• 대한설비공학회지:설비저널
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• 제16권2호
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• pp.176-184
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• 1987

The purpose of this research is to study the characteristics of the coefficient of perform-ance (COP) of the small absorption refrigeration system. This experimental study is performed with two selected variables, the temperature of the generator and the input temperature of the cooling water. In order to determine the input temperature of the generator which gives maximum COP, the experimental data are obtained with controlling the temperature of the generator in the range of $20-32^{\circ}C$ of the temperature of the cooling water. The range of the generator heat suppling temperature which gives maximum efficiency is about $90-95^{\circ}C.$ The temperature range depends on the characteristics of the equipment unit. The most important result in this experiment is the trends of the COP in accordance with the variation of these temperatures. This trend will furnish the informations and knowledges for designing and operating the absorption refrigerator.

• Journal of Advanced Marine Engineering and Technology
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• 제40권4호
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• pp.282-287
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• 2016

최근 조선사들은 선박이 운항되는 연안 환경의 개선과 보호를 위하여 $CO_2$를 절감할 수 있는 친환경 선박과 함께 선박 운항 중 소비하는 에너지의 절감을 위한 고효율화 선박 개발의 노력도 활발하게 수행하고 있다. 본 연구에서는 전기로 구동되는 선박의 증기압축식 냉동기 대신에 선박 엔진 자켓수의 폐열을 이용하여 냉방을 할 수 있는 흡수식 냉동기의 적용 가능성과 냉각시스템에 냉매를 적용하는 시스템의 성능을 분석하였다. 연구결과, 해수와 열교환하여 액화될 수 있는 냉매들 중 R236fa가 가장 적합한 냉매로 분석되었으며, 이를 적용한 흡수식 냉동기의 COP는 0.798로 육상의 냉각탑을 이용한 수랭식보다 15% 그리고 해수 열교환기식 수랭식보다 5% 향상되었다. 냉동능력 1RT를 얻기 위한 LiBr 흡수용액 순환량은 0.013 kg/s로 수랭식 보다 25% 이상 감소하며, 냉각 매체 순환량도 수랭식의 15.7%에 불과한 매우 효과적인 냉동기가 되었다. 해수온도가 $18^{\circ}C$ 이하로 낮으면 발생하게 되는 LiBr의 결정화는 재생기에서 배출되는 엔진 자켓수의 온도를 이용하여 해수 온도를 상승시킴으로써 방지할 수 있다.

• 태양에너지
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• 제15권3호
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• pp.75-90
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• 1995

본 논문은 가정용 냉방기에 널리 사용되고 있는 HCFC22를 대체할 수 있는 혼합냉매의 개발 및 이들의 성능 연구에 관한 것이다. 현재까지 HCFC22를 대체할 수 있는 순수냉매가 없으므로, 혼합냉매 개발에 본 연구의 초점이 맞추어졌고, 이를 위해 가정용 냉방기를 모사 하는 컴퓨터 프로그램이 개발되었다. 연구에서 개발된 혼합냉매를 구성하는 순수냉매들은 다음과 같다: R32, R124, R125, R134, R134a, R143a, R152a. 컴퓨터 모사 결과들은 다음의 혼합냉매들에 대해서 발표되었다: R32/R134a, R32/R152a, R32/R134, R32/R124, R143a/R134a, R143a/R152a, R143a/R124, R125/R134a, R125/R152a, R125/R124, R32/R152a/R134a, R32/R152a/R134, R32/R152a/R124. 가장 좋은 에너지 효율을 보인 것은 삼원 혼합냉매인 R32/R152a/R124로서, HCFC22에 비해 이것의 성적 계수는 13.7% 높고 냉동 능력은 23% 낮은 것으로 판명되었다. 한편 이원 혼합냉매 중 가장 성능이 좋은 것은 R32/R124로서 이것의 성적 계수는 HCFC22에 비해 13.4% 높고 냉동 체적 용량은 9.6% 낮은 것으로 판명되었다.

• 한국산학기술학회논문지
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• 제18권10호
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• pp.8-14
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• 2017

최근 들어 국민 식생활 문화가 개선되고 생활수준이 향상됨에 따라 소프트 아이스크림, 슬러시와 같은 일회용 냉동 유제품의 소비가 급증하고 있다. 이들 냉동 유제품은 소형 냉동 시스템에서 만들어진다. 소프트 아이스크림 제조기의 경우 냉각기는 동심 원통으로 구성되며 냉매는 환형부에서 증발하고 냉각기 표면에 형성된 얼음 결정이 내측에서 회전하는 스크레이퍼에 의해 빙삭되어 아이스크림이 만들어진다. 본 연구에서는 냉각기 체적 2.8 리터인 R-404A를 사용하는 소프트 아이스크림 제조기에 대하여 최적화와 성능평가를 수행하였다. 최적화는 냉각기 스크레이퍼 회전수 및 냉매 유로 개선에 주안점을 두고 실제 아이스크림 제조기에서 요소 부위의 온도와 압력 그리고 소비동력을 측정함으로써 수행되었다. 실험 결과 최적 회전수는 124 rpm으로 나타났다. 이 회전수에서 아이스크림 제조 시간은 6분 2초이고 이 때 성적계수는 0.90이었다. 또한 물-공기를 사용한 가시화 실험을 통하여 냉매측 유로 개선을 시도하였다. 유로가 개선된 제품은 아이스크림 제조 시간을 현저히 감소시켰다. 본 연구 결과는 냉동식품 제조기를 비롯한 여타 냉동 사이클의 최적화에도 활용될 수 있을 것이다.

• 설비공학논문집
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• 제7권2호
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• pp.234-248
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• 1995

A super-heat pump system composed of a suction line heat exchanger, low and high stage economizers, and a screw compressor is simulated to examine the energy performance and design options. CFC12, HCFC22, HFC134a, HCFC22/HCFC142b, HFC32/HFC134a, and HFC125/HFC134a are used as working fluids for comparison. The results indicate that the proposed system charged with appropriate mixtures is up to 33.4% more energy efficient than the normal system with CFC12. The performance of the super-heat pump system charged with mixtures was influenced by such factors as the temperature matching, heat source temperature difference, low stage economizer, and high stage economizer. The fluids with a larger liquid specific heat such as HFC134a would have more benefits when a suction line heat exchanger is installed. 40%HCFC22/60%HCFC142b mixture seems to be a good candidate to replace CFC12. On the other hand, 25%HFC32/75% HFC134a would be a good long term candidate to replace HCFC22.

• 대한기계학회논문집
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• 제19권8호
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• pp.2012-2021
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• 1995

An experimental study was performed for the analysis of dynamic characteristics of refrigeration system by controlling the evaporator superheat. Experimental data have been taken utilizing two different devices, thermostatic expansion valve(T.E.V.) and electronic expansion valve(E.E.V.), for the control of the evaporator superheat. The ranges of parameters, such as superheat, mass flow rate of refrigerant and inlet temperature of evaporator were 5-30.deg. C 90-170 kg/h and 10-25.deg. C, respectively. The data taken from the T.E.v.and E.E.v.were discussed with the control of the superheat, pressure drop, refrigerating capacity, compression work, evaporating temperature, condensing temperature and COP affecting performance characteristics of refrigeration system. In case of the refrigerant flow control with T.E..V., the superheat and pressure drop of the evaporator varied periodically, but the control with E.E.V., the parameters were very stable. In E.E.v.control, refrigerating capacity, compression work and evaporating temperature were decreased with increasing superheat, and the highest COP was obtained in the range of superheat from 5.deg. C to 15.deg. C.

• 한국수소및신에너지학회논문집
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• 제27권4호
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• pp.462-469
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• 2016

This paper presents the results of thermodynamic cycle analysis and performance tests of alternative mixtures in low temperature applications. Two near-azeotropic binary mixtures R-152a/R-1270 (35:65 by wt.%) and R-290/E170 (35:65 by wt.%) are considered in this study. They have zero ODP (Ozone Depletion Potential) and much lower GWP (Global Warming Potential) than R-404A which is an alternative of R-502. Refrigeration cycle characteristics such as cooling capacity, coefficient of performance, suction and discharge pressures and temperatures are compared to those for the baseline refrigerants (R-502 and R-404A) cycles. The performance tests are conducted at the evaporation and condensation temperatures of $5^{\circ}C$ and $45^{\circ}C$, subcooling and superheating temperatures of $5^{\circ}C$, respectively. Performance comparisons between baseline and alternative refrigerants are conducted on the same cooling capacity. The system performance of newly proposed refrigerant mixtures show promising results.

• 한국유체기계학회 논문집
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• 제18권3호
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• pp.12-19
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• 2015

As a means of improving cycle performance of a R410A air-conditioning system, a combined structure of compressor and expander was introduced. A vane rotary type expander was designed to share a common shaft with twin type rolling piston rotary compressor in a housing. Numerical simulation on the performance of the combined compressor and expander was carried out. At ARI condition, the volumetric and total efficiencies of the designed vane expander were 69.37% and 30.23%, respectively. With the application of this expander, the compressor input was reduced by 3.91%, and the cooling capacity was increased by 3.98%. As a result, COP of the air-conditioning system was improved by 8.2%. As the pressure difference between the condenser and the evaporator becomes large, COP improvement increases unless the mass flow rate in the expander exceeds that in the compressor.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2004년도 춘계학술대회
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• pp.2129-2134
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• 2004

The present study has been conducted to develop a heat pump system using river water of temperature energy which not only belongs to unutilized energy but is a kind of good heat source due to maintain its temperature in a certain degree regardless of seasonal variation. The system did not meet the proposed performance after setup. In this paper, the system performance affected by refrigerant Oil, by pressure drop, or by other factors has been discussed. The followings were obtained : (1) Refrigerant Oil mixture rate was 2.5 in weight percentage, (2) Pressure drop through evaporator was 29.1kPa($3.1^{\circ}C$ in saturated tempearture) (3) Pressure drop from the end of evaporator to compressor inlet was 39.8kPa($4.0^{\circ}C$ in saturated tempearture). (4) The system performance can to be improved by modifying a part of pipe line to compressor, and reducing pressure drop through heat exchangers.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2006년도 하계학술발표대회 논문집
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• pp.46-51
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• 2006

In order to utilize the refrigerants condensation heat of condenser on the absorption chiller system, the solution cooling condenser(SCC) were proposed, which weak solution of absorber outlet use as a cooling water. As the UA of the solution cooling condenser increased, increasement of COP is about maximum 0.09 in occasion of single effect and is about maximum 0.08 in occasion of double effect series flow. In the case of heat exchanger efficiency is about 0.85, it's increments are 0.08 and 0.072, each. And solution cooling condenser is a more effective device in the single effect absorption system more than double effect system for the principle of operation. In order to increases the heat of solution cooling condenser, if reduce the flow rate of cooling water or the value of UA, it makes COP increase a little, but it brought COP decrease because of increasing the pressure of system.