• Journal of Advanced Marine Engineering and Technology
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• 제17권3호
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• pp.24-32
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• 1993

Experimental data on the heat transfer characteristics of HCFC-123 and CFC-11 during condensation in horizontal smooth tube are presented. The experimental apparatus consisted of a closed working fluid loop, coolant loop, and measuring system. The major components of the working fluid loop made of a refrigerant pump, boiler, superheater, refrigerant flow meter, receiver and test section. The tube-in-tube type test section was made of smooth tube which were constructed form 9.52 mm outer diameter of smooth copper tube with 50 mm outside diameter of PVC tube duct. The ranges of parameter, such as refrigerant mass velocity, coolant flow rate, and quality were 90-325kg/($m^2$.s), 60-360kg/h, 5-95% respectively. Data were obtained under steady state condition for annular flow. As a result of these, the condensation heat transfer coefficients for HCFC-123 were slightly lower than those of CFC-11 from 8% to 15% inside horizontal smooth tube. Furthermore, a new generalized correlation for the heat transfer coefficients of HCFC-123 and CFC-11 during condensation inside horizontal smooth tube is proposed.

• 한국대기환경학회지
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• 제26권5호
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• pp.490-498
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• 2010

HCFC-22 (chlorodifluoromethane, $CHClF_2$), one of the major components in various refrigeration, is emitted mostly from developing countries, as its consumption is not limited until 2013 by the Montreal Protocol. In addition, HFC-23 (trifluoromethane, $CHF_3$), a by-product in the manufacture of HCFC-22, is also a powerful greenhouse gas. Here, we discuss the regional emission characteristics of these compounds based on high-frequency in-situ measurements using the "Medusa" GC-MS system. HCFC-22 and HFC-23 baseline concentrations measured at Gosan (Jeju Island, Korea) from November 2007 to December 2008 increased by 1.8 ppt/yr and 0.6 ppt/yr, respectively. Pollution events of these compounds were observed, very frequently (e.g., ~2~3 times) at Gosan than baseline levels. All the measurement data were divided into four groups by simultaneously considering the ratio (HFC-23/HCFC-22) and concentration (HCFC-22) at Trinidad Head (TH, California, USA). The residence time of trajectories were then analyzed in each of the four groups. The results exhibited the existence of a strong correlation with air mass origin for each group: 1) Air masses originating from Siberia in the north and from the Pacific in the south had ratios of 0.08~0.12 and concentrations of 196.9~254.3 ppt which is highly comparable to background air at TH. 2) Air masses passing over the Southern China exhibited similar ratios but higher HCFC-22 concentrations. 3) Air masses passing over the Northern China had ratios of 0.12~0.21. 4) Air masses passing over Korea and/or Japan had ratios of 0.01~0.08. Our results suggest that the HFC-23/HCFC-22 ratio can be used as a good indicator for the assessment of the pollution with Chinese origin. We also confirmed differences in air masses traveling over Northern and Southern China, most likely due to differences in air mass travelling speed over these regions before arriving at Gosan. This signature may be treated as one of the critical components in identifying the emission sources from different parts of China.

• 설비공학논문집
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• 제24권5호
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• pp.391-400
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• 2012

In this study, performance of HFC32/HFC152a mixture is measured in the composition range of 20 to 50% R32 with an interval of 10% for the comparison with the conventional HCFC22 in water-source heat pumps. Tests are carried out under the same capacity in a heat pump bench tester equipped with a variable speed compressor at the evaporation and condensation temperatures of 7/$45^{\circ}C$ and -7/$41^{\circ}C$ for summer and winter conditions, respectively. Test results show that the compressor power of the HFC32/HFC152a mixture is 13.7% lower than that of HCFC22 while the coefficient of performance(COP) the HFC32/HFC152a mixture is 15.8% higher than that of HCFC22. Hence, from the view point of energy efficiency, the HFC32/HFC152a mixture is excellent as compared to HCFC22. Compressor discharge temperatures of HFC32/HFC152a mixture are increased up to $15.4^{\circ}C$ as compared to that of HCFC22. The amount of charge for HFC32/HFC152 mixture decrease up to 27% as compared to that of HCFC22. Overall, HFC32/ HFC152a mixture is an excellent long term candidate to replace HCFC22 in water-source heat pumps.

• 기술표준
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• 통권1호
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• pp.64-68
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• 2002

• 설비공학논문집
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• 제15권5호
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• pp.389-396
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• 2003

Systematic methods to calculate thermodynamic properties of carbon dioxide, HFC-l34a and HCFC-22 are presented. First, application of a basic method to identify the saturation state with given temperature or pressure is attempted and the feasibility of auxiliary equations is tested. Next, detailed procedures are suggested to tell a phase when temperature/pressure and another property are specified. Finally Newton-Raphson method is applied to calculate unknown thermodynamic properties fixing the state with the two independent properties specified. The procedures described here are utilized to develop a computer program, which is used to find the relation between temperature and pressure with maximum isobaric heat capacity for super-critical carbon dioxide.

• 에너지공학
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• 제10권4호
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• pp.318-326
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• 2001

중저온 배열회수를 통해 열설비의 열효율을 향상시키기 위하여 1 MW급 유기랭킨사이클시스템을 설계, 개발하였다. 포항제철소에 있는 두 대의 100 MW급 기력발전소에서 발생하는 175$^{\circ}C$의 배가스를 산업체에서 발생하는 대표적인 중저온배열원으로 선정하고, 환경오염을 최소화할 수 있는 신냉매인 HCFC-123을 시스템의 작동유체로 선정하였다. 유기냉킨사이클시스템의 시험운전을 통하여 유기랭킨사이클시스템이 산업체의 중저온배열을 회수하는데 유용함을 확인하였다. 열수의 가열, 터빈기동 및 전기투입방법 등의 운전방법을 최적화하였다. 그러나 HCFC-123 공급펌프의 능력부족으로 작동유체의 공급이 부족하여 정격출력보다 낮은 670kW의 전력을 생산할 수 있었다. HCFC-123의 공급유량을 증가시키기 위하여 파이프의 압력손실저하 및 펌프의 성능 향상을 위한 펌프교체 등이 고려되어야 함을 알 수 있었다.

• 설비공학논문집
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• 제18권4호
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• pp.312-319
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• 2006

In this study, performance of 2 pure hydrocarbons and 7 mixtures was measured in an attempt to substitute HCFC22 used in air-conditioners and heat pumps. The mixtures were composed of R1270 (propylene), R290 (propane), HFC152a, and RE170 (Dimethyl ether, DME). The pure and mixed refrigerants tested have GWPs of $3{\sim}58$ as compared to that of $CO_2$ and the mixtures are all near-azeotropic showing the gliding temperature difference (GTD) of less than $0.6^{\circ}C$. Thermodynamic cycle analysis was carried out to determine the optimum compositions and actual tests were performed in a laboratory heat pump test bench at the evaporation and condensation temperatures of 7.5 and $45.1^{\circ}C$ respectively. Test results show that the coefficient of performance (COP) of these mixtures is up to 5.7% higher than that of HCFC22. While propane showed 11.5% reduction in capacity, most of the fluids tested had the similar capacity to that of HCFC22. Compressor discharge temperatures were reduced by $11{\sim}17^{\circ}C$ with these fluids. There was no problem with mineral oil since the mixtures were mainly composed of hydrocarbons. The amount of charge was reduced up to 55% as compared to HCFC22. Overall, these fluids provide good performance with reasonable energy savings without any environmental problem and thus can be used as long term alternatives for. residential air-conditioning and heat pumping application.

• 청정기술
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• 제13권1호
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• pp.28-33
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• 2007

본 연구에서는 variable volume view cell이 장착된 상평형 장치를 사용하여 고압 상태의 다양한 용매 내에서 고분자인 Poly(methylmethacrylate) (PMMA)의 구름점(cloud point)를 측정하였다. 이때 사용된 용매는 chlorodifluoromethane (HCFC-22), dimethylether (DME), 1,1,1-trifluoroethane (HFC-143a), 1,1-difluoroethane (HFC-152a), 1,1,1,2-tetrafluoroethane (HFC-134a) 이였으며, 이들 용매에 $CO_2$를 첨가한 $HCFC-22+CO_2$와 $DME+CO_2$의 이성분계 혼합용매에서 $CO_2$의 조성 변화가 PMMA의 상거동에 미치는 영향을 살펴보았다. 실험 결과 PMMA는 HCFC-22에서는 340K, 5MPa 정도의 가장 낮은 온도 압력 조건에서부터 잘 용해되었으며 DME에서는 300K, 28MPa 정도의 비교적 낮은 온도 압력 범위에서 잘 용해되었으나, 그 밖의 불소화합물인 HFC-143a, HFC-152a, HFC-134a에서는 423.15K, 160MPa의 높은 온도 및 압력범위에서도 전혀 용해가 일어나지 않았다. 또한, PMMA+HCFC-22 혼합물에 $CO_2$를 첨가한 $PMMA+HCFC-22+CO_2$계의 경우는 LCST (lower critical solution temperature)의 상거동을 보였으나 PMMA+DME 혼합물에 $CO_2$를 첨가한 $PMMA+DME+CO_2$계의 경우는 UCST (upper critical solution temperature)의 상거동을 보였다. $CO_2$ 혼합용매 내에서 cloud point 압력은 동일한 온도에서 첨가되는 $CO_2$의 양에 비례하여 급격히 높아지는 것을 관찰할 수 있었고, 이로부터 PMMA를 SAS (supercritical antisolvent) 법에 의해 미세입자화 할 경우 $CO_2$가 DME와 HCFC-22에 대한 역용매로 사용될 수 있다는 것을 확인할 수 있었다. 또한 $CO_2$의 농도를 변화시킴으로써 PMMA의 cloud point를 자유롭게 조절할 수 있다는 것을 알 수 있었다.

• 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.

• 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.