• 한국산학기술학회논문지
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• 제13권4호
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• pp.1427-1433
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• 2012

본 연구에서는 이원냉동시스템에서 사용되던 저온용 규제프레온냉매 R13 및 고온용 규제프레온냉매 R503의 대체냉매로서 프레온혼합냉매 및 친환경적 자연냉매를 사용하는 이원냉동시스템의 성능특성을 규명하고자 하였다. 이를 위해 일반적인 이원냉동시스템의 운전범위에서 과냉각도, 과열도, 응축온도, 증발온도, 캐스케이드 열교환기에서의 온도변화를 고려하였다. 고온시스템 및 저온시스템의 작동유체의 종류에 상관없이 이원냉동시스템의 COP는 캐스케이드의 온도영향을 받고 있으며, 또한 과냉각도가 증가할수록 COP는 높아지지만, 과열도의 영향은 크게 받지 않았다. 따라서 본 연구에서 고온용 시스템 및 저온용 시스템의 작동유체로 대체 프레온혼합냉매 및 자연냉매의 냉매조합 중에서 (R23/R290), (R23/R600), (R23/R600a), (R23/R717), (R744/R404A) 냉매를 사용하는 이원냉동시스템의 COP는 저온측에 R23, 고온측에 R22를 사용하는 시스템에 비해 20 ~ 36% 높게 나타났다.

• 설비공학논문집
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• 제12권12호
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• pp.1049-1056
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• 2000

In this study, condensation heat transfer coefficients(HTCs) of 2 nonazeotropic refrigerant mixtures of HFC32/HFC134a and HFC134a/HCFC123 at various compositions were measured on a horizontal smooth tube. All data were taken at the vapor temperature of 39$^{\circ}C$ with a wall subcooling of 3~8K. Test results showed that HTCs of tested mixtures were 11.0~85.0% lower than the ideal values calculated by the mass fraction weighting of the pure components HTCs. Thermal resistance due to the diffusion vapor film was partly responsible for the significant reduction of HTCs with these nonazeotropic mixtures. The measured data were compared against the predicted ones by Colburn and Drew\`s film model and a good agreement was observed.

• 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.

• 설비공학논문집
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• 제14권2호
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• pp.161-167
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• 2002

In this study, external condensation heat transfer coefficients (HTCs) of two non-azeotropic refrigerant mixtures of HFC32/HFC134a and HF0134a/HCF0123 at various compositions were measured on both low fin and Turbo-C enhanced tubes of 19.0 mm outside diameter All data were taken at the vapor temperature of 39$^{\circ}C$ with a wall subcooling of 3- 8 K. Test results showed that HTCs of the tested mixtures on the enhanced tubes were much lower than the ideal values calculated by the mass fraction weighting of the pure compo- nents'HTCs. Also the reduction of HTCs due to the diffusion vapor film was much larger than that of a plain tube. Unlike HTCs of pure fluids, HTCs of the mixtures measured on enhanced tubes increased as the wall subcooling increased, which was due to the sudden break up of the vapor diffusion film with an increase in wall subcooling. Finally, heat transfer enhancement ratios for mixtures were found to be much lower than those of pure fluids.

• 설비공학논문집
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• 제25권9호
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• pp.484-492
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• 2013

Nucleate pool boiling heat transfer coefficients (HTCs) are measured with HFC32/HFC152a mixture at several compositions. All data are taken at the liquid pool temperature of $7^{\circ}C$, on a horizontal plain square surface of $9.53{\times}9.53$ mm, with heat fluxes of 10 $kW/m^2$ to 100 $kW/m^2$ with an interval of 10 $kW/m^2$, in the increasing order of heat flux. Test results show that the HTCs of these mixtures are up to 45% lower than those of the ideal HTCs calculated by a linear mixing rule with pure fluids' HTCs, due to the mass transfer resistance associated with non-azeotropic refrigerant mixtures. Pool boiling data show the deduction in HTCs with an increase in GTD of the mixture. The present mixture data agree well with five well known correlations, within 20% deviation.

• 설비공학논문집
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• 제18권12호
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• pp.955-963
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• 2006

Nucleate pool boiling heat transfer coefficients (HTCs) were measured with one nonazeotropic mixture of Propane/Isobutane and two azeotropic mixtures of HFC134a/Isobutane and Propane/HFC134a. All data were taken at the liquid pool temperature of $7^{\circ}C$ on a horizontal plain tube with heat fluxes of $10kW/m^2\;to\;80kW/m^2$ with an interval of $10kW/m^2$ in the decreasing order of heat flux. The measurements were made through electrical heating by a cartridge heater. The nonazeotropic mixture of Propane/Isobutane showed a reduction of HTCs as much as 41% from the ideal values. The azeotropic mixtures of HFC134a/Isobutane and Propane/HFC134a showed a reduction of HTCs as much as 44% from the ideal values at compositions other than azeotropic compositions. At azeotropic compositions, however, the HTCs were even higher than the ideal values due to the increase in the vapor pressure. For all mixtures, the reduction in heat transfer was greater with a larger gliding temperature difference. Stephan and $K{\ddot{o}}rner's$ and Jung et al's correlations predicted the HTCs of mixtures with a mean deviation of 11%. The largest mean deviation occurred at the azeotropic compositions of HFC134a/Isobutane and Propane/HFC134a.