Study of a fuel cell cogeneration system applied to a Brazilian tertiary sector

In this paper, a methodology for the study of a molten carbonate fuel cell cogeneration system and applied to a computer center building is developed. This system permits the recovery of waste heat, available between 600°C and 700°C, which can be used to the production of steam, hot and cold water, hot and cold air, depending on the recuperation equipment associated. Initially, some technical information about the most diffusing types of the fuel cell demonstration in the world are presented. In conclusion, the fuel cell cogeneration system may have an excellent opportunity to strengthen the decentralized energy production in the Brazilian tertiary sector.

Geração de energia por microturbina alimentada à biogás em uma propriedade rural: estudo de caso

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Células-combustível a etanol direto embarcadas em aeronaves: estudo de utilização e recuperação de calor residual

Pós-graduação em Engenharia Mecânica - FEG

Gasification technology assessment of sterile coal to clean electrical power generation.

Sterile coal is a low-value residue associated to the coal extraction and mining activity. According to the type and origin of the coal bed configuration, sterile coal production can mainly vary on quantity, calorific value and presence of sulphur compounds. In addition, the potential availability of sterile coal within Spain is apparently high and its contribution to the local power generation would be of interest playing a significant role. The proposed study evaluates the availability and deployment of gasification technologies to drive clean electricity generation from waste coal and sterile rock coal, incorporating greenhouse gas emission mitigation systems, like CO2, H2S and NOx removal systems. It establishes the target facility and its conceptual basic design proposal. The syngas obtained after the gasification of sterile coal is processed through specific conditioning units before entering into the combustion chamber of a gas turbine. Flue gas leaving the gas turbine is ducted to a heat recovery steam generation boiler; the steam produced within the boilerdrives a steam turbine. The target facility resembles a singular Integrated Gasification in Combined Cycle (IGCC) power station. The evaluation of the conceptual basic design according to the power output set for a maximum sterile contribution, established that rates over 95% H2S and 90% CO2 removal can be achieved. Noticeable decrease of NOx compounds can be also achieved by the use of commercial technology. A techno-economic approach of the conceptual basic design is made evaluating the integration of potential unitsand their implementation within the target facility aiming toachieve clean power generation. The criterion to be compliant with the most restrictive regulation regarding environmental emissions is setting to carry out this analysis.

Caracterización de la ventilación en la edificación residencial existente. Conciliación entre calidad del aire interior y eficiencia en la rehabilitación energética

La edificación residencial existente en España y en Europa se encuentra abocada a una rehabilitación profunda para cumplir los objetivos marcados en la estrategia europea para el año 2050. Estos, para el sector de la edificación, se proponen una reducción del 90% de emisiones de gases de efecto invernadero (GEI) respecto a niveles del año 1990. Este plan a largo plazo establece hitos intermedios de control, con objetivos parciales para el año 2020 y 2030. El objetivo último es aprovechar el potencial de reducción de demanda energética del sector de la edificación, del cual la edificación residencial supone el 85% en España. Dentro de estos requerimientos, de reducción de demanda energética en la edificación, la ventilación en la edificación residencial se convierte en uno de los retos a resolver por su vinculación directa a la salud y el confort de los ocupantes de la misma, y al mismo tiempo su relación proporcional con la demanda energética que presenta el edificio asociada al acondicionamiento térmico. Gran parte de las pérdidas térmicas de la edificación residencial se producen por el aire de renovación y la infiltración de aire a través de la envolvente. La directiva europea de eficiencia energética de la edificación (EPBD), que establece las directrices necesarias para alcanzar los objetivos de este sector en cuanto a emisiones de CO2 y gases de efecto invernadero (GEI), contempla la ventilación con aire limpio como un requisito fundamental a tener en cuenta de cara a las nuevas construcciones y a la rehabilitación energética de los edificios existentes. El síndrome del edificio enfermo, un conjunto de molestias y síntomas asociados a la baja calidad del aire de edificios no residenciales que surgió a raíz de la crisis del petróleo de 1973, tuvo su origen en una ventilación deficiente y una renovación del aire interior insuficiente de estos edificios, producto del intento de ahorro en la factura energética. Teniendo en cuenta que, de media, pasamos un 58% de nuestro tiempo en las viviendas, es fundamental cuidar la calidad del aire interior y no empeorarla aplicando medidas de “eficiencia energética” con efectos no esperados. Para conseguir esto es fundamental conocer en profundidad cómo se produce la ventilación en la edificación en bloque en España en sus aspectos de calidad del aire interior y demanda energética asociada a la ventilación. El objetivo de esta tesis es establecer una metodología de caracterización y de optimización de las necesidades de ventilación para los espacios residenciales existentes en España que aúne el doble objetivo de garantizar la calidad ambiental y reducir la demanda energética de los mismos. La caracterización del parque edificatorio residencial español en cuanto a ventilación es concluyente: La vivienda en España se distribuye principalmente en tres periodos en los que se encuentran más del 80% del total de las viviendas construidas. El periodo anterior a las normas básicas de la edificación (NBE), de 1960 a 1980, el periodo desde 1980 al año 2005, con el mayor número total de viviendas construidas, guiado por la NTE ISV 75, y el periodo correspondiente a la edificación construida a partir del Código Técnico de la Edificación, en 2006, cuyo documento básico de condiciones de salubridad (DB HS3) es la primera norma de obligado cumplimiento en diseño y dimensionamiento de ventilación residencial en España. La selección de un modelo de bloque de viviendas de referencia, un valor medio y representativo, seleccionado de entre estos periodos, pero con cualidades que se extienden más allá de uno de ellos, nos permite realizar un intensivo análisis comparativo de las condiciones de calidad de aire interior y la demanda energética del mismo, aplicando las distintas configuraciones que presenta la ventilación en viviendas dependiendo del escenario o época constructiva (o normativa) en que esta fuera construida. Este análisis se lleva a cabo apoyándose en un doble enfoque: el modelado numérico de simulaciones y el análisis de datos experimentales, para comprobar y afinar los modelos y observar la situación real de las viviendas en estos dos aspectos. Gracias a las conclusiones del análisis previo, se define una estrategia de optimización de la ventilación basada fundamentalmente en dos medidas: 1) La introducción de un sistema de extracción mecánica y recuperación de calor que permita reducir la demanda energética debida a la renovación del aire y a la vez diluir los contaminantes interiores más eficazmente para mejorar, de esta forma, la calidad del ambiente interior. 2) La racionalización del horario de utilización de estos sistemas, no malgastando la energía en periodos de no ocupación, permitiendo una leve ventilación de fondo, debida a la infiltración, que no incida en pérdidas energéticas cuantiosas. A esta optimización, además de aplicar la metodología de análisis previo, en cuanto a demanda energética y calidad del aire, se aplica una valoración económica integradora y comparativa basada en el reglamento delegado EU244/2012 de coste óptimo (Cost Optimal Methodology). Los resultados principales de esta tesis son: • Un diagnóstico de la calidad del aire interior de la edificación residencial en España y su demanda energética asociada, imprescindible para lograr una rehabilitación energética profunda garantizando la calidad del aire interior. • Un indicador de la relación directa entre calidad de aire y demanda energética, para evaluar la adecuación de los sistemas de ventilación, respecto de las nuevas normativas de eficiencia energética y ventilación. • Una estrategia de optimización, que ofrece una alternativa de intervención, y la aplicación de un método de valoración que permite evaluar la amortización comparada de la instalación de los sistemas. ABSTRACT The housing building stock already built in Spain and Europe faces a deep renovation in the present and near future to accomplish with the objectives agreed in the European strategy for 2050. These objectives, for the building sector, are set in a 90% of Green House Gases (GHG) reduction compared to levels in 1990. This long‐term plan has set milestones to control the correct advance of achievement in 2020 and 2030. The main objective is to take advantage of the great potential to reduce energy demand from the building sector, in which housing represents 85% share in Spain. Among this reduction on building energy demand requirements, ventilation of dwellings becomes one of the challenges to solve as it’s directly connected to the indoor air quality (IAQ) and comfort conditions for the users, as well as proportional to the building energy demand on thermal conditioning. A big share of thermal losses in housing is caused by air renovation and infiltration through the envelope leaks. The European Directive on Building energy performance (EPBD), establishes the roots needed to reach the building sector objectives in terms of CO2 and GHG emissions. This directive sets the ventilation and renovation with clean air of the new and existing buildings as a fundamental requirement. The Sick Building Syndrome (SBS), an aggregation of symptoms and annoys associated to low air quality in non residential buildings, appeared as common after the 1973 oil crisis. It is originated in defective ventilation systems and deficient air renovation rates, as a consequence of trying to lower the energy bill. Accounting that we spend 58% of our time in dwellings, it becomes crucial to look after the indoor air quality and focus in not worsening it by applying “energy efficient” measures, with not expected side effects. To do so, it is primary to research in deep how the ventilation takes place in the housing blocks in Spain, in the aspects related to IAQ and ventilation energy demand. This thesis main objective is to establish a characterization and optimization methodology regarding the ventilation needs for existing housing in Spain, considering the twofold objective of guaranteeing the air quality as reducing the energy demand. The characterization of the existing housing building stock in Spain regarding ventilation is conclusive. More of 80% of the housing stock is distributed in 3 main periods: before the implementation of the firsts regulations on building comfort conditions (Normas Básicas de la Edificación), from 1960 to 1980; the period after the first recommendations on ventilation (NTE ISV 75) for housing were set, around 1980 until 2005 and; the period corresponding to the housing built after the existing mandatory regulation in terms of indoor sanity conditions and ventilation (Spanish Building Code, DB HS3) was set, in 2006. Selecting a representative blueprint of a housing block in Spain, which has medium characteristics not just within the 3 periods mention, but which qualities extent beyond the 3 of them, allows the next step, analyzing. This comparative and intense analyzing phase is focused on the air indoor conditions and the related energy demand, applying different configurations to the ventilation systems according to the different constructive or regulation period in which the building is built. This analysis is also twofold: 1) Numerical modeling with computer simulations and 2) experimental data collection from existing housing in real conditions to check and refine the models to be tested. Thanks to the analyzing phase conclusions, an optimization strategy on the ventilation of the housing stock is set, based on two actions to take: 1) To introduce a mechanical exhaust and intake ventilation system with heat recovery that allows reducing energy demand, as improves the capacity of the system to dilute the pollutant load. This way, the environmental quality is improved. 2) To optimize the schedule of the system use, avoids waste of energy in no occupancy periods, relying ventilation during this time in a light infiltration ventilation, intended not to become large and not causing extra energy losses. Apart from applying the previous analyzing methodology to the optimization strategy, regarding energy demand and air quality, a ROI valorization is performed, based on the cost optimal methodology (delegated regulation EU244/2012). The main results from the thesis are: • To obtain a through diagnose regarding air quality and energy demand for the existing housing stock in Spain, unavoidable to reach a energy deep retrofitting scheme with no air quality worsening. • To obtain a marker to relate air quality and energy demand and evaluate adequateness of ventilation systems, for the new regulations to come. • To establish an optimization strategy to improve both air quality and energy demand, applying a compared valorization methodology to obtain the Return On Investment (ROI).

A study of thermodynamic characteristics and predictive computer modelling of an air to water heat pump system

A study on heat pump thermodynamic characteristics has been made in the laboratory on a specially designed and instrumented air to water heat pump system. The design, using refrigerant R12, was based on the requirement to produce domestic hot water at a temperature of about 50 °C and was assembled in the laboratory. All the experimental data were fed to a microcomputer and stored on disk automatically from appropriate transducers via amplifier and 16 channel analogue to digital converters. The measurements taken were R12 pressures and temperatures, water and R12 mass flow rates, air speed, fan and compressor input powers, water and air inlet and outlet temperatures, wet and dry bulb temperatures. The time interval between the observations could be varied. The results showed, as expected, that the COP was higher at higher air inlet temperatures and at lower hot water output temperatures. The optimum air speed was found to be at a speed when the fan input power was about 4% of the condenser heat output. It was also found that the hot water can be produced at a temperature higher than the appropriate R12 condensing temperature corresponding to condensing pressure. This was achieved by condenser design to take advantage of discharge superheat and by further heating the water using heat recovery from the compressor. Of the input power to the compressor, typically about 85% was transferred to the refrigerant, 50 % by the compression work and 35% due to the heating of the refrigerant by the cylinder wall, and the remaining 15% (of the input power) was rejected to the cooling medium. The evaporator effectiveness was found to be about 75% and sensitive to the air speed. Using the data collected, a steady state computer model was developed. For given input conditions s air inlet temperature, air speed, the degree of suction superheat , water inlet and outlet temperatures; the model is capable of predicting the refrigerant cycle, compressor efficiency, evaporator effectiveness, condenser water flow rate and system Cop.

Energy conservation in the steel industry

The last few years have witnessed an unprecedented increase in the price of energy available to industry in the United Kingdom and worldwide. The steel industry, as a major consumer of energy delivered in U.K. (8% of national total and nearly 25% of industrial total) and whose energy costs currently form some 28% of the total manufacturing cost, is very much aware of the need to conserve energy. Because of the complexities of steelmaking processes it is imperative that a full understanding of each process and its interlinking role in an integrated steelworks is understood. An analysis of energy distribution shows that as much as 70% of heat input is dissipated to the environment in a variety of forms. Of these, waste gases offer the best potential for energy conservation. The study identifies areas for and discusses novel methods of energy conservation in each process. Application of these schemes in BSC works is developed and their economic incentives highlighted. A major part of this thesis describes design, development and testing of a novel ceramic rotary regenerator for heat recovery from high temperature waste gases, where no such system is available. The regenerator is a compact, efficient heat exchanger. Application of such a system to a reheating furnace provides a fuel saving of up to 40%. A mathematical model developed is verified on the pilot plant. The results obtained confirm the success of the concept and material selection and outlines the work needed to develop an industrial unit. Last, but not least, the key position of an energy manager in an energy conservation programme is identified and a new Energy Management Model for the BSC is developed.

Economic efficiency of mobile latent heat storages

In a pilot project an optimized mobile latent heat storage based on a system available on the market has been tested at Fraunhofer Institute for Environmental, Safety and Energy Technology. Initially trials were conducted with the aim of optimizing the process of charging and discharging. A specifically constructed test rig at the incineration trials centre at the institute allowed charging and discharging procedures of the mobile latent heat storage with adjustable parameters. In addition an evaluation model was constructed to further optimize the heat exchanger systems. In conclusion the prototype of the mobile latent heat storage was tested in practical operation. The economic and technical feasibility of heat transportation was shown if not utilized waste heat is available. © 2014 The Authors.

Low-temperature isothermal Rankine cycle for desalination

In brackish groundwater desalination, high recovery ratio (of fresh water from saline feed) is desired to minimise concentrate reject. To this effect, previous studies have developed a batch reverse osmosis (RO) desalination system, DesaLink, which proposed to expand steam in a reciprocating piston cylinder and transmit the driving force through a linkage crank mechanism to pressurise batches of saline water (recirculating) in a water piston cylinder unto RO membranes. However, steam is largely disadvantaged at operation from low temperature (< 150oC) thermal sources; and organic working fluids are more viable, though, the obtainable thermal cycle efficiencies are generally low with low temperatures. Consequently, this thesis proposed to investigate the use of organic working fluid Rankine cycle (ORC) with isothermal expansion, to drive the DesaLink machine, at improved thermal efficiency from low temperature thermal sources. Following a review of the methods of achieving isothermal expansion, ‘liquid flooded expansion’ and ‘expansion chamber surface heating’ were identified as potential alternative methods. Preliminary experimental comparative analysis of variants of the heated expansion chamber technique of effecting isothermal expansion favoured a heated plain wall technique, and as such was adopted for further optimisation and development. Further, an optimised isothermal ORC engine was built and tested at < 95oC heat source temperature, with R245fa working fluid – which was selected from 16 working fluids that were analysed for isothermal operation. Upon satisfactory performance of the test engine, a larger (10 times) version was built and coupled to drive the DesaLink system. Operating the integrated ORC-RO DesaLink system, gave freshwater (approximately 500 ppm) production of about 12 litres per hour (from 4000 ppm feed water) at a recovery ratio of about 0.7 and specific energy consumption of 0.34 kWh/m3; and at a thermal efficiency of 7.7%. Theoretical models characterising the operation and performance of the integrated system was developed and utilised to access the potential field performance of the system, when powered by two different thermal energy sources – solar and industrial bakery waste heat – as case studies.

Heat dissipation from carbon nano-electronics

The incorporation of graphitic compounds such as carbon nanotubes (CNTs) and graphene into nano-electronic device packaging holds much promise for waste heat management given their high thermal conductivities. However, as these graphitic materials must be used in together with other semiconductor/insulator materials, it is not known how thermal transport is affected by the interaction. Using different simulation techniques, in this thesis, we evaluate the thermal transport properties - thermal boundary conductance (TBC) and thermal conductivity - of CNTs and single-layer graphene in contact with an amorphous SiO2 (a-SiO2) substrate. First, the theoretical methodologies and concepts used in our simulations are presented. In particular, two concepts are described in detail as they are necessary for the understanding of the subsequent chapters. The first is the linear response Green-Kubo (GK) theory of thermal boundary conductance (TBC), which we develop in this thesis, and the second is the spectral energy density method, which we use to directly compute the phonon lifetimes and thermal transport coefficients. After we set the conceptual foundations, the TBC of the CNT-SiO2 interface is computed using non- equilibrium molecular dynamics (MD) simulations and the new Green-Kubo method that we have developed. Its dependence on temperature, the strength of the interaction with the substrate, and tube diameter are evaluated. To gain further insight into the phonon dynamics in supported CNTs, the scattering rates are computed using the spectral energy density (SED) method. With this method, we are able to distinguish the different scattering mechanisms (boundary and CNT-substrate phonon-phonon) and rates. The phonon lifetimes in supported CNTs are found to be reduced by contact with the substrate and we use that lifetime reduction to determine the change in CNT thermal conductivity. Next, we examine thermal transport in graphene supported on SiO2. The phonon contribution to the TBC of the graphene-SiO2 interface is computed from MD simulations and found to agree well with experimentally measured values. We derive the theory of remote phonon scattering of graphene electrons and compute the heat transfer coefficient dependence on doping level and temperature. The thermal boundary conductance from remote phonon scattering is found to be an order of magnitude smaller than that of the phonon contribution. The in-plane thermal conductivity of supported graphene is calculated from MD simulations. The experimentally measured order of magnitude reduction in thermal conductivity is reproduced in our simulations. We show that this reduction is due to the damping of the flexural (ZA) modes. By varying the interaction between graphene and the substrate, the ZA modes hybridize with the substrate Rayleigh modes and the dispersion of the hybridized modes is found to linearize in the strong coupling limit, leading to an increased thermal conductance in the composite structure.

Biomassan energia-arvon nostaminen sekundäärilämmöllä kuivaamalla

Viime aikoina ilmastonmuutos, fossiilisten polttoaineiden väheneminen ja niiden hinnan nousu ovat lisänneet merkittävästi maailmanlaajuista kiinnostusta uusiutuviin energiavaroihin. Suomessa uusiutuvien energialähteiden käytössä on jo pitkään panostettu metsäteollisuuden sivutuotevirtana tuottamaan puuperäiseen biomassaan, jota metsäteollisuus käyttää energiantuotantoonsa. Metsäteollisuuden jätevesien käsittelyssä syntyy erilaisia lietteitä, jotka joko uusiokäytetään tai hävitetään polttamalla tai sijoittamalla kaatopaikalle. Erityisesti biolietteiden uusiokäyttö on hankalaa ja kaatopaikkasijoitus tulevaisuudessa mahdotonta tai ainakin kustannuksiltaan kohtuutonta. Käytännössä liete hävitetään polttamalla ja kuivaamalla siitä tulee polttoaine. Lietteiden energiakäyttö on järkevin tapa hävittää jäteliete. Lietteiden korkean vesipitoisuuden vuoksi ne tulee kuitenkin kuivata ennen polttoa. Lietteen kuivaaminen sekundäärienergiavirralla eli metsäteollisuusprosesseissa sivutuotteena muodostuvalla ns. hukkalämmöllä lisää lietteen poltosta saatavaa energiamäärää ja korvaa fossiilisten polttoaineiden käyttöä. Tutkimuksen tavoitteena oli selvittää lietteen kuivaukseen optimaalisin kuoren ja lietteen seossuhde eri kuivausparametrejä vaihdellen. Kokeellinen työ aloitettiin rakentamalla energiatekniikan koehalliin laboratoriokokoluokan kiintopetikuivuri, jossa kuivumista tutkittiin puhaltamalla polttoainepedin läpi lämmitettyä ilmaa. Kuivattavina polttoaineina olivat kuoren ja lietteen seos tai pelkkä kuori ja liete erilaisilla massoilla ja erilaisilla prosenttisilla suhteilla ja erilaisissa lämpötiloissa. Kuivumiskäyrien määritys perustui massanmuutokseen. Koelaitteessa olivat anturit lämpötilan mittausta varten, jotta lämpötila saatiin säädettyä ja seurattua kokeen edellyttämällä tavalla. Lämpötilat ja painonmuutokset tallentuivat koetta tehdessä tietokoneelle. Kuivauskokeet osoittivat, että liete-kuori seos kuivuu hyvin kiintopedissä kun lietteen massaosuus seoksessa on korkeintaan 50 %. Lietteen massaosuuden ollessa tätä suurempi kuivaaminen ei enää ole tehokasta, mikä johtuu luultavasti ilman suuresta kanavoitumisesta kuivauspedissä. Kuorta kuivatessa lämpötilan nosto 50 °C:stä 70 °C:een oli huomattavasti tehokkaampaa kuin 70 °C:stä 90 °C:een, ajallisesti ero oli noin kaksinkertainen.

Demi-glace-kastikepohjan valmistuksen optimointi ylipainekeittomenetelmälle

Tämän tutkimuksen kirjallisuusosan tavoitteena oli selvittää perinteisen kastikepohjan valmistukseen ja valmistuksen kokonaisvaltaiseen onnistumiseen vaikuttavia seikkoja. Lisäksi käsiteltiin kastikepohjan valmistukseen liittyviä ympäristö- ja energia-asioita, kuten eläinperäisten sivutuotteiden kierrätysmahdollisuuksia. Kokeellisessa osassa tutkimuksen keskeinen lähtökohta oli pyrkiä löytämään ratkaisu ylipainekeittomenetelmään liittyvään kastikepohjan liemiaineksen sameutumisongelmaan. Tutkimuksessa haluttiin löytää syyt sameuden muodostumiseen luiden painekeitossa (max. 1,5 bar). Näin pyrittiin selvittämään keinot sameuden syntymisen estämiseen tai tuotteesta poistamiseen. Ratkaisua etsittiin sekä keittoaika-paine-kombinaatiosta että proteolyyttisen entsyymivalmisteen käytöstä. Tavoitteena oli ulkonäöltään kirkas ja kuiva-ainepitoisuudeltaan mahdollisimman korkea naudanmakuinen demi-glace-kastikepohjaliemi. Liemiaineksista tarkasteltiin kuiva-aine-, kokonaisproteiini- ja sidekudosproteiinipitoisuuksia, pH-arvoja sekä sameutta, ja vertailtiin näitä tuloksia käytettyihin valmistusmenetelmiin ja -olosuhteisiin. Lisäksi otettiin selvää lämmöntalteenoton parantamis-mahdollisuuksista. Tutkimuksessa valmistetun kastikepohjaliemen kuiva-aine koostui pääasiassa proteiineista. Liemen valmistuksessa suuremmalla paineella päästiin hieman nopeammin samoihin kuiva-ainepitoisuuksiin kuin matalammalla paineella. Samoin tapahtui entsyymiä käytettäessä kuin käyttämättä jätettäessä. Tämän tutkimuksen perusteella korkeaa kuiva-ainepitoisuutta tavoiteltaessa kastikepohjaliemen valmistuksessa on valittava korkean sidekudosproteiinin tai sameuden väliltä. Ylipainekeitolla luista saatiin irti lähes pelkästään sidekudosproteiinia, koska luita kuumennettaessa vain kollageeni liukeni veteen muiden proteiinien saostuessa. Lämmöntalteenottojärjestelmien rakentaminen pieneen elintarviketeollisuusyritykseen voi olla kannattamatonta, koska investointikustannuksia ei välttämättä pystytä maksamaan takaisin. Energiatehokkuuden parantaminen pienessä elintarviketeollisuusyrityksessä on haastavaa, mutta kuitenkin mahdollista ammattilaisten tekemien tarkkojen laskelmien ja arviointien avulla.

Thermodynamic modelling of absorption-resorption heating cycles with some new working pairs

This paper presents the results of a thermodynamic cycle analysis of single stage resorption heat pump (RHP) and resorption heat transformer (RHT) cycles with the new working pairs R22-NMP and R22-DMA. The coefficients of performance (COP) are correlated with the low grade source temperature, temperature at which useful heat is obtained and ambient temperature. The COPs are in the range 1.20–1.60 for the RHP mode and 0.25–0.45 for the RHT mode. Absorber temperatures (useful temperatures) as high as 50°C in the RHP mode and 87°C in the RHT mode have been obtained. It is observed that absorption-resorption systems are inflexible in their range of operating temperature and necessitate a higher pump work as compared with simple single-stage absorption heating systems. However, single stage RHTs show higher temperature boosts than simple absorption heat transformers.

Experimental results of an activated carbon-HFC 134a adsorption cooling system for thermal management of electronics

Results of performance measurement of a small cooling capacity laboratory model of an adsorption refrigeration system for thermal management of electronics are compiled. This adsorption cooler was built with activated carbon as the adsorbent and HFC 134a as the refrigerant to produce a cooling capacity under 5 W using waste heat up to 90 degrees C. The thermal compression process is obtained from an ensemble of four solid sorption compressors. Parametric study was conducted with cycle times of 16 and 20 min, heat source temperatures from 73 to 87 degrees C and cooling loads from 3 to 4.9W. Overall system performance is analyzed using two indicators, namely, cooling effectiveness and normalized exergetic efficiency. (C) 2011 Elsevier Ltd. All rights reserved.

Numerical analysis on thermoacoustic prime movers for development of pulse tube cryocoolers

Thermo Acoustic Prime Movers (TAPMs) are being considered as the ideal choice for driving the Pulse Tube Cryocoolers replacing the conventional compressors. The advantages are the absence of moving components and they can be driven by low grade energy as such as fuel, gas, solar energy, waste heat etc. While the development of such TAPMs is in progress in our laboratory, their design and fabrication should be guided by numerical modeling and this may be done by several methods such as solving the energy equation 1], enthalpy flow model 2], CFD 3], etc. We have used CFD technique, since it provides a better insight into the velocity and temperature profiles. The analysis is carried out by varying parameters such as (a) temperature difference across the stack, (b) stack and resonator lengths and (c) different working fluids such as air, nitrogen, argon etc. The theoretical results are compared with the experimental data wherever possible and they are in reasonably good agreement with each other. The analysis indicate that (i) larger temperature difference across the stack leads to increased acoustic amplitude, (ii) longer resonator leads to decrease in frequency with lesser amplitude and (iii) there exists an optimal stack length for the best performance of TAPM. These results are presented here.