801 resultados para heat output


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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.

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This thesis records the design and development of an electrically driven, air to water, vapour compression heat pump of nominally 6kW heat output, for residential space heating. The study was carried out on behalf of GEC Research Ltd through the Interdisciplinary Higher Degrees Scheme at Aston University. A computer based mathematical model of the vapour compression cycle was produced as a design aid, to enable the effects of component design changes or variations in operating conditions to be predicted. This model is supported by performance testing of the major components, which revealed that improvements in the compressor isentropic efficiency offer the greatest potential for further increases in cycle COPh. The evaporator was designed from first principles, and is based on wire-wound heat transfer tubing. Two evaporators, of air side area 10.27 and 16.24m2, were tested in a temperature and humidity controlled environment, demonstrating that the benefits of the large coil are greater heat pump heat output and lower noise levels. A systematic study of frost growth rates suggested that this problem is most severe at the conditions of saturated air at 0oC combined with low condenser water temperature. A dynamic simulation model was developed to predict the in-service performance of the heat pump. This study confirmed the importance of an adequate radiator area for heat pump installations. A prototype heat pump was designed and manufactured, consisting of a hermetic reciprocating compressor, a coaxial tube condenser and a helically coiled evaporator, using Refrigerant 22. The prototype was field tested in a domestic environment for one and a half years. The installation included a comprehensive monitoring system. Initial problems were encountered with defrosting and compressor noise, both of which were solved. The unit then operated throughout the 1985/86 heating season without further attention, producing a COPh of 2.34.

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Até 2020, a Europa terá de reduzir 20% das suas emissões de gases com efeito de estufa, 20% da produção de energia terá de ser proveniente de fontes renováveis e a eficiência energética deverá aumentar 20%. Estas são as metas apresentadas pela União Europeia, que ficaram conhecidas por 20/20/20 [1]. A Refinaria de Matosinhosé um complexo industrial que opera no sector da refinação e que apresenta preocupações ao nível da eficiência energética e dos aspectos ambientais subjacentes. No âmbito da racionalização energética das refinarias, a Galp Energia tem vindo a implementar um conjunto de medidas, adoptando as melhores tecnologias disponíveis com o objectivo de diminuir os consumos de energia, promover a eficiência energética e reduzir as emissões de dióxido de carbono. Para ir de encontro a estas medidas foi elaborado um estudo comparativo que permitiu à empresa definir as medidas consideradas prioritárias. Uma solução encontrada visa a execução de projectos que não requerem investimento e que têm acções imediatas, tais como o aumento da eficiência energética das fornalhas [1]. Este trabalho realizado na Galp Energia S.A. teve como objectivo principal a optimização energética da Unidade de Desalfatação do Propano da Fábrica de Óleos Base. Esta optimização baseou-se no aproveitamento energético da corrente de fundo da coluna de rectificação T2003C com uma potência calorífica de 2,79 Gcal/h. Após levantamento de todas as variáveis do processo relativas a esta unidade, especialmente a potência calorífica das correntes envolvidas chegou-se á conclusão que a fornalha H2101 poderá ser substituída por dois permutadores, reduzindo desta forma os consumos energéticos. Pois a corrente de fundo da coluna T2003 com uma potência calorífica 2,79 Gcal/h poderá permutar calor com a corrente da mistura asfalto com propano, fazendo com que esta atinja temperatura superior à obtida com a fornalha em funcionamento. A análise económica ao consumo e respectivo custo do fuelóleo na fornalha para o período de um ano foi realizada, sendo o seu custo de combustível de 611.396,00 €. O valor da aquisição dos permutadores é 86.355,97€, sendo rentável a alteração proposta neste projecto.

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Nowadays the used fuel variety in power boilers is widening and new boiler constructions and running models have to be developed. This research and development is done in small pilot plants where more faster analyse about the boiler mass and heat balance is needed to be able to find and do the right decisions already during the test run. The barrier on determining boiler balance during test runs is the long process of chemical analyses of collected input and outputmatter samples. The present work is concentrating on finding a way to determinethe boiler balance without chemical analyses and optimise the test rig to get the best possible accuracy for heat and mass balance of the boiler. The purpose of this work was to create an automatic boiler balance calculation method for 4 MW CFB/BFB pilot boiler of Kvaerner Pulping Oy located in Messukylä in Tampere. The calculation was created in the data management computer of pilot plants automation system. The calculation is made in Microsoft Excel environment, which gives a good base and functions for handling large databases and calculations without any delicate programming. The automation system in pilot plant was reconstructed und updated by Metso Automation Oy during year 2001 and the new system MetsoDNA has good data management properties, which is necessary for big calculations as boiler balance calculation. Two possible methods for calculating boiler balance during test run were found. Either the fuel flow is determined, which is usedto calculate the boiler's mass balance, or the unburned carbon loss is estimated and the mass balance of the boiler is calculated on the basis of boiler's heat balance. Both of the methods have their own weaknesses, so they were constructed parallel in the calculation and the decision of the used method was left to user. User also needs to define the used fuels and some solid mass flowsthat aren't measured automatically by the automation system. With sensitivity analysis was found that the most essential values for accurate boiler balance determination are flue gas oxygen content, the boiler's measured heat output and lower heating value of the fuel. The theoretical part of this work concentrates in the error management of these measurements and analyses and on measurement accuracy and boiler balance calculation in theory. The empirical part of this work concentrates on the creation of the balance calculation for the boiler in issue and on describing the work environment.

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Tämä tutkimus tehtiin osana Vapo Oy:n uuden turvetuotantotekniikan kehitystä. Kihniön Aitonevalle on rakennettu uuden turvetuotantotekniikan tutkimusalue, johon kuuluu muun muassa yksi lämmittämätön kuivatuskenttä sekä yksi aurinkolämmöllä lämmitetty kuivatuskenttä aurinkokeräimineen ja putkistoineen. Työn tavoitteena oli selvittää aurinkolämmöllä lämmitetyn kuivatuskentän tuotannon teho verrattuna lämmittämättömään kenttään. Toinen tavoite oli selvittää Aitonevan tutkimusalueella käytössä olevista aurinkokeräimistä turpeen kuivaustarkoitukseen parhaiten soveltuva keräin. Tuotantoa uudella menetelmällä tehtiin vuoden 2005 kesän ajan. Tuotantotehon ero pyrittiin selvittämään seuraamalla yksittäisten turvetuotantoerien eli satokiertojen kuivumista kosteusnäyttein ja toisaalta vertaamalla koko kesän aikana saatua tuotantoa. Aurinkokeräimien vertailu toteutettiin energiamäärä- ja hyötysuhdemittauksin. Lisäksi kuivatuskenttien lämpötiloja mitattiin kentässä tapahtuvan lämmönsiirron selvittämiseksi. Mittausten perusteella havaittiin, ettälämmitetyn ja lämmittämättömän kentän välillä on tutkimuksen aikaisella kenttärakenteella 6-8 % ero satokierron aikana haihdutetussa vesimäärässä. Tätä voidaanpitää odotuksia pienempänä. Kenttien lämpötilamittausten perusteella osoittautui, että kentän pintarakenne tulisi eristää maaperästä, koska kentän alle siirrettyä lämpöä siirtyy häviöinä kylmään pohjamaahan. Käytössä olleista aurinkokeräimistä parhaaksi osoittautui katettu kumimattokeräin niin hyötysuhteen kuin tehokkuudenkin puolesta. Työn aikana todettiin, että tutkimusta keräimien ja varsinkinkenttärakenteen suhteen tulee jatkaa tulevaisuudessa ennen aurinkokeräinkentän laajamittaisen käytön aloittamista.

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Diplomityön tavoitteena on määrittää rajahinta Mertaniemen lämmitysvoimalaitoksella tuotetun kaukolämpöenergian korvaamiselle erillishankinnalla Lappeenrannan Energian kannalta tarkasteltuna. Tarkoituksena on muodostaa taulukkolaskentapohjat erilaisille lämmönkorvaustapauksille sekä päivittää kyseisen lämmitysvoimalaitoksen sähköteho/kaukolämpöteho -karakteristikat. Työssä selvitetään myös lämmön erillishankinnan vaikutusta laitoksen ajotapaan. Laadittujen laskentapohjien ja karakteristikoiden avulla arvioitiin erillishankinnan kannattavuutta suunnitellun UPM-Kymmene Oyj:n Kaukaan voimalaitoksen, paikkakunnan teollisuuslaitoksien, Mertaniemen voimalaitoksen kaasukattiloiden sekä Lappeenrannan Energian lämpökeskuksien lämmöntuotannon tapauksissa. Lisäksi työssä tehtiin kustannuslaskelma kiinteälle lämpökeskukselle sekä laadittiin optimointilaskelma lämmöntuotannon polttoaineiden käytölle. Tuloksiksi saatiin, että yhteistuotanto on erillishankintaa paljon edullisempaa kaikissa tapauksissa. Kaukaan voimalaitoshankkeesta Lappeenrannan Energia jättäytyi täten toistaiseksi pois. Paikkakunnan teollisuuslaitoksilta ostetaan lämpöä edelleen, koska se on todettu edulliseksi yhteistuotannon seisokkien aikaan. Lappeenrantaan suunnitellaan uutta kiinteää lämpökeskusta, mutta sen käyttö korvaamaan yhteistuotantoa ei kannata nykyisillä polttoaineen hinnoilla.

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Energiantuotantoa koskeva jatkuvasti tiukentuva lainsäädäntö ja yleinen tarve polttaa yhä vaativampia polttoaineita asettaa leijukerroskattiloille suuria haasteita. Eräs käyttökelpoinen työkalu tulevaisuuden haasteisiin vastaamisessa on säädettävä leijukerroslämmönsiirrin. Tiheässä leijukerroksessa toimiva lämmönsiirrin on vähemmän alttiina korroosiolle kuin savukaasukanavistossa sijaitsevat rakenteet. Rakenne tuo tarpeellista säädettävyyttä koko kattilalle, mikäli lämmönsiirtimen antamaa tehoa voidaan säätää tehokkaasti. Erityisen hyvä tilanne saavutetaan, jos lämmönsiirrin kykenee käyttämään hyväkseen tulipesän sisäistä kiintoainekiertoa. Tässä työssä tutkitaan kiertoleijukattilaan sijoitettavan leijukerroslämmönsiirtimen säädön toteuttamista leijutusjärjestelyjen avulla. Teoreettinen tarkastelu keskittyy leijukerroslämmönsiirtimen toimintaolosuhteisiin ja kiintoainevirtauksen säätömahdollisuuksiin. Kokeellisessa osuudessa etsitään käytännössä toimivaa säätöperiaatetta tutkimuksen kohteena olevalle leijukerroslämmönsiirrinrakenteelle.

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Tyypillisesti sahoilla tarvittava lämpö tuotetaan omalla lämpölaitoksella, jossa hyödynnetään sahalla syntyviä sivutuotteita kuten kuorta ja purua. Lämmöntuotantoon ei yleensä käytetä lainkaan öljyä. Jos lämpölaitoksen teho ei riitä tai lämmöntuotannossa syntyy katkoksia, tyydytään rajoittamaan tuotantoa tai annetaan sahatavaran laadun kärsiä. Diplomityössä etsitään taloudellisesti kannattavia konsepteja, joilla voidaan parantaa lämmöntuotannon varmuutta sahoilla. Työssä tarkastellaan sahoja kolmessa eri kokoluokassa, kattaen yleisimmät sahalaitokset. Koska diplomityöhön ei otettu malliksi mitään tiettyä sahaa, määritettiin em. kolmelle kokoluokalle materiaali- ja energiavirrat yleisten tunnuslukujen perusteella. Lisäksi sahoille määritettiin kuivaustiedot, kun kaikilla sahoilla oletettiin olevan ainoastaan kamarikuivaamoita. Sahojen käyttämä kuori on kosteaa, ja se asettaa käytettävälle polttotekniikalle korkeat vaatimukset. Kuoren lämpöarvoa voidaan parantaa kuivattamalla sitä ennen polttoa erillisessä kuivurissa. Diplomityössä tarkastellaan suoraa ja epäsuoraa kuivatusta, joista molemmat perustuvat kiertoleijutekniikkaan. Suorassa kuivatuksessa hyödynnetään kattilasta saatavia savukaasuja, kun taas epäsuorassa kuivatuksessa lämmönlähteenä käytetään kuuma vettä. Molempien kuivatuskonseptien osalta käydään läpi toimintaperiaate ja kytkentä lämpölaitokseen, sekä lasketaan lämmöntuotannon omakustannushinta. Lisäksi tarkastellaan suoran kuivatuksen asentamista nykyiseen kostean polttoaineen laitokseen. Kuoren kuivatuksen lisäksi arvioidaan kuumavesikattilan käyttöä sahoilla ja sahatavaran kuivauksessa tarvittavan erillisen höyrynkehityksen korvaamista kuumavesiakulla. Lopuksi diplomityössä tarkastellaan pienimuotoista sähköntuotantoa sahojen lämpölaitosten yhteydessä ja sen kannattavuutta. Tarkasteltavia tekniikoita ovat ORC –tekniikka sekä höyrykone.

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The present study shows that with liquid nitrogen stored inocula of Saccharomyces cerevisiae, and standardized experimental procedure, flow microcalorimetry can be a valuable tool for monitoring in real time the alcoholic fermentation processes on line. The avaliation of cultural conditions contained different carbon sources for alcohol fermentation (sucrose, glucose, fructose, manose, maltose, galactose, molasses, honey and sugar cane) and their effects on the heat output recording is discussed. Some examples of diauxic growth is given, where the microcalorimeters serves to detect the temporal order of succession of alternating metabolic pathways.

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A ventilation radiator is a combined ventilation and heat emission unit currently of interest due to its potential for increasing energy efficiency in exhaust ventilated buildings with warm water heating. This paper presents results of performance tests of several ventilation radiator models conducted under controlled laboratory conditions.   The purpose of the study was to validate results achieved by Computational Fluid Dynamics (CFD) in an earlier study and indentify possible improvements in the performance of such systems. The main focus was on heat transfer from internal convection fins, but comfort and health aspects related to ventilation rates and air temperatures were also considered.   The general results from the CFD simulations were confirmed; the heat output of ventilation radiators may be improved by at least 20 % without sacrificing ventilation efficiency or thermal comfort.   Improved thermal efficiency of ventilation radiators allows a lower supply water temperature and energy savings both for heating up and distribution of warm water in heat pumps or district heating systems. A secondary benefit is that a high ventilation rate can be maintained all year around without risk for cold draught.

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In order to verify the effects of heat and exercise acclimation (HA) on resting and exercise-induced expression of plasma and leukocyte heat shock protein 72 (Hsp72) in humans, nine healthy young male volunteers (25.0 +/- 0.7 years; 80.5 +/- 2.0 kg; 180 +/- 2 cm, mean +/- SE) exercised for 60 min in a hot, dry environment (40 +/- 0A degrees C and 45 A +/- 0% relative humidity) for 11 days. The protocol consisted of running on a treadmill using a controlled hyperthermia technique in which the work rate was adjusted to elevate the rectal temperature by 1A degrees C in 30 min and maintain it elevated for another 30 min. Before and after the HA, the volunteers performed a heat stress test (HST) at 50% of their individual maximal power output for 90 min in the same environment. Blood was drawn before (REST), immediately after (POST) and 1 h after (1 h POST) HST, and plasma and leukocytes were separated and stored. Subjects showed expected adaptations to HA: reduced exercise rectal and mean skin temperatures and heart rate, and augmented sweat rate and exercise tolerance. In HST1, plasma Hsp72 increased from REST to POST and then returned to resting values 1 h POST (REST: 1.11 A +/- 0.07, POST: 1.48 A +/- 0.10, 1 h POST: 1.22 A +/- 0.11 ng mL(-1); p < 0.05). In HST2, there was no change in plasma Hsp72 (REST: 0.94 A +/- 0.08, POST: 1.20 A +/- 0.15, 1 h POST: 1.17 A +/- 0.16 ng mL(-1); p > 0.05). HA increased resting levels of intracellular Hsp72 (HST1: 1 A +/- 0.02 and HST2: 4.2 A +/- 1.2 density units, p < 0.05). Exercise-induced increased intracellular Hsp72 expression was observed on HST1 (HST1: REST, 1 A +/- 0.02 vs. POST, 2.9 A +/- 0.9 density units, mean +/- SE, p < 0.05) but was inhibited on HST2 (HST2: REST, 4.2 +/- 1.2 vs. POST, 4.4 +/- 1.1 density units, p > 0.05). Regression analysis showed that the lower the pre-exercise expression of intracellular Hsp72, the higher the exercise-induced increase (R = -0.85, p < 0.05). In conclusion, HA increased resting leukocyte Hsp72 levels and inhibited exercise-induced expression. This intracellular adaptation probably induces thermotolerance. In addition, the non-increase in plasma Hsp72 after HA may be related to lower stress at the cellular level in the acclimated individuals.

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The combined-cycle gas and steam turbine power plant presents three main pieces of equipment: gas turbines, steam turbines and heat recovery steam generator (HRSG). In case of HRSG failure the steam cycle is shut down, reducing the power plant output. Considering that the technology for design, construction and operation of high capacity HRSGs is quite recent its availability should be carefully evaluated in order to foresee the performance of the power plant. This study presents a method for reliability and availability evaluation of HRSGs installed in combined-cycle power plant. The method`s first step consists in the elaboration of the steam generator functional tree and development of failure mode and effects analysis. The next step involves a reliability and availability analysis based on the time to failure and time to repair data recorded during the steam generator operation. The third step, aiming at availability improvement, recommends the fault-tree analysis development to identify components the failure (or combination of failures) of which can cause the HRSG shutdown. Those components maintenance policy can be improved through the use of reliability centered maintenance (RCM) concepts. The method is applied on the analysis of two HRSGs installed in a 500 MW combined-cycle power plant. (C) 2010 Elsevier Ltd. All rights reserved.

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PURPOSE: This study investigated the isolated and combined effects of heat [temperate (22 °C/30 % rH) vs. hot (35 °C/40 % rH)] and hypoxia [sea level (FiO2 0.21) vs. moderate altitude (FiO2 0.15)] on exercise capacity and neuromuscular fatigue characteristics. METHODS: Eleven physically active subjects cycled to exhaustion at constant workload (66 % of the power output associated with their maximal oxygen uptake in temperate conditions) in four different environmental conditions [temperate/sea level (control), hot/sea level (hot), temperate/moderate altitude (hypoxia) and hot/moderate altitude (hot + hypoxia)]. Torque and electromyography (EMG) responses following electrical stimulation of the tibial nerve (plantar-flexion; soleus) were recorded before and 5 min after exercise. RESULTS: Time to exhaustion was reduced (P < 0.05) in hot (-35 ± 15 %) or hypoxia (-36 ± 14 %) compared to control (61 ± 28 min), while hot + hypoxia (-51 ± 20 %) further compromised exercise capacity (P < 0.05). However, the effect of temperature or altitude on end-exercise core temperature (P = 0.089 and P = 0.070, respectively) and rating of perceived exertion (P > 0.05) did not reach significance. Maximal voluntary contraction torque, voluntary activation (twitch interpolation) and peak twitch torque decreased from pre- to post-exercise (-9 ± 1, -4 ± 1 and -6 ± 1 % all trials compounded, respectively; P < 0.05), with no effect of the temperature or altitude. M-wave amplitude and root mean square activity were reduced (P < 0.05) in hot compared to temperate conditions, while normalized maximal EMG activity did not change. Altitude had no effect on any measured parameters. CONCLUSION: Moderate hypoxia in combination with heat stress reduces cycling time to exhaustion without modifying neuromuscular fatigue characteristics. Impaired oxygen delivery or increased cardiovascular strain, increasing relative exercise intensity, may have also contributed to earlier exercise cessation.

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Training and competition in major track-and-field events, and for many team or racquet sports, often require the completion of maximal sprints in hot (>30 °C) ambient conditions. Enhanced short-term (<30 s) power output or single-sprint performance, resulting from transient heat exposure (muscle temperature rise), can be attributed to improved muscle contractility. Under heat stress, elevations in skin/core temperatures are associated with increased cardiovascular and metabolic loads in addition to decreasing voluntary muscle activation; there is also compelling evidence to suggest that large performance decrements occur when repeated-sprint exercise (consisting of brief recovery periods between sprints, usually <60 s) is performed in hot compared with cool conditions. Conversely, poorer intermittent-sprint performance (recovery periods long enough to allow near complete recovery, usually 60-300 s) in hotter conditions is solely observed when exercise induces marked hyperthermia (core temperature >39 °C). Here we also discuss strategies (heat acclimatization, precooling, hydration strategies) employed by "sprint" athletes to mitigate the negative influence of higher environmental temperatures.

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The optimal design of a heat exchanger system is based on given model parameters together with given standard ranges for machine design variables. The goals set for minimizing the Life Cycle Cost (LCC) function which represents the price of the saved energy, for maximizing the momentary heat recovery output with given constraints satisfied and taking into account the uncertainty in the models were successfully done. Nondominated Sorting Genetic Algorithm II (NSGA-II) for the design optimization of a system is presented and implemented inMatlab environment. Markov ChainMonte Carlo (MCMC) methods are also used to take into account the uncertainty in themodels. Results show that the price of saved energy can be optimized. A wet heat exchanger is found to be more efficient and beneficial than a dry heat exchanger even though its construction is expensive (160 EUR/m2) compared to the construction of a dry heat exchanger (50 EUR/m2). It has been found that the longer lifetime weights higher CAPEX and lower OPEX and vice versa, and the effect of the uncertainty in the models has been identified in a simplified case of minimizing the area of a dry heat exchanger.