• 태양에너지
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• 제7권2호
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• pp.22-29
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• 1987

This paper dealed with thickness variation of bottom heat sotrage zone due to salinity and flow rate of extration hot brine in small test solar pond (0.5m wide, 0.5m high, 1.0m long). Testing apparatus and situation were follows: 7.1 cm of height of suction diffuser and 1.8cm of height of discharge diffuser above the test pond respectively, 0.3cm of slot size of suction diffuser, 1.0cm of slot size of discharge diffuser, 47cm of length of the slot; heating of hot water ($75^{\circ}C$) through separated hot water tank, discharge of the brine into storage zone through discharge diffuser, the extration of the brine through suction diffuser, circulation of the extracted brine through a heat exchanger (cooler). Following results were obtained through the experiments. 1. In small test solar pond, the typical three zone which showed up in real solar pond were established. 2. Richardson Number was used more effectively to confirm hydrodynamic stability of the stratified flow. 3. The thickness of non convective layer had a great effect on the heat storage of the bottom convective layer, then the temperature of bottom convective layer had a relation to that of upper convective layer. 4. Optimum operating condition in the test pond was on 10%-15% of salt concentration and $0.05m^3/hr$ of flow rate of extraction hot brine. 5. Following thickness of 3 zones were available to obtain under optimum operation condition: o bottom storage zone: $30%{\pm}10%$ of total pond depth o non-convective zone: $40%{\pm}10%$ of total pond depth o Upper surface zone: $20%{\pm}10%$ of total pond depth.

• 설비공학논문집
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• 제16권5호
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• pp.397-407
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• 2004

It is well known that some key parameters, such as evaporating temperature, refrigerant mass flow rate, face velocity and inlet air temperature, have significant influence on the evaporator performance. However performance studies related to a humid environment have been very scarce. It is demonstrated that the refrigerant mass flow rate, heat flux, water condensing rate and air outlet temperature of the evaporator significantly increase with air inlet relative humidity. As the air inlet relative humidity increases, the latent and total heat transfer rates increase, but the sensible heat transfer rate decreases. The purpose of this study is to provide experimental data on the effect of air inlet relative humidity on the air and refrigerant side pressure drop characteristics for a slit fin-tube heat exchanger. Experiments were carried out under the conditions of inlet refrigerant saturation temperature of 7 $^{\circ}C$ and mass flux varied from 150 to 250 kg/$m^2$s. The condition of air was dry bulb temperature of 27$^{\circ}C$, air Velocity Varied from 0.38 to 1.6 m/s. Experiments Showed that air Velocity decreased 8.7% on 50% of relative humidity 40% of that at degree of superheat of 5$^{\circ}C$, which resulted that pressure drop of air and refrigerant was decreased 20.8 and 8.3% for 50% of relative humidity as compared to 40%, respectively.

• 신재생에너지
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• 제3권4호
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• pp.31-37
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• 2007

Because of their low operating and maintaining costs, ground-source heat pump(GSHP) systems are an increasingly popular choice for providing heating, cooling and water heating to public and commercial buildings. Despite these advantages and the growing awareness, GSHP systems to residential sectors have not been adopted in Korea until recently. A feasibility study of a residential GSHP system was therefore conducted using the traditional life cycle cost(LCC) analysis within the current electricity price framework and potential scenarios of that framework. As a result, when the current residential electricity costs for running the GSHP system are applied, the GSHP system has weak competitiveness to conventional HV AC systems considered. However, when the operating costs are calculated in the modified price frameworks of electricity, the residential GSHP system has the lower LCC than the existing cooling and heating equipments. The calculation results also show that the residential GSHP system has lower annual prime energy consumption and total pollutant emissions than the alternative HVAC systems considered in this work.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 추계학술대회 논문집
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• pp.515-518
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• 2007

Because of their low operating and maintaining costs, ground-source heat pump(GSHP) systems are an increasingly popular choice for providing heating, cooling and water heating to public and commercial buildings. Despite these ad- vantages and the growing awareness, GSHP systems to residential sectors have not been adopted in Korea until recently. A feasibility study of a residential GSHP system was therefore conducted using the traditional life cycle cost(LCC) analysis within the current electricity price framework and potential scenarios of that framework. As a result, when the current residential electricity costs for running the GSHP system are applied, the GSHP system has weak competitiveness to conven- tional HVAC systems considered. However, when the operating costs are calculated in the modified price frameworks of electricity, the residential GSHP system has the lower LCC than the existing cooling and heating equipments. The calculation results also show that the residential GSHP system has lower annual prime energy consumption and total pollutant emissions than the alternative HVAC systems considered in this work.

• 설비공학논문집
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• 제28권3호
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• pp.103-109
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• 2016

The purpose of this study is to perform comparative economic evaluation for the systems of ground source heat pump (GSHP) and district heating and cooling (DHC) by focusing on the analysis of operation case of GSHP. The adapted research object is a public office building located in Seoul. The capacity of ground source pump is about 3,900 kW. Ground heat exchanger is closed loop type. The analysis period for life cycle cost is 30 years. Economic evaluation is assessed from the viewpoints of the following four parts: initial cost, energy cost, maintenance and replacement cost, and environment cost. The total life cycle cost of GSHP is approximately 8,447 million won. The cost of the DHC System is approximately 3,793 million won. The cost of the DHC is approximately 46% lower than GSHP system under the condition of current rate for GSHP and DHC.

• Journal of Mechanical Science and Technology
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• 제17권11호
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• pp.1801-1811
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• 2003

An experimental study was conducted to investigate the effects of air-side fouling and cleaning on the performances of various condenser coils used in unitary air-conditioning systems. A total of six condenser coils with different fin geometry and row number were tested. Performance tests were performed at three different conditions: clean-as-received, after fouling, and after cleaning. In all cases, it was observed that the fouling was mostly confined to the frontal face of the heat exchanger as reported in the previous investigations. The amount of deposited dust was more dependent on fin geometry for the single-row heat exchangers than for the double-row heat exchangers. The predominant effect of fouling was to cause a more significant increase in air-side pressure drop than a degradation in heat transfer performance. For the single-row heat exchangers, the pressure drop increased by 28 to 31%, while the heat transfer performance decreased by 7 to 12% at the standard air face velocity of 1.53 m/s depending on fin shape. For the double-row heat exchangers, the pressure drop increased by 22 to 37%, and heat transfer performance decreased by only 4-5% at the same air face velocity. Once the contaminated coils were cleaned according to the given cleaning procedure the original performance of the heat exchangers could almost be recovered completely. The pressure drop could be restored within 1 to 7% and the heat transfer performance could be recovered to within 1 to 5% of the originally clean heat exchangers. Therefore, it is concluded that a periodic application of the specified cleaning technique will be effective in maintaining the thermal performance of the condenser coils.

• 생물환경조절학회지
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• 제9권4호
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• pp.212-222
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• 2000

본 연구는 온실 난방시스템의 연소 체임버에 부착된 연소가스 배출연통에 열회수기를 장착하여 배출가스로부터 열을 회수하는 열회수장치의 성능에 대해 실험·분석하였다. 열회수시스템은 LPG 연소 체임버와 두 개의 열회수기로 구성되어있다. 열회수기-A는 배기가스 연통에 직접 연결되어 있으며 열회수기-B는 열회수기-A에 직렬로 연결되어 있다. 회수되는 열량은 가스의 질량흐름율과 두 측점간의 엔탈피 차이로서 산정하였으며 5가지의 송풍전압별로 각 열회수기의 성능을 검토하였다. 각 열회수기의 공기튜브 다발에 공급된 공기와 튜브 다발에 가로질로 통과하는 연소가스간의 열교환, 열회수기 유·출입부간의 압력감소, 열회수기의 총열회수성능 등으로 온실의 연통을 통해 낭비되는 열을 회수하여 연료 절감 효과를 얻을 수 있는 최적의 열회수장치 설계용 기초자료 확보에 본 연구의 목적이 있다.

• 한국산학기술학회논문지
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• 제15권7호
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• pp.4047-4051
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• 2014

현대의 공동 주택은 에너지 효율을 높이기 위해 고기밀, 고단열 방식으로 지어지고 있는데 이러할 경우 환기량 부족에 따른 각종 부작용이 발생을 한다. 본 연구에서는 우리나라의 겨울철 대표적인 난방원으로 사용되고 있는 온돌시스템을 기본으로 구성하고 환기방법에 따른 실내 열환경을 평가하여 환기 방식에 따른 에너지 절감 요인을 분석하였다. 실험장치는 일정한 외기 조건을 모사하기 위해 항온항습 챔버에 뜬바닥 온돌 시스템을 설치하고 온돌시스템의 외기온도/습도 조건은 3조건($10^{\circ}C$/50%Rh, $0^{\circ}C$/-, $-10^{\circ}C$,-)으로 설정 하였다. 공급되는 온수온도는 2 조건($60^{\circ}C$, $50^{\circ}C$) 설정하여 설정된 환기 방식에 따라 성능시험을 수행 하여 열 환경 및 에너지 절감 요인을 비교 분석 하였다. 실험결과 급기온도는 온수온도가 높을수록 급기풍량이 적을수록 높았으며 바닥 급/배기 > 전열교환 급/배기 > 강제 급/배기 순으로 나타났다. 본 연구를 통해 다양한 환기 방식의 적용 가능성에 대하여 검토 할 수 있었다.

• 자원환경지질
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• 제40권6호
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• pp.833-841
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• 2007

지하수열펌프시스템(GWHP)은 지원열펌프시스템(GSHP)가운데 성능이 가장 우수하며 저온의 천부지하수열을 이용하는 시스템이다. GWHP시스템은 지중연결 열펌프시스템(GCHP)에 비해 최대 블록부하와 전 시스템 성능에 부합되는 지하수유량을 기준으로 하여 설계를 하며 최적 지하수유량은 해당지역의 지하수온도, 판형열교환기의 규격과 전체펌프와 배관류의 전 양정고에 따라 결정한다. 대체적으로 전형적인 빌딩루프순환수의 필요유량은 1RT당 $9.5{\sim}11.4lpm$ 정도인데 비해 GWHP시스템이 필요로 하는 최적 지하수유량은 이보다 꿜씬 적은 $3.8{\sim}9.5lpm$정도이다.

• Korean Chemical Engineering Research
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• 제61권3호
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• pp.378-387
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• 2023

석유화학은 전체 산업에너지 소비량 중 약 30%를 소비하는 에너지 다소비 업종으로써 대표적인 이산화탄소(carbon dioxide, CO₂) 배출원이다. 그 중 에틸렌, 프로필렌, 프로판 및 혼합 C4를 생산하는 납사 분해 공정(naphtha cracking center, NCC)은 많은 양의 에너지를 소비하고 상당한 양의 CO₂를 배출한다. 이러한 이유로 경제성과 환경적 측면에서의 효율성을 보장하기 위해 에너지 사용량 및 환경 영향 인자 감소를 목표로 하는 통합 기술경제적-환경영향 평가가 필요하다. 본 연구는 핀치분석에 근거하여 기존 NCC에서 사용되는 열 교환망의 효율성을 분석하고 이를 통해 에너지 사용량을 감축 시킬 수 있는 개선안을 선정하는 것을 목표로 한다. 공정 내 유틸리티 소비량을 줄이기 위하여 고온 스트림과 저온 스트림 사이를 고려한 최적의 열 교환망을 도출하고, 유틸리티 사용량 감소와 열교환기 설치 비용 증가 사이의 트레이드 오프를 고려하여 경제성 평가를 진행하였다. 또한, 환경적 측면을 고려하여 감소된 CO₂ 배출에 대한 환경영향평가를 실시하였고, 경제적-환경 영향 평가는 투자된 자금을 회수하는 회수기간을 사용하여 실제 공정을 바탕으로 적용 가능성이 있는 에너지 절감안을 도출하였다. 경제적-환경영향평가를 고려한 결과 경제성만을 고려한 부분에서는 각 사례별로 4.29개월, 3.21개월, 3.39개월로 나타났고, 경제적-환경 통합 평가의 경우에는 각 사 례별로 4.24개월, 3.17개월, 3.35개월로 각각의 회수기간을 보였다. 이러한 결과는 환경영향평가를 포함하지 않았을 때와 포함하였을 때 모두 동등하게 나타났다. 추가로 주요한 요소가 회수기간에 어느정도 영향을 미치는지 확인하기 위해 각 사례별 민감도 분석을 진행하였다. 민감도 분석결과 열 교환기 비용이 전체적인 비용에 영향을 미치는 주요 원인으로 확인되었다.