• 제목/요약/키워드: Heat exchange area

검색결과 100건 처리시간 0.027초

건축외부공간에 있어서 인체의 일사열부하(日射熱負荷) 및 열적(熱的) 쾌적성(快適性)에 관한 실험적 연구 (Human Solar Heat Load and Thermal Comfort in an Outdoor Environment)

  • 정창원;윤인
    • 한국산업융합학회 논문집
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    • 제1권2호
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    • pp.65-74
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    • 1998
  • The purpose of this paper is to investigate the mount of relief of human solar heat load and thermal comfort in outdoor environment in summer, Six different types of sites, T garden and its neighboring area in Japan, were selected as the experiment sites. The experiments were conducted from 22 to 29 August, 1994 to find the relationship between climatic conditions and human responses, Climatic conditions, subjects's thermal sensation and skin temperature were measured. Radiant heat exchange on the human body was estimated on the basis of the measured air and surface temperature and solar radiation. Thermal index Operative Temperature and New Effective Temperature was modified with the effect of the radiant heat exchange. Human thermal comfort and skin temperature is affected by the solar radiation and the sky factor in an outdoor environment. The effect of tree shade was verified on thermal comfort, The mount of relief of human solar heat load is relation to the existence of shade a solar radiation and the sky factor. The urban garden is one of the effective design element in an urban environmental planning.

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Wilson plot법을 이용한 Plate & Shell 열교환기의 단상유동 열전달 특성에 관한 실험적 연구 (Experimental Study on Heat Transfer Characteristics for Single-phase Flow in Plate & Shell Heat Exchangers by Using Wilson Plot Method)

  • 서무교;김영수;이상경
    • 동력기계공학회지
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    • 제3권4호
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    • pp.22-27
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    • 1999
  • Single phase heat transfer coefficients were measured for turbulent water flow in a plate & shell heat exchangers by using Wilson plot method. An experiment for counterflow heat exchange between the plate and shell was performed. The shell side heat transfer resistance was varied and the overall heat transfer coefficients were measured. The single-phase heat transfer coefficients in a plate side were obtained by Wilson plot method. Single-phase heat transfer correlations based on projected heat transfer area have been proposed for a plate & shell heat exchanger.

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핀 튜브 열교환기와 알루미늄 열교환기의 성능 비교 (Performance Comparison of Fin-Tube Heat Exchanger and Aluminum Heat Exchanger)

  • 장근선;이현수;김재덕;홍석률
    • 대한설비공학회:학술대회논문집
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    • 대한설비공학회 2008년도 하계학술발표대회 논문집
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    • pp.408-413
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    • 2008
  • This study presents comparison of the air side heat transfer and friction characteristics in a heating condition between Louver fin-tube heat exchangers and aluminum heat exchangers. Experiments are performed for the Louver fin-tube heat exchangers and aluminum heat exchangers using a calorimeter, which is designed based on air-enthalpy method described in ASHRAE standards. The air velocities its are varied from 0.7 to 1.6 m/s with 0.3 m/s interval. A study result shows that the heat transfer performances of aluminum heat exchangers are $40{\sim}80%$ higher than those of Louver fin-tube heat exchangers per unit volume, mass and heat transfer area.

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산화알루미늄의 치환에 따른 붕규산 유리의 분상 미 이온교환성에 관한 연구 (Ion Exchange Capacity and Phase Separation of Alkali Borosilicate Glass by Substituting $Al_2O_3$)

  • 김병호;유영문
    • 한국세라믹학회지
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    • 제21권1호
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    • pp.41-50
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    • 1984
  • The ion-exchange porous glasses were prepared by heat treating and subsequently acid treating the (95-y) $SiO_2$.$yB_2O_3$.$5Na_2O+xAl_2O_3$ glasses with y=55, 45, 35, 25. mole% and x=0, 2, 5, 9 mole% It was then investigated how the cation exchange capacity was affected by the phase separation in these glasses. For that matter such quantities as alkali extraction amount pore volume and specific surface area of the glasses were measured. The phase separation in these glasses was in general suppressed by the addition of $Al_2O_3$ maximally around the composition of 5 mole% $Al_2O_3$ This may be because the micro-phase separation prevailed in the glass of that composition over the macro-phase separation increasing thereby the specific surface area as well as the residual amount Al of after acid-treatment and accordingly the cation exchange capacity. The maximum values of the cation exchange capacity was observed to be about 150meq/100g for the glasses of (40-50) $SiO_2$ (55~45)$yB_2O_3$. $5Na_2O+5Al_2O_3$.

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EXHAUST GAS HEAT RECOVERY SYSTEM FOR PLANT BED HEATING IN GREENHOUSE PRODUCTION

  • Kim, Y.J.;Ryou, Y.S.;Rhee, K.J.;Kang, G.C.
    • 한국농업기계학회:학술대회논문집
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    • 한국농업기계학회 2000년도 THE THIRD INTERNATIONAL CONFERENCE ON AGRICULTURAL MACHINERY ENGINEERING. V.III
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    • pp.639-646
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    • 2000
  • Hot air heater with light oil combustion is the most common heater for greenhouse heating in the winter season in Korea. However, since the heat efficiency of the heater is about 80%, considerable unused heat in the form of exhaust gas heat discharges to atmosphere. In order to capture this exhaust gas heat a heat recovery system for plant bed heating in the greenhouse was built and tested in the hot air heating system of greenhouse. The system consists of a heat exchanger made of copper pipes, ${\phi}\;12.7{\times}0.7t$ located inside the rectangular column of $330{\times}330{\times}900mm$, a water circulation pump, circulation plastic pipe and a water tame The total heat exchanger area is $1.5m^2$, calculated considering the heat exchange amount between flue gas and water circulated in the copper pipes. The system was attached to the exhaust gas path. The heat recovery system was designed as to even recapture the latent heat of flue gas when exposing to low temperature water in the heat exchanger. According to performance test it can recover 45,200 to 51,000kJ/hr depending on the water circulation rates of 330 to $690{\ell}$/hr from the waste heat discharged. The exhaust gas temperature left from the heat exchanger dropped to $100^{circ}C$ from $270^{circ}C$ by the heat exchange between the water and the flue gas, while water gained the difference and temperature increased to $38^{circ}C$ from $21^{circ}C$ at the water flow rate of $690{\ell}$/hr. And, the condensed water amount varies from 16 to $43m{\ell}$ at the same water circulation rates. This condensing heat recovery system can reduce boiler fuel consumption amount in a day by 34% according to the feasibility study of the actual mimitomato greenhouse. No combustion load was observed in the hot air heater.

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Performance of A Three-Stage Condensation Heat Pump

  • Lee, Yoon-Hak;Jung, Dong-Soo;Kim, Chong-Bo
    • International Journal of Air-Conditioning and Refrigeration
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    • 제7권
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    • pp.55-68
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    • 1999
  • In this study, computer simulation programs were developed for single-stage, two-stage, and three-stage condensation heat pumps and their performance with CFC11, HCFC123, HCFC141b was examined under the same external conditions. The results showed that the coefficient of performance(COP) of an optimized 'non-split type' three-stage condensation heat pump is 25-42% higher than that of a conventional single-stage heat pump. The increase in COP, however, differed among the fluids tested. The improvement in COP is largely due to the decrease in average LMTDs in condensers, which results in the decrease in thermodynamic irreversibility in heat exchange process. For the three-stage heat pump, the highest COP is achieved when the total condenser area is evenly distributed among the three condensers. For the two-stage heat pump, however, the optimum distribution of the total condenser area varies with an individual working fluid. For the three-stage system, 'splitting the condenser cooling water'for the use of intermediate and high pressure subcoolers helps increase the COP further. When the individual cooling water entering the intermediate and high pressure subcoolers is roughly 10% of the total condenser cooling water, the maximum COP is achieved showing roughly an 11% increase in COP as compared to that of the 'non-split type' heat pump.

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2013년 부산지역 폭염사례일의 열쾌적성 평가 (Evaluation of Thermal Environments during the Heat Waves of Summer 2013 in Busan Metropolitan Area)

  • 김영준;김현수;김유근;김진국;김연매
    • 한국환경과학회지
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    • 제23권11호
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    • pp.1929-1941
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    • 2014
  • Now a days, frequency of abnormally high temperatures like heat wave by global warming and climate change is increasing constantly and the number of patient with heat related illness are jumping rapidly. In this study, we chose the case day for the heat wave in Busan area(Busan and Yangsan), 2013 which it was the most hottest year during 21th century. And then, we analysed the weather condition using automatic synoptic observing system(ASOS) data. Also, four indices, heat index(HI), wet bulb globe temperature(WBGT), Man-ENvironment heat EXchange model(MENEX)'s results like Physiological subjective temperature(PST), Physiological strain(PhS), were calculated to evaluate the thermal comfort and stress quantitatively. However, thermal comfort was different as the each station and thermal comfort index during same time. Busan's thermal indices (HI: hot, WBGT: sweltering, PST: very hot, PhS: very hot) indicated relatively higher than Yansan's (HI: very hot, WBGT: sweltering, PST: very hot, PhS: sweltering). It shows that Busan near coast is relatively more comfortable than Yangsan located in inland.

온실 난방부하 산정방법의 검증 및 틈새환기와 지중전열의 영향 분석 (Validation of Load Calculation Method for Greenhouse Heating Design and Analysis of the Influence of Infiltration Loss and Ground Heat Exchange)

  • 신현호;남상운
    • 원예과학기술지
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    • 제33권5호
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    • pp.647-657
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    • 2015
  • 원예시설의 환경설계 중 난방부하 산정방법에 대한 검증을 위하여, 대규모 플라스틱 온실에서 총난방부하와 틈새환기율, 지중전열량을 계측하여 계산결과와 비교 분석하였고, 지중전열 및 틈새환기가 온실의 난방부하에 미치는 영향을 검토하였다. 실험기간 동안 실내기온은 $13.3{\pm}1.2^{\circ}C$, 실외 기온은 $-9.4{\sim}+7.2^{\circ}C$의 범위를 보였으며, 우리나라의 난방 설계 외기온 범위에서 유효한 것으로 확인하였다. 가스트레이서법으로 측정한 틈새환기율은 평균 $0.245h^{-1}$로 나타났다. 온실의 피복면적에 일정한 환기전열계수값을 사용하는 방법은 온실의 규모에 따라서 문제가 있는 것으로 분석되었다. 따라서 환기전열부하는 온실의 체적과 틈새환기율을 이용하는 방법이 합리적인 것으로 판단된다. 온실 중앙에서 측정한 지중열류는 실내외 기온차에 따라 음으로 약간 증가하는 경향을 보이고, 온실 측면에서 측정한 지중열류는 실내외 기온차에 따라 양으로 크게 증가하는 경향을 보였다. 계측 결과를 바탕으로 온실의 외주부를 통한 열손실 개념을 도입한 새로운 지중전열부하 산정 방법을 개발하였으며, 검증결과 잘 일치하는 것으로 나타났다. 관류열부하는 대체로 실내외 기온차에 비례하는 것으로 나타났으나, 열관류율은 작아지는 경향을 보였다. 따라서 관류열부하 산정시 설계조건에 따라 열관류율의 선택에 주의를 기울여야 할 것으로 판단된다. 실험온실의 열관류율은 평균 $2.73W{\cdot}m^{-2}{\cdot}C^{-1}$로 단일피복의 플라스틱 온실 대비 60%의 열절감율을 보이는 것으로 나타났다. 전체 난방부하 중에서 관류열부하가 84.7~95.4%, 환기전열부하가 4.4~9.5%, 지중전열부하가 -0.2~+6.3%를 차지하는 것으로 나타났다. 관류열부하는 실내외 기온차가 낮은 그룹에서 더 큰 비율을 차지하고, 환기전열 부하는 실내외 기온차가 높은 그룹에서 더 큰 비율을 차지하는 것으로 나타났다. 지중전열부하의 경우 실내외 기온차가 낮은 그룹에서는 부하를 경감시키는 방향으로 작용하고, 실내외 기온차에 따라 부하를 증가시키거나 경감시키는 방향으로 작용하는 것으로 나타났으므로 이 기준 온도차의 선택이 중요한 것으로 판단된다. 지중전열부하에 비하여는 환기전열부하가 더 큰 비중을 차지하므로 에너지 절감을 위해서는 틈새환기율을 줄일 수 있는 대책이 필요한 것으로 판단된다.

자연대류형 태양열온수기의 특성별 성능평가에 관한 연구 (Performance Ratings According to Characteristics of Thermosyphon Solar Hot Water System)

  • 강용혁;곽희열;유창균;윤환기;강명철;이동규
    • 태양에너지
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    • 제20권2호
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    • pp.9-17
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    • 2000
  • To obtain thermal performance data, an experiment was performed with the two selected thermosyphon systems. The system parameters obtained by experimental data were used to perform TRNSYS simulation and verified TRNSYS model of thermosyphon solar hot water system. The thermosyphon solar hot water system was TYPE 145 which is modified from non-linear model. This model can describe heat exchange type and non-linear efficiency equation. It is possible to analyze the annual energy rate with efficiency equation and system specification. In this paper, we could compare the annual performance of the coil heat exchanger with that of the tank-in-tank heat exchanger. Under the same efficiency and parameter, heat exchange, drain, initial tank temperature, ratio of tank volume over collector area(V/Ac), regional annual performance rating were performed.

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광합성과 증발산의 미기상학적 측정기술 (Technique for Estimating $CO_2$ and $H_2O$ Exchange between the Atmosphere and the Biosphere : Eddy Covariance Method)

  • Wonsik Kim
    • 한국농림기상학회:학술대회논문집
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    • 한국농림기상학회 2003년도 춘계 학술발표논문집
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    • pp.115-128
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    • 2003
  • o What is the flux \ulcorner Flux is the transfer of a quantity per unit area per unit time. The quantities are mass, heat, moisture, momentum and pollutant in micrometeorology. Kinematic flux (Fluid). The reduction in wind speed due to frictional drag transfers momentum from the atmosphere to the surface, creating turbulence that mixes the air and transports heat and water from the surface into the lower atmosphere. (omitted)

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