustion chamber of the engine. However, since alcohol has its boiling point lower than that of gasoline and the composition of its components is relatively pure, a great deal of alcohol evaporate instantly and the alcohol rich blowby gas is forced to return abruptly into the intake air inviting engine stalling particularly during the idling condition, when warming-up of the alcohol fuel engine progresses to the extent that the oil temperature of the oil pan reaches the boiling point of alcohol. In order to solve the above problems, this invention proposes to provide an alcohol fuel engine which has a blowby gas treatment device with a measure to detect the vaporizing condition of alcohol on the side of engine itself during its warming-up condition and a measure to control the blowby gas flow corresponding to the detection output of the above detection measure. (2 figs)

400

Engineering development of coal-fired high performance power systems, Phase 2 and 3. Quarterly progress report, October 1--December 31, 1995  

The goals of the program are to develop a coal-fired high performance power generation system (HIPPS) by the year 2000 that is capable of: >47% thermal efficiency (HHV); NO{sub x}, SO{sub x} and particulates {ge} 10% NSPS; coal {ge} 65% of heat input; all solid wastes benign; and cost of electricity 90% of present plant. The HIPPS generating plant integrates a combustion gas turbine/HRSG combined cycle arrangement with an advanced coal-fired boiler. The unique feature of the HIPPS plant is the partial heating of gas turbine (GT) compressor outlet air using energy released by firing coal in the high temperature advanced furnace (HITAF). The compressed air is additionally heated prior to entering the GT expander section by burning natural gas. Energy available, in the gas turbine exhaust and in the HITAF flue gas are used in a steam cycle to maximize energy production. The HIPPS plant arrangement is thus a combination of existing technologies (gas turbine, heat recovery boilers, conventional steam cycle) and new technologies (the HITAF design especially the heater located in the radiant section). Work reported herein is from Task 1.3, HIPPS Commercial Design and Task 2.2, HITAF Air Heaters.

 
 
 
 
401

Integral unitary manifold-muffler-catalyst device  

An integral manifold-muffler-catalyst device for an internal combustion engine having a plurality of combustion cylinders generating exhaust gases is described, comprising: (a) a monolithic catalyst having a plurality of aligned passages for effecting laminar flow of the exhaust gases therethrough; (b) a high temperature resistant chamber assembly for close coupling the catalyst to the engine having (i) an expansion chamber for substantially dissipating low frequency sound waves of the exhaust gases and for modifying high frequency sound waves of the exhaust gases and (ii) manifolding passages at one side of the expansion chamber for collecting and delivering the exhaust gases from the cylinders to the expansion chamber; and (c) means for effecting converging flow from the expansion chamber to and substantially the full entrance face of the aligned passages and for effecting converging flow from the catalyst, the dual-stage convergence reflecting and attenuating high frequency sound waves carried by the exhaust gases by interference.

402

California Institute for Energy Efficiency 1991 annual report  

This 1991 annual report of the California Institute for Energy Efficiency (CIEE) presents current research topics along with institutional events. Various modes for energy conservation are reported including: residential and commercial air distribution systems, thermal energy storage, natural gas and electric powered vehicles, gas-filled thermal insulation panels, exhaust hoods, shade trees and white surfaces, industrial natural gas burners, and lighting systems. (GHH)

403

Energy-efficient system for automatic control of gas-air duct of heating boiler  

A new energy-efficient technique to control the gas-air duct of a heating boiler is examined. The technique consists in simultaneous regulating the gas-air duct resistance by means of guiding devices (of the damper) and changing a frequency of the supply voltage of motors of the flue gas exhauster and blower. The implementation results are also considered.

404

77 FR 57001 - Airworthiness Directives; Pratt & Whitney Canada, Auxiliary Power Units  

...auxiliary power units (APUs) approved...of the rear gas generator...support, and turbine exhaust duct...Auxiliary Power Units have experienced...High Pressure Turbine (HPT) blade...of the rear gas generator...auxiliary power units (APUs) approved...high-pressure turbine blade fracture...of the rear gas...

405

Methods for monitoring and diagnosing the efficiency of catalytic converters  

The evolution of methods concerned with on-board (OBD) and non-OBD monitoring and diagnosing of efficiency of catalytic converters of internal combustion engines is described based on patents and published patent applications. Non-patent references are also used. The basic principles of modern catalytic converters are described in an extensive Introduction, where the importance of monitoring and diagnosing the efficiency of catalytic converters is demonstrated. The book is divided into four parts. The first part describes methods involving the use of oxygen or air/fuel ratio exhaust gas sensors to determine the oxygen storage capacity of a catalytic converter. The second part describes methods involving the use of temperature sensors to determine the exothermic reaction capacity of a catalytic converter. The third part describes all other methods existing in patent literature that monitor and diagnose the efficiency of catalytic converters. The great majority of the methods of the third part involves exhaust gas concentration measurements. The fourth part comprises a general discussion of all methods described. In the beginning of each part, a short introduction is given to explain the problem that the methods attempt to solve. The methods in each part are presented in chronological order per patent applicant. This helps to evaluate how the patent applicant has improved his methods over time. A patent number index with information about the patent applicants, inventors, priorities and patent-families, an inventor index, a company index and a subject index can be found at the end of the book. 34 refs.

406

Gas turbine cycles with solid oxide fuel cells. Part 1: Improved gas turbine power plant efficiency by use of recycled exhaust gases and fuel cell technology  

The energy conversion efficiency of the combustion process can be improved if immediate contact of fuel and oxygen is prevent4ed and an oxygen carrier is used. In a previous paper (Harvey et al., 1992), a gas turbine cycle was investigated in which part of the exhaust gases are recycled and used as oxygen-carrying components. For the optimized process, a theoretical thermal efficiency of 66.3% was achieved, based on the lower heating value (LHV) of the methane fuel. One means to further improve the exergetic efficiency of a power cycle is to utilize fuel cell technology. Solid oxide fuel cells (SOFC) have many features that make them attractive for utility and industrial applications. In this paper, the authors will therefore consider SOFC technology. In view of their high operating temperatures and the incomplete nature of the fuel oxidation process, fuel cells must be combined with conventional power generation technology to develop power plant configurations that are both functional and efficient. In this paper, the authors will show how monolithic SOFC (MSOFC) technology may be integrated into the previously described gas turbine cycle using recycled exhaust gases as oxygen carriers. An optimized cycle configuration will be presented based upon a detailed cycle analysis performance using Aspen Plus[trademark] process simulation software and a MSOFC fuel cell simulator developed by Argonne National Labs. The optimized cycle achieves a theoretical thermal efficiency of 77.7%, based on the LHV of the fuel.

407

Use of secondary energy resources  

At the seminar ''Use of Secondary Energy Resources at Enterprises of the Leningrad and Leningrad Oblast'' (1979, Leningrad) twelve papers and fourteen reports were heard covering questions of improving the efficient use of secondary energy (SER), improvement in the heat recovery and energy technological equipment, analysis of the condition and outlook for the use of SER in industry. The output of SER is one billion Gcal, including low-potential SER 50%, and physical heat of the exhaust gases 30%. The installation behind the boilers of industrial enterprises of contact HE with active adapter for recovering low-potential steam-gas streams with temperature less than or equal to300/sup 0/C makes it possible to conserve 8-12% of the natural gas and mazut and 20-35% of the cut peat. At the Volkhovskiy aluminum plant, boiler-recovery units have been installed behind the furnaces for combustion of sulfur, units for monitering the quality and supply of thermowaters of evaporation of the soda conversion for chemical water purification and in unit for use of heat of the exhaust gases from the furnaces of sintering the nepheline burden. The energy conservation was 53,000 tons of conventional fuel per year.

408

Experimental investigation of control of NO{sub x} emissions in biodiesel-fueled compression ignition engine  

Biodiesel is an alternative fuel consisting of the alkyl esters of fatty acids from vegetable oils or animal fats. Vegetable oils are produced from numerous oil seed crops (edible and non-edible), e.g., rapeseed oil, linseed oil, rice bran oil, soybean oil, etc. Research has shown that biodiesel-fueled engines produce less carbon monoxide (CO), unburned hydrocarbon (HC), and particulate emissions compared to mineral diesel fuel but higher NO{sub x} emissions. Exhaust gas recirculation (EGR) is effective to reduce NO{sub x} from diesel engines because it lowers the flame temperature and the oxygen concentration in the combustion chamber. However, EGR results in higher particulate matter (PM) emissions. Thus, the drawback of higher NO{sub x} emissions while using biodiesel may be overcome by employing EGR. The objective of current research work is to investigate the usage of biodiesel and EGR simultaneously in order to reduce the emissions of all regulated pollutants from diesel engines. A two-cylinder, air-cooled, constant speed direct injection diesel engine was used for experiments. HCs, NO{sub x}, CO, and opacity of the exhaust gas were measured to estimate the emissions. Various engine performance parameters such as thermal efficiency, brake specific fuel consumption (BSFC), and brake specific energy consumption (BSEC), etc. were calculated from the acquired data. Application of EGR with biodiesel blends resulted in reductions in NO{sub x} emissions without any significant penalty in PM emissions or BSEC. (author)

409

The new platinum high temperature sensor HTS 1000 S from Beru; Der neue Platin-Hochtemperatursensor HTS 1000 S von Beru  

Beru engineers have developed a high temperature sensor for exhaust gas applications, the HTS 1000 S, which meets all the demands of the automotive industry including a high price/performance ratio. As a compromise between signal yield and accuracy a platinum RTD is used as sensing element. It is fitted in a protection sheath made of Cr-Ni-Steel which is also employed for glow plugs. The most important feature of the new sensor is its accuracy. Response time comes next in importance; it is kept low by the fast heat transfer from the exhaust gas to the sensing element. This is due to the small diameter and thin wall of the protection sheath. The response time of the new sensor comes close to the time constant of a similarly protected thermocouple. High accuracy and signal stability are achieved by protecting the platinum sensing element against any catalytic reactions. This is achieved by providing at all times a sufficiently high partial pressure of oxygen within the sheath through an airpermeable membrane. (orig.) [Deutsch] Fuer den Einsatz im Automobil gewinnen Sensoren zunehmend an Bedeutung. Ein Einsatzfall, der fuer zukuenftige Motorenkonzepte immer wichtiger wird, ist die Messung der Abgastemperatur als Regelgroesse fuer das Motormanagement oder als Schutz- und Ueberwachungsparameter. Die Leistungsfaehigkeit und Lebensdauer von Katalysatoren (Dreiwege oder Denox) laesst sich so betraechtlich erhoehen. Mit dem neuen Hochtemperatursensor auf Platinbasis steht der Automobilindustrie ein schneller, genauer und kostenguenstiger Abgassensor zur Verfuegung, der alle Anforderungen an die elektrische und mechanische Stabilitaet erfuellt. (orig.)

410

Operating experiences gained with the ALSTOM NID process in the example case of AWG Wuppertal; Betriebserfahrungen mit dem ALSTOM NID-Verfahren am Beispiel der AWG Wuppertal  

Acting on behalf of the EKOCity waste disposal group the Abfallwirtschaftsgesellschaft mbH Wuppertal (AWG = Wuppertal waste management company) disposes of the municipal waste in the cities Wuppertal, Remscheid and Bochum as well as in the Ennepe-Ruhr and large parts of the Mettmann district and of industrial wastes in the Bergian region. The AWG has also operated the Wuppertal waste incineration plant since 1976. ALSOM Power Service GmbH was commissioned to replace two existing wet flue gas purification lines with two conditioned dry sorption lines. The exhaust gases are purified in accordance with the limit values of the 17th Federal Emission Control Ordinance using the ALSTOM NID (new integrated desulphurisation) process. The two exhaust gas purification lines have a cleaning capacity of up to 120,000 Nm{sup 3} each. The specific advantages of the NID process are its high separation efficiency, low consumption of sorbent material, low equipment requirement, extremely low space requirement and low maintenance requirement. Another asset is the use of caustic lime in place of lime hydrate as absorbent. The paper gives a short description of the ALSTOM NID process and its above-named advantages. It also reports in detail on experiences gained with commissionings and retrofittings. Process engineering aspects are discussed on the basis of current operating values. The paper also discusses the influences of the temperature, humidity, chloride levels and other parameters of the recirculated material on conditioned dry sorption processes involving residue recirculation.

411

Investigation on the Dioxin Emission from a Commercial Sintering Plant  

Recent studies concerning the dioxin emission from the iron ore sintering process have clarified a dominant mechanism of dioxin formation and the substances to promote or to inhibit the reaction. In this paper, a detailed analysis of the exhaust gas at the Oita No. 1 sintering plant has specified the strand positions where dioxins were released into the exhaust gas. The release of dioxins was detected at two different positions. The first release position was located at the point where the drying zone reached the hearth layer, showing a broad peak containing a large amount of furans. The second release position was located at the point where the melting zone reached the heath layer, showing a sharp peak. Differences in dioxin congeners at the release positions imply a different mechanism of dioxin formation. The dioxins of the second release are considered to be formed in wind boxes at temperatures of 300°C or more. Controlling the burn through point to the discharge end is supposed to be effective for decreasing the dioxin emission in the second step.   

412

Variable area nozzles for turbomachines  

Jet propulsion powerplant comprising a gas producer 11 having a first flow duct 12 for receiving the output of the gas producer 11. The flow duct 12 includes a nozzle 13 having a center body 16 which has an upstream part 17 and a downstream part 20. Motors 22 are provided for expanding and contracting the downstream part 20 relative to the upstream part 17. A second flow duct 33 having an inlet 30 openable to airflow and connected to the interior of said upstream part 17 is provided. An outlet 24 from the interior of the upstream part 17, is provided at the downstream end of the upstream part 17. The outlet 24 opens into the interior of the first flow duct 12 by contracting the downstream part 20 relative to the upstream part 17. By such an arrangement, infrared radiation may be suppressed when necessary by opening the inlet for air flow and controlling the upstream and downstream parts so that there can be a mixing of air with exhaust gases which reduces the mean temperature of the exhaust gases.

413

The cryogenic diffusion pump and its implementation in a complete fusion reactor forevacuum system  

A cryogenic diffusion pump has been developed and tested. It uses the main constituent of the fusion reactor exhaust gas, i.e., deuterium--tritium (D--T), as a working fluid in a diffusion pump operating at low temperature, to separate and compress the minor constituent {sup 4}He. Since a suitable tritium-handling facility was not available, a prototype was tested using mixtures of deuterium with 1%, 2%, and 4% helium. As the deuterium is pumped by cryocondensation at 4 K, the entrained helium is staying in the gas phase, is compressed, and leaves the pump outlet at pressures up to 80% of the total inlet pressure. Compression ratios of up to 80 (for 1% helium) and inlet pumping speeds ranging from 1 to 2 m{sup 3} s{sup {minus}1} have been measured for operating pressures between 3 and 10 Pa. Deuterium carry-over into the helium exhaust was below the detection limit of the equipment. A design is presented incorporating the cryogenic diffusion pump in a complete fusion reactor forevacuum system, including the separation of impurities from hydrogen isotope mixtures.

414

Advantages of Low Air-Ratio Combustion in a Stoker-Type Incinerator  

Low air-ratio combustion has become the major subject with enormous attention as a measure to reduce the amount of substances with environment impact from the waste incineration process, and to make the most effective use of energy. However, it has been thought that there would be considerable difficulty in utilizing low air-ratio combustion on the classic grate furnace due to fundamental problems in its process, which treats the wide range and heterogeneity of waste materials. The application of high temperature air combustion technology for enhancing sound combustibility provided solutions to these problems. In practice, a mixture of high-temperature air and flue gas is injected at high velocity from both sides of the furnace walls to form a stable high-temperature zone in the combustion initiation region above the waste. This prevents fluctuations or localized extinguishing of the flame, while heating the waste directly with the flame to promote gasification at the same time. A practical study was conducted at a 105-ton/day municipal solid waste stoker type incineration plant. The test demonstrated that stable low excess-air combustion operation is possible at a combustion air stoichiometry of 1.3 with EGR (Exhaust Gas Recirculation) and high temperature air combustion technology resulting in a 17% decrease in flue gas flow, an energy efficiency improvement of 10%, and more than 50% reduction in NOx emissions when compared with an air stoichiometry of 1.6.   

415

Problems and measures for the calorie reduction in coke oven carbonization  

For the promotion of carbonization calorie reduction, it is necessary to maintain the coke quality and to prevent the damage of the oven body. Quality degradation was maintained by the longer stay time, and the oven body degradation by time was prevented and reduced by restricting the calorie of carbonization. However, due to the high yen economic situation and the reduction of iron output, the plant operation rate has come down below 110% (rated minimum operation) since Oct., 1986 and even down to the present 95%. The plant management reviewed the operation management standard (oven temperature, limit of staying time, etc), and, for further reduction of carbonization calorie, investigated to develop new technologies (ACC, coal humidity control, etc). These are a uniform oven heating (ACC), reduction of temperature fluctuation, installment of coal pre-treatment unit, reduction of O/sub 2/ fluctuation of the exhaust gas, reinforcement of the oven body insulation, and reduction of water content, etc.. (9 figs, 3 tabs)

416

Transient Scuffing of Candidate Diesel Engine Materials at Temperatures up to 600oC  

This milestone report summarizes the general characteristics of scuffing damage to solid surfaces, then describes transient effects on scuffing observed during oscillating sliding wear tests of candidate material pairs for high-temperature diesel engine applications, like waste-gate bushings in exhaust gas recirculation (EGR) systems. It is shown that oxidation and the formation of wear particle layers influence the friction of such components. In the case of metallic materials in cylindrical contacts where there is a generous clearance, debris layers can form which reduce the torque over time. For ceramic combinations, the opposite effect is observed. Here, the accumulation of wear debris leads to an increase in the turning torque. High-temperature transient scuffing behavior is considered in terms of a series of stages in which the composition and morphology of the contact is changing. These changes are used to explain the behavior of 11 material pairs consisting of stainless steels, Ni-based alloys, Co-based alloys, and structural ceramics.

417

Experimental study of the mild combustion of liquid hydrocarbons  

A strong exhaust gas recirculation combined with air preheating generates relatively low maximum flame temperatures allowing for a better control of the furnace temperature and a lower pollutant production. While the sustainability of this combustion technology (named mild or flameless combustion) for different gaseous fuels has been extensively studied, much less information are available for liquid fuels. Consequently, this work has focused on the investigation of the sustainability of mild combustion for liquid hydrocarbons using a dual-nozzle laboratory-scale burner. Pure liquid n-octane has been used as a reference fuel, while mixtures involving also other hydrocarbons commonly found in practical fuels have been investigated to start collecting information on surrogate fuels. It has b...

418

Using Air Cycle Refrigerator Integrated with Desiccant System for Simultaneous Air Conditioning and Domestic Hot Water Heating  

The performance of a system for simultaneous air conditioning and domestic hot water heating is estimated numerically in this study. The system consists of air cycle refrigerator, desiccant rotor, evaporative cooler and heat recovery heat exchanger. The system uses air and water which are natural and safe substances. The system can supply air at low temperature and humidity. Also, it is easy to control the humidity of supply air by using evaporative cooling process before supplying air to the conditioning area. A recovery of exhausted heat from the desiccant rotor significantly decreasing not only the consumption of primary energy for heating domestic hot water but also the calefaction to the surroundings due to the rejection of heat. The system can supply hot water at a significant high temperature. The proposed system coefficient of performance is greater than the coefficient of performance of conventional system composed from vapor compression cycle and gas heater.   

419

Hydrocarbon emissions from apartment building incinerators  

The performance of apartment building incinerators was studied at eleven incinerator sites in Toronto. The study focused on hydrocarbon emissions and combustion characterization. The chosen sites had a record of smoke and odour complaints. The measurements were performed with a mobile testing laboratory and included continuous monitoring of exhaust gas temperature, oxygen, carbon dioxide, carbon monoxide, and total hydrocarbons (THC). During the stack testing the incinerators were operated by the building superintendents according to normal practices. The test runs lasted at least a half hour following ignition. During the first half hour of operation none of the units met the Ministry's THC emission limit of 100 ppm and only one did so after this period. THC concentrations from the 11 sites averaged 480 ppm as methane equivalent. Average combustion efficiency was poor (94.0%) as a result of high excess air and low temperatures. Multichamber incinerators performed slightly better than flue fed units. 52 figs., 32 tabs.

420

A study of recovery of copper and cobalt from copper-cobalt oxide ores by ammonium salt roasting  

Copper and cobalt recovery from a copper-cobalt ore of Democratic Republic of Congo (DRC) by ammonium chloride roasting is studied. The effects of roasting temperature, roasting time, and the dosage of ammonium chloride on the leaching rate of copper and cobalt are investigated. The results show 90% copper and 95% cobalt recovery under the optimal experimental conditions of average particle diameter 0.10mm and 1:2 ammonium chloride to ore mass ratio at a roasting temperature of 300^oC for 3h. After adjusting the pH of the leaching solution to 7 by ammonia addition, the copper and cobalt in the solution were precipitated by ammonium bicarbonate at 60^oC for 40min. Ammonium chloride crystals obtained after absorbing the exhaust gas and filtration of the scrub liquor could be reused for the r...

 
 
 
 
421

Competitive no, co and hydrocarbon oxidation reactions over a diesel oxidation catalyst  

Abstract The oxidation of NO, CO and hydrocarbons (HC) individually, in mixtures, and with NO2 were investigated over a monolith-supported Pt/Al2O3 catalyst under oxidising conditions. Although competitive adsorption and inhibition by other species on oxidation reactions is a relatively well-known phenomenon, this study represents a more comprehensive examination of such effects between key components in vehicle exhaust gases. NO2 was completely reduced by CO and C3H6, under NO2 limited conditions, at temperatures as low as 110C and at temperatures above 140C with dodecane and m-xylene. NO2 was then again observed once the extent of oxidation of the other species by oxygen was significant. Under the conditions tested, NO, CO and HC oxidation was inhibited by NO2 in the feed gas mixture. HC...

422

Heat storage type combustion equipment. Deodorizing equipment for waste gas; Chikunetsushiki nensho sochi. Hai gas no dasshu sochi  

A heat storage type combustion deodorizing equipment was developed by means of a three tower system, as measures for deodorizing organic solvent compound (VOC) contained in industrial waste gas and the like. A ceramic-made heat accumulator was employed instead of the conventional exhaust gas preheat exchanger. In the first stage, a waste gas ascending in a heat storage chamber 1 was preheated, oxidized and dissolved in a high temperature combustion chamber; then, descending in a heat storage chamber 2 as a clean gas, and imparting heat to the heat accumulator, the gas was discharged. During that time, a remaining unprocessed gas was purged upward by the clean gas in a heat storage chamber 3, oxidized and dissolved in the combustion chamber; then, similarly, passing through the heat storage chamber 2, the gas was discharged. In the following second stage, a valve was switched, turning the heat storage chamber 1 to a purging chamber, the chamber 2 to the entrance side for the gas to be treated, and the chamber 3 to the exit side for the clean gas. Furthermore, after a specific time elapsed, the sequence was repeated going back to the first stage through the third. Total hydro carbon removal ratio was approximately 99% regardless of the concentration on the entrance side. Odor concentration was 13,000 on the entrance side and 420 on the exit side. The equipment being a heat storage type, the heat efficiency was 85 to 95% showing less energy consumption compared with a conventional direct burning type or a catalytic type equipment. 4 refs., 9 figs., 1 tab.

423

An experimental study of jet exhaust simulation  

Afterbody drag predictions for jet aircraft are usually made experimentally with the jet exhaust flow simulated. The physical gas properties of the fluid used for the model jet exhaust can affect the accuracy of simulation of the airplane's jet exhaust plume. The effect of the accuracy of this simulation on afterbody drag was investigated by wind-tunnel tests with single engine model. In addition to unheated air as the