Thematische Bibliographien / Waste heat recovery boiler

Inhaltsverzeichnis

  1. Zeitschriftenartikel
  2. Dissertationen
  3. Bücher
  4. Buchteile
  5. Konferenzberichte
  6. Berichte der Organisationen

Auswahl der wissenschaftlichen Literatur zum Thema „Waste heat recovery boiler“

Autor: Grafiati
Veröffentlicht am 28. Juni 2021
Zuletzt aktualisiert am 14. Februar 2022

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Zeitschriftenartikel zum Thema "Waste heat recovery boiler"

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Yanai, Eiji, und Tetsuzo Kuribayashi. „Waste heat recovery boiler“. Atmospheric Environment (1967) 22, Nr. 2 (Januar 1988): ii. http://dx.doi.org/10.1016/0004-6981(88)90065-0.

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Hoizumi, Shinichi, und Tsugutom Teranishi. „5109665 Waste heat recovery boiler system“. Environment International 19, Nr. 1 (Januar 1993): II. http://dx.doi.org/10.1016/0160-4120(93)90032-d.

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3

White, Martin. „4448136 Boiler with waste heat recovery“. Journal of Heat Recovery Systems 5, Nr. 2 (Januar 1985): iv. http://dx.doi.org/10.1016/0198-7593(85)90057-8.

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4

Manickam, M., M. P. Schwarz und J. Perry. „CFD modelling of waste heat recovery boiler“. Applied Mathematical Modelling 22, Nr. 10 (Oktober 1998): 823–40. http://dx.doi.org/10.1016/s0307-904x(98)10020-3.

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5

Baradey, Y., M. N. A. Hawlader, Ahmad Faris Ismail und Meftah Hrairi. „WASTE HEAT RECOVERY IN HEAT PUMP SYSTEMS: SOLUTION TO REDUCE GLOBAL WARMING“. IIUM Engineering Journal 16, Nr. 2 (30.11.2015): 31–42. http://dx.doi.org/10.31436/iiumej.v16i2.602.

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Energy conversion technologies, where waste heat recovery systems are included, have received significant attention in recent years due to reasons that include depletion of fossil fuel, increasing oil prices, changes in climatic conditions, and global warming. For low temperature applications, there are many sources of thermal waste heat, and several recovery systems and potential useful applications have been proposed by researchers [1-4]. In addition, many types of equipment are used to recover waste thermal energy from different systems at low, medium, and high temperature applications, such as heat exchangers, waste heat recovery boiler, thermo-electric generators, and recuperators. In this paper, the focus is on waste heat recovery from air conditioners, and an efficient application of these energy resources. Integration of solar energy with heat pump technologies and major factors that affect the feasibility of heat recovery systems have been studied and reviewed as well. KEYWORDS: waste heat recovery; heat pump.
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Seyedan, B., P. L. Dhar, R. R. Gaur und G. S. Bindra. „Optimization of Waste Heat Recovery Boiler of a Combined Cycle Power Plant“. Journal of Engineering for Gas Turbines and Power 118, Nr. 3 (01.07.1996): 561–64. http://dx.doi.org/10.1115/1.2816684.

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In the present work a procedure for optimum design of waste heat recovery boiler of a combined cycle power plant has been developed. This method enables the optimization of waste heat recovery boiler independent of the rest of the system and the design thus obtained can directly be employed in an existing plant.
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Bichevin, Vladislav, und Nina Sosnovskaya. „PROTECTION AGAINST CORROSION OF THE TECHNOLOGICAL EQUIPMENT OF THE OIL REFINING ENTERPRISE“. Modern Technologies and Scientific and Technological Progress 2020, Nr. 1 (16.06.2020): 23–24. http://dx.doi.org/10.36629/2686-9896-2020-1-23-24.

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A method for slowing down the corrosion of heat exchangers in the T-104 and T102 heat recovery boiler blocks is considered. PK-1 Aminate was selected as the most suitable inhibitor for process heat exchangers of the waste heat recovery boiler unit
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Xiao, Zhong Zheng, Shu Zhong Wang und Jian Ping Yang. „Research on Recovering Waste Heat from Liquid Produced in Heavy Oil Exploitation by SAGD Technology“. Advanced Materials Research 960-961 (Juni 2014): 410–13. http://dx.doi.org/10.4028/www.scientific.net/amr.960-961.410.

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In order to enhance the economy of steam assisted gravity drainage (SAGD) technology, researches were conducted on the technology for recovering heat from liquid produced from oil wells. In this study, spiral-plate heat exchanger has been chosen after comparison and analysis, which is used to recover the heat from the produced liquid and raise the temperature of the softened water used in steam injection boilers. The procedures are liquid produced from the wellhead enters a metering and transfer station for degasification and then enters a centralized heat exchanger station where its temperature is reduced to 100°C from 170°C and the temperature of softened water used as boiler feed water is increased to 110°C from 70°C. The result shows that the fuel gas consumption will drop by 907200Nm3 for each boiler annually when the liquid heat recovery technology is adopted.
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Zhou, Y., Z. Liu und A. Golyanin. „Simulation of Waste Heat Recovery From Ship Boiler Exhaust Gas“. Bulletin of Science and Practice 6, Nr. 4 (15.04.2020): 232–42. http://dx.doi.org/10.33619/2414-2948/53/27.

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The heat pipe type waste heat recovery system can effectively reduce energy consumption when the ship is sailing in a polar region, so it has great engineering application value. In order to improve the design of the heat pipe waste heat recovery system and ensure that the design parameters meet the design requirements, this project has carried out a three-dimensional simulation analysis of the internal flow field of the heat pipe waste heat recovery system. Through reasonable model processing, application of boundary conditions, and the assignment of physical attributes the flow field characteristics of the key positions of the heat pipe type waste heat recovery system were obtained scientifically and effectively. The model was simulated and calculated, and the flue gas temperature distribution in the evaporator heat exchange tube, the overall temperature distribution of the waste heat recovery system, and the temperature change curve from the cold water entering the condenser to the steady state were obtained. The change curve of the thermal efficiency of the system during the temperature of the flue gas from the evaporator to the steady state.
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Joshi, Pratik M., Shekhar T. Shinde und Kedarnath Chaudhary. „A Case Study on Assessment Performance and Energy Efficient Recommendations for Industrial Boiler“. International Journal of Research and Review 8, Nr. 4 (06.04.2021): 61–69. http://dx.doi.org/10.52403/ijrr.20210410.

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As India is a developing country, industrialization is increasing day by day and there is a great need for industry energy audit. Audit helps to maintain and save energy from being wasted and helps in achieving highest efficiency of industrial equipment. This paper contains an actual industry audit report on boiler performance. This paper contains a report on Thermal analysis of boilers, thermal skin heat loss of boilers, O2 percentage control in flue gases to standard values, effect of coal additive, etc. This paper also contains a report on waste heat recovery options for thermal boiler, flue efficiency monitor, infrared thermometer, ultrasonic peak detector IR thermal imager. These equipment are used for energy assessment of boilers. Thermography survey of boiler surface is carried out to estimate the radiation and the other losses and the result of this total annual saving after insulation repairing or maintenance is Rs.8.48 lakh and investment is around Rs.6.31 lakh. Economizer performance of both the ISGEC and Thermax boiler can be improved with the help of suggested measures. It will help to save approximately rupees Rs.38.42 Lakh annually and investment on maintenance cost is negligible. In short, this paper deals with assessment of all boilers, evaluates their efficiencies and losses to identify energy saving opportunities and presents them in a report with their payback periods. Keywords: Energy, Energy audit, assessment, boiler.
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Dissertationen zum Thema "Waste heat recovery boiler"

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Rezaie, Navaie Ali [Verfasser], George [Akademischer Betreuer] Tsatsaronis, George [Gutachter] Tsatsaronis und Udo [Gutachter] Hellwig. „Thermal design and optimization of heat recovery steam generators and waste heat boilers / Ali Rezaie Navaie ; Gutachter: George Tsatsaronis, Udo Hellwig ; Betreuer: George Tsatsaronis“. Berlin : Technische Universität Berlin, 2017. http://d-nb.info/1156187052/34.

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Primes, Alois. „Modularní horizontální kotel – HRSG“. Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2021. http://www.nusl.cz/ntk/nusl-443235.

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This thesis deals with the design of a Heat Recovery Steam Generator (HRSG). Theintroductory part is devoted to a brief description of the boiler, the specified parametersand the compilation of the temperature profile. The main computational part of thiswork is divided into 6 parts. The first contains preparatory calculations, including thecalculation of boiler eiciency. In the second part, a flue gas duct is designed. This isfollowed by a thermal calculation of the boiler for all heat exchange surfaces. The last 3parts deal with the design of the drum, piping and the loss of boiler draft calculation.
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Dlouhá, Kristýna. „Návrh HRSG kotle“. Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2019. http://www.nusl.cz/ntk/nusl-401508.

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This master’s thesis deals with the design of a heat recovery steam generator. The introductory part of the thesis is dedicated to waste heat boilers, their division and their utilization in combined cycles gas turbine. In the following chapter, an analysis of the existing combined heat and power plant operation is performed. In the next part of the thesis, the conceptual layout of the new source is designed. Subsequently, the thermal calculation of the boiler is carried out as well as the design of individual heat exchanging surfaces. The sixth chapter deals with the strength calculation of the boiler and the outer piping, chambers and drum are designed here. At the end of the thesis there are described off-design states of the new combined cycle gas turbine.
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Rojas, Tena Fernando, und Reber Kadir. „Waste Heat Recovery Modellering“. Thesis, KTH, Förbränningsmotorteknik, 2011. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-39923.

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SammanfattningI ett tidigare projekt, utfört under våren 2010, modellerades och simulerades en ånggenerator i GT-SUITE för att analysera och jämföra dess resultat med de faktiska motormätningarna. Projektet utfördes på Kungliga Tekniska Högskolan i Stockholm, på uppdrag av företaget som introducerat idén, Ranotor. Konceptet gick ut på att ersätta EGR-kylaren i en lastbilsmotor och med hjälp av Rankine cykeln försöka öka motorns verkningsgrad. Ånggeneratorn består av 48 mikro tuber, som alla innehåller vatten med högt tryck, vattnet värms upp av de varma avgaserna som letts in i ånggeneratorn. Detta gör att vattnet förångas och leds sedan för att driva en expander för att avlasta motorn.Huvudfokus i detta examensarbete har varit att modellera, studera och analysera ånggeneratorns prestanda i simuleringsprogrammet GT-SUITE. För att kunna göra detta måste ånggeneratorn, även kallad HRSG (Heat Recovery Steam Generator), modelleras från grunden med specifikationer från tillverkaren. En elementarmodell byggdes inledningsvis upp för att belysa beteendet av flödet inuti mikro tuberna och vilka parametrar som påverkar resultatet av simuleringarna. Senare gjordes även en komplett identisk modell av den verkliga ånggeneratorn. Modellen användes i ESC-cykeln och även för transienta körningar, där all indata är samlad från motormätningar på den verkliga ånggenerator, monterad på en DS1301, 6-cylinder 12 liter Scania diesel motor. För att kunna förbättra simuleringen av den kompletta modellen, gjordes en nedskalad modell som bara innehöll två tuber. Denna modell har samma dimensioner och egenskaper med den kompletta modellen, men fördelen med denna tvåtubs modell är den förkortade simuleringstiden.Inlopps parametrar såsom, vattenflöde, ångtryck, avgasflöde och avgastemperaturen togs från verkliga motormätningar. Samtliga parametrar varierar med tiden; detta gör det möjligt att göra en direkt jämförelse mellan den verkliga ånggeneratorn och den modellerade. Ångans och avgasernas temperatur samt tryckfallet över ångpannan är huvudparametrar som har jämförts med de verkliga mätningarna. Testkörningen är baserad på ESC-cykeln, European Stationary Cycle, som innehåller tolv lastpunkter och en tomgångspunkt. Jämförelser mellan den kompletta modellen och de faktiska provkörningarna visade följande: i det bästa fallet avviker ångans temperatur ~5% motsvarande 10°C. För det sämsta fallet är temperatur skillnaden ~20%, ca 40°C, övriga lastpunkter visar en felmarginal mellan 5-10% motsvarande 10-35°C. Tryckfallet över ångpannan visar en större felmarginal, vilket beror på mätningar under testkörningar där vissa filter var igen satta, därav uppmättes tryckfallet i vissa fall upp till 20 bar. I bästa fallet skiljer det ~1 % mellan simulering och verklighet, vilket är nästan identiskt, medan det i det sämsta falletskiljer uppemot 70 % som motsvarar 10 bar, övriga lastpunkter ligger i intervallet 10-15 % felmarginal, motsvarande 1-4 bar.Två tubs modellen beter sig som den kompletta modellen; avvikelsen mellan dessa modeller är 1-5% ~5-15°C i de flesta fallen, där skillnaden för det mesta liknar mätningarna. Värmeöverföringen, Reynolds tal, ångans effekt studeras i tvåtubs modellen. Analys av modellen visar att ~40-55 % av värmeöverföringen sker i fasomvandlingen, vilket var förvånande mycket och Reynolds tal ökar med ~450 % i denna region, från 1500 till ~6500, vilket tyder på en flödesövergångs fas. Ångans effekt varierar mellan 5-23 kW beroende på lastpunkt.Den slutliga modellen ger tillfredställande resultat och anses vara tillräckligt bra för vidare analys.
AbstractIn a previous project, made in the spring of 2010, a steam generator was modelled and simulated in GT-SUITE, in order to analyze and compare with engine measurements. This was made at the Royal Institute of Technology in Stockholm, on behalf of the company that introduced this idea, Ranotor. The concept was to replace the EGR-cooler in a heavy duty engine and with help of the Rankine cycle, try to improve its efficiency. The steam generator consists of 48 micro tubes, all containing high pressured water, which in turn is heated by the warm exhausts that are led into the steam generator. This causes the water in the tubes to evaporate which propels an expander that will unload the engine.The main focus of this thesis is to model, study and analyze the performance of the steam generator built in the simulation program GT-SUITE. The steam generator, called Heat Recovery Steam Generator (HRSG), is modelled from scratch with the specifications of the manufacturer. An elementary model was initially made to highlight the behaviour of the flow inside the micro tubes and what parameters affect the outcome of the simulations. Finally a complete identical model was made of the actual steam generator. The model was used in an ESC-cycle and also for a transient cycle, where all the input data is gathered on engine measurements of the actual HRSG, mounted on a DS1301, 6-cylinder 12 litre Scania diesel engine. In order to improve the simulation of the complete model a downsized model, only containing two tubes, was made. This model has the same dimensions and properties as the complete model but the advantage of this double-tube model is the shortened simulation time.The inlet parameters to the model such as water mass flow, steam pressure, exhaust mass flow and exhaust temperature were taken from actual engine measurements. All the parameters vary due to time; this makes a comparison possible between the real steam generator and the modelled one. Steam temperature, exhaust temperature and pressure drop along the HRSG are the main parameters from the simulations that are compared to the actual measurements. The engine measurements are made based on the ESC-cycle, European Stationary Cycle, which contains twelve load points and one idle point. During comparison between the complete model and the engine measurements following is observed, in the best case the steam temperature differs ~ 5 %, equalling 10°C. In the worst case the temperature difference is ~20 %, which is approximately 40°C, the rest of the load points shows a margin of error between 5-10 % equalling 10-35 °C. Pressure drop along the HRSG is less accurate;this is due to an error during the measurement where some filters where clogged. Disparity in pressure drop is ~1% in best case, which is almost identical and ~70% in worst case, corresponding to approximately 10 bar, where rest of the load points shows a margin of error between 10-15% equalling 1-4 bar.The double-tube model behaves like the complete model; the difference between the models is 1-5 % in most cases ~5-15°C, where the difference is mostly closer to the measurements. Heat transfer, Reynolds number and steam power are taken and studied from the double tube model. Analyses of the models reviles that ~40-55 % of the heat transfer is in the transition phase, which is surprisingly much and Reynolds number increases by ~450% in the same region, from 1500 to ~6500 which indicates a flow transition phase. Steam power varies between 5-23 kW depending on load point.The final model shows satisfying result and therefore assumed to be good enough for further analyse.
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Razavinia, Nasimalsadat. „Waste heat recovery with heat pipe technology“. Thesis, McGill University, 2010. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=94983.

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High grade energy, which is primarily derived from hydrocarbon fuels, is in short supply; therefore alternative energy sources such as renewable and recycled energy sources are gaining significant attention. Pyro-metallurgical processes are large consumers of energy. They in return generate large quantities of waste heat which goes un-recovered. The overall theme of this research is to capture, concentrate and convert some of this waste heat to a valuable form. The main objective is to characterize and develop heat pipe technology (some of which originated at McGill) to capture and concentrate low grade heat. Heat pipe employs boiling as the means to concentrate the energy contained in the waste heat and transfers it as higher quality energy. The distinct design features of this device (separate return line and flow modifiers in the evaporator) maximize its heat extraction capacity. During the testing the main limitations within the heat pipe were identified. Different test phases were designed throughout which the configuration of the system was modified to overcome these limitations and to increase the amount of extracted heat.
L'énergie d'haut grade de nos jours est produite principalement à base de combustion d'hydrocarbure et les réserves de cette énergie deviennent de plus en plus rare, mais certaines énergies alternatives connues gagnent des forces parmi les marchés incluant les sources d'énergie renouvelables et recyclées. Les usines pyrométallurgiques sont des consommateurs significatifs d'énergie d'haut grade. Ces procédés industriels relâches un montant important de chaleurs (perte) à l'environnement sans aucune récupération. Le but du projet est de concentrer, capturer et convertir cette chaleur résiduelle de basse qualité en énergie valable. Par contre, l'objectif principal du projet comme tel est de développer et de perfectionner un caloduc capable d'extraire cette chaleur parvenant des gaz effluents. Le point d'ébullition d'une substance (vapeur) est utilisé comme moyen de concentrer l'énergie contenu dans les effluents avec la technologie des caloducs. Pour maximiser les gains énergétiques, la conception de ce caloduc en particulier utilise des canaux de retour indépendant ainsi qu'un modificateur de débit dans l'évaporateur, lui permettant d'extraire un niveau supérieur de chaleur. Pendant les essais lors du projet, les éléments limitants des systèmes de caloducs ont été identifiés. Les configurations du système ont été ajustées et modifiés dans la phase expérimentale d'essai pour surmonter ces limitations et maximiser l'extraction de chaleur.
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Hua, Lihong. „Heat exchanger development for waste water heat recovery“. Thesis, University of Canterbury. Mechanical Engineering, 2005. http://hdl.handle.net/10092/6459.

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Hot water plays an import role in modem life. The consumption of hot water represents a significant part of the nation's energy consumption. One way of reducing the energy consumption involved, and hence the cost of that energy, is to reclaim heat from the waste warm water that is discharged to the sewer each day. The potential for economic waste water heat recovery depends on both the quantity available and whether the quality fits the requirement of the heating load. To recover heat from waste water in residential and commercial buildings is hard to achieve in quality because of its low temperature range. Nevertheless, efforts to recycle this waste energy could result in significant energy savings. The objective of this research was to develop a multiple panel thermosyphon heat exchanger for a waste water heat recovery system. The advantage of the system proposed in this work is that it not only provides useful energy transfer during simultaneous flow of cold supply and warm drain water but also has the ability to store recovered energy at the bottom of a hot water storage tank for later use. While this concept is not new, the design of the heat exchanger proposed for the present study is significantly different from those used previously. Component experiments were carried out to determine the performance characteristics of a single thermosyphon panel. By changing the inclination angle of the single panel heat exchanger and varying its working condition, it was found that the inclination angle of 10° could be identified as the minimum inclination angle at which good performance was still obtained. The close values of the overall heat transfer coefficients between top surface of the panel insulated and both top and bottom surfaces of the panel uninsulated shows that the overall heat transfer coefficient of the single panel was dominated by the bottom surface of the panel. Even if in a worst case the top surface of the panel might be possibly covered by the deposits from the waste water, it would not affect much on the heat transfer performance of the panel. Measurements of hot water usage and waste water temperature and flow rates were obtained for a potential application of the proposed exchanger (the dishwasher for the kitchen in the University Halls of Residence). A model of a multi-panel thermosyphon heat exchanger was also developed to predict the energy savings that would be expected if such a heat exchanger was used in this situation. The result indicated that an overall electricity of 7500 kWh could be saved annually from the dishwasher system by employing a four-panel thermosyphon heat exchanger.
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Aguilar, Alex. „Harnessing thermoacoustics for waste heat recovery“. Thesis, Massachusetts Institute of Technology, 2020. https://hdl.handle.net/1721.1/130213.

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Thesis: S.B., Massachusetts Institute of Technology, Department of Mechanical Engineering, September, 2020
Cataloged from student-submitted PDF of thesis.
Includes bibliographical references (pages 25-26).
Environmental concerns and economic incentives have created a push for a reduction in emissions and an increase in efficiency. The U.S. Department of Energy estimates that 20 to 50% of the energy consumed in manufacturing processes is lost in some form to waste heat. The purpose of this study is to review the waste heat recovery technologies currently available in both commercial and research applications to determine how thermoacoustics may serve a role in furthering the use of waste heat recovery units. A literary review of the most common waste heat recovery units was compiled to determine the advantages and disadvantages of the different technologies by comparing components and their governing processes. An existing model of a thermoacoustic converter (TAC) was reviewed and a conceptual analysis written to suggest improvements for future experimental designs.
by Alex Aguilar.
S.B.
S.B. Massachusetts Institute of Technology, Department of Mechanical Engineering
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Lemaire, Lacey-Lynne. „Miniaturized stirling engines for waste heat recovery“. Thesis, McGill University, 2012. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=107690.

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Portable electronic devices have made a profound impact on our society and economy due to their widespread use for computation, communications, and entertainment. The performance and autonomy of these devices can be greatly improved if their operation can be powered using energy that is harvested from the ambient environment. As a step towards that goal, this thesis explored the feasibility of developing miniaturized Stirling engines for harvesting waste heat. A mesoscale (palmtop-size) gamma-type Stirling engine, with a total volume of about 165 cubic centimeters, was manufactured using conventional machining techniques. The engine was able to sustain steady-state operation at relatively low temperature differentials (between 20 degrees Celsius and 100 degrees Celsius) and generated a few millijoules of mechanical energy at frequencies ranging from 200 to 500 revolutions per minute. Subsequently, the gamma-type engine was transformed into a Ringbom engine; and its operation was compared with the predictions of an analytical model available in the literature. The experience gained from these studies provides some guidelines for further miniaturization of Stirling engines using microfabrication technologies.
Les appareils électroniques portatifs ont définitivement laissé un impact sur notre société et économie par leur utilisation fréquente pour le calcul, les communications et le divertissement. La performance et l'autonomie de ces appareils peuvent s'améliorer grandement si leur exploitation fonctionne en utilisant l'énergie récoltée de l'environnement. Pour s'orienter vers ce but, cette thèse a exploré si le développement d'un moteur Stirling fonctionnant sur l'énergie résiduelle était faisable. Un moteur Stirling de configuration 'gamma', de la grandeur d'une paume de main, avec un volume d'environ 165 centimètres cubes, a été fabriqué en utilisant des techniques conventionnelles d'usinage. Ce moteur a été capable de soutenir l'opération constante et stable à des différences en température relativement basses (entre 20 degrés Celsius et 100 degrés Celsius). De plus, il a produit quelques milli-Joules d'énergie mécanique à des fréquences entre 200 et 500 révolutions par minute. Par la suite, le moteur Stirling de configuration 'gamma' a été transformé en un moteur Ringbom. Par après, l'opération de ce moteur a été comparée à des prédictions basées sur un modèle analytique disponible dans la littérature. Les informations recueillies durant cette étude ont fourni certaines directives pour la miniaturisation éventuelle d'un moteur Stirling en utilisant des techniques de microfabrication.
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Gibbons, Jonathan S. (Jonathan Scott) 1979, und Stephen V. 1982 Samouhos. „Mobile power plants : waste body heat recovery“. Thesis, Massachusetts Institute of Technology, 2004. http://hdl.handle.net/1721.1/32814.

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Thesis (S.B.)--Massachusetts Institute of Technology, Dept. of Mechanical Engineering, 2004.
Includes bibliographical references.
Novel methods to convert waste metabolic heat into useful and useable amounts of electricity were studied. Thermoelectric, magneto hydrodynamic, and piezo-electric energy conversions at the desired scope were evaluated to understand their role and utility in the efficient conversion of waste body heat. The piezo-electric generator holds the most promise for the efficient conversion of waste body heat into electricity. In the future, this same device could be easily extended into a combustion based power plant. An experimental apparatus investigating the use of magneto hydrodynamics was designed, built, and tested. A room temperature liquid inetal was propelled through a magneto hydrodynamic channel of 4 inches by 0.1875 inches at a rate of 10 mL/s. A 2 T induction field was applied within the channel. However, the results of the analysis did not find the magneto hydrodynamic device to be an effective electric generator at the scale tested.
by Jonathan S. Gibbons and Stephen V. Samouhos.
S.B.
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Sapa, Ihor. „Waste heat recovery in the ceramic industry“. Master's thesis, Universidade de Aveiro, 2013. http://hdl.handle.net/10773/11827.

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Mestrado em Sistemas Energéticos Sustentáveis
Este trabalho tem como objetivo principal constituir um contributo para a sistematização e análise das diferentes opções disponíveis para a recuperação de calor residual na indústria cerâmica, através do desenvolvimento e aplicação de uma metodologia para a incorporação eficiente de tecnologias de recuperação de calor residual. Com base na revisão da literatura, a metodologia proposta fornece bases para a identificação e caracterização das fontes de calor residual presentes na indústria cerâmica, bem como apresenta a revisão e análise de aplicabilidade das tecnologias de recuperação de calor mais comuns e inerentes a este sector. A demonstração e aplicação da metodologia proposta foi desenvolvida no âmbito de um estágio extracurricular numa unidade fabril portuguesa do setor cerâmico - TopCer - integrado no programa Galp 202020@UA. O estudo de caso desenvolvido revelou a importância da recuperação de calor como uma das ferramentas para a melhoria da eficiência energética no sector cerâmico no sentido de obter uma vantagem competitiva. A revisão bibliográfica sobre recuperação de calor demonstrou que esta área do conhecimento tem apresentado um crescimento significativo em termos de número de publicações quase duplicando em número de 2011 para 2012, o que ilustra o crescente interesse da comunidades científica e tecnológica por este tema. A metodologia proposta tendo o setor da indústria cerâmica como ponto de partida, é suficientemente robusta para poder ser facilmente adaptada a outras indústrias que procuram soluções de poupança de energia através da valorização de calor residual.
This work aims to be a contribution to the systematization and analysis of the different options available for waste heat recovery in the ceramic industry, through the development and application of a methodology for incorporating efficient technologies in waste heat recovery in the industrial process. Based on a review of the literature, the proposed methodology provides the bases for the identification and characterization of waste heat sources in the ceramics industry, and presents a review and analysis of the applicability of the available technologies for heat recovery, most common and inherent in this sector. The demonstration and application of the proposed methodology was developed at a Portuguese ceramic manufacturing unit – TopCer – as part of an extracurricular internship under Galp 202020@UA program. The undertaken case study revealed the importance of heat recovery as a tool for improving energy efficiency in the ceramic sector in order to gain competitive advantage. The literature review on the waste heat recovery has demonstrated that this area has suffered a significant increase in terms of number of publications in 2012, illustrating the growing interest of scientific communities and practitioners in the heat recovery problems. The elaborated methodology for waste heat recovery incorporation is a rather robust instrument and, therefore, it can be easily tailored to other industries looking for energy saving solutions though consideration of waste heat recovery options.
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Bücher zum Thema "Waste heat recovery boiler"

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Dixon, J. Design of waste heat boilers for the recovery of energy from arc furnace waste gases. Luxembourg: Commission of the European Communities, 1985.

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V, Ganapathy. Waste heat boiler deskbook. Lilburn, GA: Fairmont Press, 1991.

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3

Goldstick, Robert. Principles of waste heat recovery. Atlanta, Ga: Fairmont Press, 1986.

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4

Albert, Thumann, Hrsg. Principles of waste heat recovery. Hemel Hempstead: Prentice-Hall, 1986.

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5

Meeting, American Society of Mechanical Engineers Winter. Heat transfer in waste heat recovery and heat rejection systems. New York (345 E. 47th St., New York 10017): ASME, 1986.

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6

Adams, Terry N. Kraft recovery boiler physical and chemical processes. New York, NY: American Paper Institute, 1988.

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7

Cole, William E. Fluidized-bed waste-heat recovery system development. Waltham, Mass: Thermo Electron Corp., 1987.

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Woodward, John B. Engine waste heat thermodynamics. Ann Arbor, MI: Sarah Jennings Press, 1985.

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9

International Recovery Boiler Conference (2004 Porvoo, Finland). 40 years recovery boiler co-operation in Finland: Proceedings, International Recovery Boiler Conference, Haikko Manor, Porvoo, May 12-14, 2004. Helsinki, Finland: The Committee, 2004.

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Gettings, Mike. Heat recovery from high temperature waste gas streams. [London]: Energy Efficiency Office, 1987.

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Buchteile zum Thema "Waste heat recovery boiler"

1

Sengupta, Prasunjit. „Refractories for Boiler and Waste Heat Recovery“. In Refractories for the Chemical Industries, 303–16. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-61240-5_12.

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2

Zhao, Hua, Pengfei Dai, Shanshan Cao und Qing Hao. „Waste Heat Recovery System Using Coal-Fired Boiler Flue Gas to Heat Heating Network Return Water“. In Lecture Notes in Electrical Engineering, 567–75. Berlin, Heidelberg: Springer Berlin Heidelberg, 2013. http://dx.doi.org/10.1007/978-3-642-39581-9_56.

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Mehta, D. Paul. „Waste Heat Recovery“. In Energy Management Handbook, 209–32. Ninth edition. | Louisville, Kentucky : Fairmont Press, Inc., [2018]: River Publishers, 2020. http://dx.doi.org/10.1201/9781003151364-8.

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Kaya, Durmuş, Fatma Çanka Kılıç und Hasan Hüseyin Öztürk. „Waste Heat Recovery“. In Energy Management and Energy Efficiency in Industry, 463–78. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-25995-2_17.

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Sengupta, Piyali, S. K. Dutta und B. K. Choudhury. „Waste Heat Recovery Policy“. In Energy, Environment, and Sustainability, 185–205. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-7509-4_11.

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Yang, Wen-Jei. „Recovery and Storage of Waste Heat“. In Energy Storage Systems, 525–37. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-2350-8_23.

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Ottie, Timothy W. „Other Opportunities for Waste Heat Recovery“. In 47th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 8, Issue 3/4, 181–87. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2008. http://dx.doi.org/10.1002/9780470320389.ch6.

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Yu, Miao, Maria S. Gudjonsdottir, Pall Valdimarsson und Gudrun Saevarsdottir. „Waste Heat Recovery from Aluminum Production“. In Energy Technology 2018, 165–78. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-72362-4_14.

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Kennel, Daniel, und Melanie Raimer. „Waste Heat Recovery - Marktsicht zur Technologieführerschaft“. In Heavy-Duty-, On- und Off-Highway-Motoren 2015, 189–200. Wiesbaden: Springer Fachmedien Wiesbaden, 2018. http://dx.doi.org/10.1007/978-3-658-21583-5_13.

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Nakano, Jinichiro, James Bennett und Anna Nakano. „Energy Generation From Waste Slags: Beyond Heat Recovery“. In Rewas 2016: Towards Materials Resource Sustainability, 129–36. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2016. http://dx.doi.org/10.1002/9781119275039.ch19.

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Konferenzberichte zum Thema "Waste heat recovery boiler"

1

Zhou, Xian, Hua Liu, Lin Fu und Shigang Zhang. „Experimental Study of Natural Gas Combustion Flue Gas Waste Heat Recovery System Based on Direct Contact Heat Transfer and Absorption Heat Pump“. In ASME 2013 7th International Conference on Energy Sustainability collocated with the ASME 2013 Heat Transfer Summer Conference and the ASME 2013 11th International Conference on Fuel Cell Science, Engineering and Technology. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/es2013-18316.

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Condensing boiler for flue gas waste heat recovery is widely used in industries. In order to gain a portion of the sensible heat and latent heat of the vapor in the flue gas, the flue gas is cooled by return water of district heating through a condensation heat exchanger which is located at the end of flue. At low ambient air temperature, some boilers utilize the air pre-heater, which makes air be heated before entering the boiler, and also recovers part of the waste heat of flue gas. However, there are some disadvantages for these technologies. For the former one, the low temperature of the return water is required while the utilization of flue gas heat for the latter one is very limited. A new flue gas condensing heat recovery system is developed, in which direct contact heat exchanger and absorption heat pump are integrated with the gas boiler to recover condensing heat, even the temperature of the return water is so low that the latent heat of vapor in the flue gas could not be recovered directly by the general condensing technologies. Direct contact condensation occurs when vapor in the flue gas contacts and condenses on cold liquid directly. Due to the absence of a solid boundary between the phases, transport processes at the phase interface are much more efficient and quite different from condensation phenomena on a solid surface. Additionally, the surface heat exchanger tends to be more bulky and expensive. In this study, an experimental platform of the new system is built, and a variety of experimental conditions are carried out. Through the analysis of the experimental data and operational state, the total thermal efficiency of the platform will be increased 3.9%, and the system is reliable enough to be popularized.
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Zakariya, Kaneesamkandi M. „Heat Recovery From Bottom Ash in Waste Fired Boilers: Status of Technologies and Thermal Performance Modeling“. In ASME 2013 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/imece2013-62798.

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Bottom ash from Municipal Waste fired boilers have sufficient heat content and this can be used to pre-heat the boiler feed water or the combustion air. A study of the recent developments in this area is done with a focus on the air based cooling method. Modeling and simulation of the thermal performance of an air cooled ash cooling system is done with the help of Gambit/Fluent software. Among several methods of waste disposal, incineration of Municipal Waste is opted mainly due to its energy potential and specific advantages like high volume reduction ratio and convenience in plant location. However, the inherent fuel qualities that confront this method are its high moisture and ash content and the consequent low calorific values. The fuel bed temperature in stoker fired incineration systems can reach up to 1200K and a considerable part of this heat is wasted by way of ash sensible heat loss. The methods used for ash cooling include the water cooled ash screw system, the rolling cylinder ash cooler, fluidized bed ash cooler and the high strength steel belt ash cooler. In this study, the simulation of the performance of water based and air based ash cooling systems is done for a certain municipal waste fired boiler. The effect of the two methods on the overall boiler efficiency is studied. Comparison of results with that of a working system indicates that air cooling systems can be as efficient as the water cooled systems. With the help of this study, bottom ash heat recovery, especially for waste fired boilers, will be appreciated better and power plant designers will have a better insight into this area.
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Wang, Dexin, William Liss und Ainan Bao. „Water Reclamation From High Moisture Content Waste Heat Streams“. In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-63513.

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A new waste heat and water recovery technology based on a nanoporous ceramic membrane water vapor separation mechanism was developed, to extract the water vapor and its latent heat from low temperature high moisture content waste gas streams. For the water reclamation process, water vapor condenses inside the membrane pores and passes through to the permeate side which is in direct contact with a low-temperature water stream. Contaminants such as CO2, O2, NOx, and SO2 are inhibited from passing through the membrane by its high selectivity. The recovered water is of high quality and mineral free, therefore can be used as supplemental makeup water for almost all industrial processes. The membrane based technology has been first developed and demonstrated for industrial boiler flue gas heat and water recovery. Now it is being developed for wider applications, from residential humidification, commercial laundry, biomass production to utility boilers. The increased application areas will greatly enhance waste heat and water recovery potentials worldwide, to save both energy and water, and benefit the global environment. In this paper, the technology development process, and several demonstrations for different applications are discussed in details.
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Yang, Kaixuan, Ming Liu und Junjie Yan. „Thermo-Economic Analysis on Waste Heat and Water Recovery Systems of Boiler Exhaust in Coal-Fired Power Plants“. In ASME 2020 Power Conference collocated with the 2020 International Conference on Nuclear Engineering. American Society of Mechanical Engineers, 2020. http://dx.doi.org/10.1115/power2020-16269.

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Abstract Waste heat and water recovery from boiler exhaust fluegas is significant for reducing coal and water consumption of coal-fired power plants. In this study, waste heat and water recovery system No.1 (WHWR1) and No.2 (WHWR2) were proposed with a 330MW air-cooling coal-fired power plant as the reference power plant. In these systems, boiler exhaust fluegas is cooled to 95 °C in fluegas coolers before being fed to the electrostatic precipitator. Moreover, a fluegas condenser is installed after the desulfurizer to recover water from fluegas. The recovered waste heat is used to heat the condensation water of the regenerative system, boiler feeding air and the fluegas after fluegas condenser. Then, thermodynamic and economic analyses were carried out. Heat exchangers’ areas of WHWRs are affected by heat loads and heat transfer temperature differences. For the unit area cost of heat exchangers is different, the cost of WHWRs may be decreased by optimizing multiple thermodynamic parameters of WHWR. Therefore, the optimization models based on Genetic Algorithm were developed to obtain the optimal system parameters with best economic performance. Results show that the change in coal consumption rate (Δb) is ∼ 4.8 g kW−1 h−1 in WHWR2 and ∼ 2.9 g kW−1 h−1 in WHWR1. About 15.3 kg s−1 of water can be saved and recovered when the fluegas moisture content is reduced to 8.5%. The investment of WHWR2 is higher than WHWR1, while the static recovery period of WHWR2 is shorter than that of WHWR1 for the additional Δb of pre air pre-heater.
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Wang, Yufeng, Chunyun Hu, Shi'en Hui, Qinxin Zhao und Qulan Zhou. „Deposition of Cement Kiln Ash on the Tubes of Waste Heat Recovery Boiler“. In 2011 Asia-Pacific Power and Energy Engineering Conference (APPEEC). IEEE, 2011. http://dx.doi.org/10.1109/appeec.2011.5747731.

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Brandstetter, Gottfried, Wolfgang Oberleitner und Michael Pichler. „How to Change Over Heat Recovery Steam Generators After Gas Turbine Trip“. In ASME Turbo Expo 2006: Power for Land, Sea, and Air. ASMEDC, 2006. http://dx.doi.org/10.1115/gt2006-90648.

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Heat recovery steam generators downstream of gas turbines are often used in combination with process steam applications. Because of the high importance of the required process steam, a boiler trip is more severe than in usual applications, where only electricity is produced. In most cases these boilers are equipped with a supplementary and fresh air firing system having the capacity of replacing the whole waste heat coming from the gas turbine or even more. A fresh air firing system offers the possibility to keep the boiler in operation without the gas turbine running. If the boiler has to stay in operation even after a gas turbine trip a change over from waste heat firing to fresh air firing has to follow immediately. Due to the very sharp breakdown of the gas turbine speed after trip, the change over procedure has to be carried out within a few seconds to avoid a boiler shut down. The problems are — on the one hand — not to have to switch off the supplementary firing, on the other hand not to exceed the backpressure of the gas turbine because of too fast closing of dampers necessary for fresh air firing. The first would cause a necessary purging with a certain time period without firing, the second would lead to damages of the gas turbine exhaust system. Backpressure and oxygen supply have to be managed carefully to provide a smooth and save change over. In addition it has to be considered, that the first time period after gas turbine trip, the oxygen supply of the boiler’s firing has to be ensured by the running out gas turbine. Special investigations allow to predict the amount of exhaust gas mass flow after gas turbine trip by using the speed behavior of a reference gas turbine trip. At an Austrian steel mill (VOESTALPINE) these procedures were investigated in detail, and a lot of measurements were done. Based on this the existing change over procedure was optimized and the possibility of a quick change over procedure was realized.
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Strehler, Jennifer, Scott Vandenburgh, Dave Parry und Tim Rynders. „Colorado Community Benefits From Installing Waste Heat Recovery System“. In ASME 2010 4th International Conference on Energy Sustainability. ASMEDC, 2010. http://dx.doi.org/10.1115/es2010-90479.

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The Town of Avon Colorado and the Eagle River Water and Sanitation District have partnered to design, construct, and operate a mechanical “Community Heat Recovery System” which extracts low-grade waste heat from treated wastewater and delivers this heat for beneficial use. Immediate uses include heating of the community swimming pool, melting snow and ice on high pedestrian areas in an urban redevelopment zone in order to improve pedestrian safety, and space heating for project buildings and an adjacent water plant pump station building. Points of use are located within one mile of the treatment plant. The initial system is sized to extract heat from 170 m3/hr (1.08 mgd) of wastewater plant effluent with a 298 kW (400 hp) heat pump. The heat pump will deliver 1,026 kW (3,500,000 BTU/hr) energy to the heat recovery system. A supplemental natural gas boiler provided to meet peak demands will provide an additional 1,026 kW (3,500,000 BTU/hr) energy. The system is expandable allowing the installation of a second heat pump in the future and roof-mounted solar thermal panels. Power for the waste heat recovery system is provided by wind-generated electricity purchased from the local electric utility. The use of wind power with an electric-powered heat pump enables the agencies to fulfill energy needs while also reducing the carbon footprint. The system will achieve a reduction in the temperature of the treated wastewater, which is currently discharged to the Eagle River during low river flow, fish-sensitive periods. The agencies expect to save tax payers and rate payers money as a result of this project as compared to other alternatives or the status quo because it results in a more sustainable long-term operation. At 2008 utility commodities pricing, delivery of heat generated from this system was estimated to cost about one-third less than that from a conventional natural gas boiler system. This facility is the first of its kind in the U.S. and received a “New Energy Community” grant from the State of Colorado. This project shows how local agencies can work cooperatively for mutual benefit to provide infrastructure which accommodates growth and urban renewal and simultaneously demonstrate strong environmental leadership. The potential application of this technology is broad and global. The installed system is expected to cost about $5,000,000; construction will be completed in 2010.
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Sitorus, Febrin, und Totok Soehartanto. „Utilization of waste heat (off gas) from electric furnace no.4 to generate saturated steam using waste heat recovery boiler“. In ADVANCED INDUSTRIAL TECHNOLOGY IN ENGINEERING PHYSICS. Author(s), 2019. http://dx.doi.org/10.1063/1.5095314.

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Bae, Sukjung, Hyungseok Heo, Heonkyun Lee, Donghyuk Lee, Taejin Kim, Jeongsang Park und Charnjung Kim. „Performance Characteristics of a Rankine Steam Cycle and Boiler for Engine Waste Heat Recovery“. In 16th Asia Pacific Automotive Engineering Conference. 400 Commonwealth Drive, Warrendale, PA, United States: SAE International, 2011. http://dx.doi.org/10.4271/2011-28-0055.

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Janik, Carl, und Art Cole. „Boiler Rebuild and Upgraded Design for Pinellas County MSW“. In 10th Annual North American Waste-to-Energy Conference. ASMEDC, 2002. http://dx.doi.org/10.1115/nawtec10-1001.

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This paper discusses the Boiler Rebuild and Upgraded design features of the Pinellas County Solid Waste Recovery Plant located in Pinellas County, Florida. The Pinellas County Solid Waste Recovery plant consists of three 1000 Tons/Day Bulk Refuse fired boilers each designed to generate a nominal 250,000 lbs. of steam per hour (pph), at 750° F/615 psig. The boilers have been in operation since the early 1980’s and had come to the end of their reliability life. Based on the previous years of operating experience, specific areas of improvement were established. Desired improvements included; reduce tube bundle fouling, increase the length of time between the off-line cleaning cycles, reduce economizer exit gas temperature and increase steam capacity while achieving unit design steam conditions. Design options were evaluated using a computerized heat transfer mathematical model calibrated to the current level of boiler performance. The model enabled design modifications to be evaluated and optimized with respect to performance, maintenance and cost. Considering both the performance and maintainability allowed the design team to make a final evaluation and design selection that provided the greatest value over a long-term period. The unit was designed, fabricated and erected within an 18-month schedule. Performance and optimization testing was accomplished 8 weeks after start-up. The unit has met all of its performance guarantees and is fully operational.
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Berichte der Organisationen zum Thema "Waste heat recovery boiler"

1

Grieco, A. (Waste water heat recovery system). Office of Scientific and Technical Information (OSTI), Mai 1990. http://dx.doi.org/10.2172/6839699.

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Levy, Edward, Harun Bilirgen und John DuPont. Recovery of Water from Boiler Flue Gas Using Condensing Heat Exchangers. Office of Scientific and Technical Information (OSTI), März 2011. http://dx.doi.org/10.2172/1084027.

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Edward Levy, Harun Bilirgen und John DuPoint. Recovery of Water from Boiler Flue Gas Using Condensing Heat Exchangers. Office of Scientific and Technical Information (OSTI), März 2011. http://dx.doi.org/10.2172/1037725.

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Jovovic, Vladimir. Thermoelectric Waste Heat Recovery Program for Passenger Vehicles. Office of Scientific and Technical Information (OSTI), Dezember 2015. http://dx.doi.org/10.2172/1337561.

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Johnson, Ilona, William T. Choate und Amber Davidson. Waste Heat Recovery. Technology and Opportunities in U.S. Industry. Office of Scientific and Technical Information (OSTI), März 2008. http://dx.doi.org/10.2172/1218716.

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Patch, K. D., und W. E. Cole. Fluidized-bed waste-heat recovery system development: Final report. Office of Scientific and Technical Information (OSTI), Juni 1988. http://dx.doi.org/10.2172/6411874.

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Hopman, Ulrich,, und Richard W. Kruiswyk. Diesel Engine Waste Heat Recovery Utilizing Electric Turbocompound Technology. Office of Scientific and Technical Information (OSTI), Juli 2005. http://dx.doi.org/10.2172/862432.

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Webb, Stephen W., Charles W. Morrow, Susan Jeanne Altman und Brian P. Dwyer. Water recovery using waste heat from coal fired power plants. Office of Scientific and Technical Information (OSTI), Januar 2011. http://dx.doi.org/10.2172/1008108.

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Subramanian, Swami Nathan. Affordable Rankine Cycle Waste Heat Recovery for Heavy Duty Trucks. Office of Scientific and Technical Information (OSTI), Juni 2017. http://dx.doi.org/10.2172/1375960.

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Smith, K., und M. Thornton. Feasibility of Thermoelectrics for Waste Heat Recovery in Conventional Vehicles. Office of Scientific and Technical Information (OSTI), April 2009. http://dx.doi.org/10.2172/951806.

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