• The Magazine of the Society of Air-Conditioning and Refrigerating Engineers of Korea
• /
• v.31 no.7
• /
• pp.24-28
• /
• 2002

1987년의 몬트리얼 의정서에 의한 CFCs와 HCFCs의 규제에 이어 1999년의 교토의정서에 의한 지구온난화 물질에 대한 규제는 CFCs와 HCFCs의 대체물질로 준비되어온 HFCs의 사용에 제동을 걸게 되었다. 아울러 환경론자들은 냉동공조 업계가 HFCs를 사용하지 말고 탄화수소, 이산 화탄소, 암모니아, 물 및 공기와 같은 보다 환경친 화적인 자연냉매를 사용할 것을 요구하고 있으며, 최근 학계의 자연냉매에 대한 고무적인 연구결과는 자연냉매의 사용에 대한 산업계의 관심을 고조 시키고 있다. 본 고에서는 최근 주목을 받고있는 이 산화탄소를 냉매로 하는 냉방시스템 중의 한 요소인 가스쿨러에 대한 연구개발 현황분석 및 향후 과제에 대하여 살펴보기로 한다.

• Journal of Advanced Marine Engineering and Technology
• /
• v.29 no.8
• /
• pp.870-876
• /
• 2005

This study of the performance characteristics of natural refrigerants such as R-290 (propane), R-6OOa (iso-butane) and R-1270 (propylene) has investigated to compare with conventional HCFC's refrigerant R-22 for water-cooled heat pump system. The experimental apparatus has basic parts of cycle that uses the water as a heat source. The Performance of the water-cooled system using hydrocarbon refrigerants had been getting better than R-22 from start-up to the similar evaporating temperature after stabilizing system. Through the above it is possible that hydrocarbon refrigerants could be drop-in alternatives for R-22.

• Proceedings of the Korean Society of Marine Engineers Conference
• /
• 2005.11a
• /
• pp.41-42
• /
• 2005

The experimental apparatus has been set-up as a conventional vapor compression type heat pump system. The test section is a horizontal double pipe heat exchanger. A tube diameter of 12.70 mm, 9.52 mm, 6.35 mm with 1.78 mm,1.52 mm,1.4 mm wall thickness each is used for this investigation. The local evaporating heat transfer coefficients of hydrocarbon refrigerants were superior to that of R-22. and the maximum increasing rate of heat transfer coefficient was found in R-1270. The average evaporating heat transfer coefficient increased with the increase of the mass velocity and it showed the higher values in hydrocarbon refrigerants than R-22. The highest evaporating heat transfer coefficient of all refrigerants was shown in a tube diameter of 6.35 mm with same mass flux.

• Journal of Advanced Marine Engineering and Technology
• /
• v.23 no.4
• /
• pp.447-452
• /
• 1999

This paper describes the cycle performance of heat-pump system using R-22 and R-290. Experiments were performed in the smooth tube with inside diameter of 10.07mm and outside diameter of 12.07 mm and grooved inner tube having 75 fins with a height of 0.25mm Condensing temperatures were held constantly between 318K and 328 K while evaporating temperatures were varied from 257 K to 288 K mass velocities from 51 to $280 kg/m^2s$. From the experiments it was known that the evaporating temperature and condensing temperature had more affected by the compressor shaft power than the tube geometries. Cooling capacity of the R-22 and R-290 had similar values in the smooth and grooved inner tubes. The coefficient of performance(COP) was calculated using the compressor shaft power volumetric refrigeration capacity compression ratio and cooling capacity. The COP of the R-290 had slightly higher values than that of R-22 The major parameters affecting the heat pump cycle performance wee the refrigerant proper-ties and operating conditions rather than the geometric shapes of the heat exchanger

• Journal of Advanced Marine Engineering and Technology
• /
• v.31 no.1
• /
• pp.74-83
• /
• 2007

This paper presents the experimental results of evaporation heat transfer coefficients of HC refrigerants (e.g. R290 and R600a). R-22 as a HCFCs refrigerant and R-l34a as a HFCs refrigerant in horizontal double pipe heat exchangers, having four different inner diameters of 10.07, 7.73, 6.54 and 5.80 mm respectively. The experiments of the evaporation process were conducted at mass flux of $35.5{\sim}210.4 kg/m^2s$ and cooling capacity of $0.95{\sim}10.1 kW$. The main results were summarized as follows : The average evaporation heat transfer coefficient of hydrocarbon refrigerants(R-290 and R-600a) was higher than the refrigerants, R-22 and R-l34a. In comparison with R-22 the evaporation heat transfer coefficient of R-l34a is approximately $-11{\sim}8.1 %$ higher. R-290 is $56.7{\sim}70.1 %$ higher and R-600a is $46.9{\sim}59.7 %$ higher. respectively. In comparison with experimental data and some correlations, the evaporation heat transfer coefficients are well predicted with the Kandlikar's correlation regardless of a type of refrigerants and tube diameters.

• Korean Journal of Air-Conditioning and Refrigeration Engineering
• /
• v.12 no.1
• /
• pp.20-25
• /
• 2000

An experimental study on the condensation heat transfer coefficients of R-22, R-290 and R-600a inside horizontal tube was performed. Heat transfer measurements were performed for smooth tube with inside diameter of 10.07 mm and outside diameter of 12.07 mm and inner grooved tube having 75 fins whose height is 0.25 mm. This study was performed for condensation temperatures were from 308 K to 323 K, and mass velocity of $51 kg/m^2s - 250kg/m^2s$. The test results showed that the local condensation heat transfer coefficients increased as the mass flux increased, and also the effect of mass flow rate on heat transfer coefficients of R-290 was less than R-22. In addition, heat transfer coefficient of R-22 increased to a larger extent than R-290 and R-600a as the mass flow rate increased. Average condensation heat transfer coefficients of natural refrigerants were superior to that of R-22. The present results had a good agreement with Cavallini-Zecchin's correlation for smooth and inner grooved tubes.

• Transactions of the Korean Society of Mechanical Engineers B
• /
• v.24 no.1
• /
• pp.39-49
• /
• 2000

This paper presents the modeling approach that can predict transient behavior of rotary compressor. Mass and energy conservation laws are applied to the control volume, real gas state equation is used to obtain thermodynamic properties of refrigerant. The valve equation is solved to analyze discharge process also. Dynamic analysis of vane and roller is carried out to gain friction work. From the above modeling, the performance of rotary compressor with radial clearance and friction loss is investigated numerically. The performance of each refrigerant is estimated, respectively by applying R12, R134a, and R290/ R600a mixture.

• Journal of Advanced Marine Engineering and Technology
• /
• v.30 no.2
• /
• pp.204-210
• /
• 2006

This study presents heat pump system characteristics using hydrocarbon refrigerants as alternative refrigerant for R-22 with respect to the variation of indoor load. Pure R-22 and R-290. R-600a, R-1270 were considered as working fluids The experimental apparatus was constructed to investigate the performance of heat pump using the air as a heat source. The performance were calculated based on compression shaft work. refrigeration capacity. pressure ratio, discharge temperature and COP. The experimental results show that the COP and refrigeration capacity of hydrocarbon refrigerants were higher than that of R-22. Through the above. hydrocarbon refrigerants are good alternatives in the heat pump system for R-22.

• Proceedings of the Korean Society of Marine Engineers Conference
• /
• 2001.11a
• /
• pp.15-20
• /
• 2001

This study investigated the condensation heat transfer coefficients of R-22, R-290 and R-600a inside horizontal tube. Heat transfer measurements were peformed for smooth tube with outside diameter of 12.7 mm Condensation temperatures and mass velocity were ranged from 308 K to 323 K and $51kg/\textrm{m}^2s$s to $250kg/\textrm{m}^2s$, respectively. The test results showed that the local condensation heat transfer coefficients increased as the mass flux increased, and also the effects of mass velocity on heat transfer coefficients of R-290 and R-600a were less than R-22. Average condensation heat transfer coefficients of natural refrigerants were superior to that of R-22. The present results had a good agreement with Haraguchi's correlation.

• The Magazine of the Society of Air-Conditioning and Refrigerating Engineers of Korea
• /
• v.30 no.4
• /
• pp.56-60
• /
• 2001

경험에 의하면 앞에서 언급한 장비의 사용, 규율, 규제된 용제의 사용, 기름 페인트 사용의 억제, 그리고 엄격한 페인트 과정을 따르는 것에 의해 잠수함내의 탄화수소 농도를 100만분의 1 또는 2 수준으로 유지할 수 있다. 예방책으로는 세심한 관찰, 선체내로 들여오는 모든 물질의 기록 그리고 규제된 물질의 사용 시간, 장소 및 양의 제어이다. 이러한 점들은 잠수함 내부를 안전하고 건강한 환경으로 설계하기 위하여 활용될 수 있는 자료들이다. 잠수함 내의 공기질은 적외선 분광 광도계, 질량 분광계, 상자성(paramagnetics), 열전도율, 광이온화 그리고 열량 검사에 의해 분석될 수 있다. 분석된 결과는 과거의 데이터와 비교되어 활성탄충의 교체등을 포함하여 유지 관리의 자료로 활용된다. 이러한 원리를 이용한 다양한 계측기가 선체 내의 대기 상태를 분석하기 위하여 사용된다. 중앙 대기 측정기, 추적 가스 분석기, 수소 탐지기, 이동형 대기 모니터, 이동형 산소 분석기, 탄광 안전 지시계, 열량 분석관, 탐지 펌프 시험기가 사용된다. 이러한 계측기는 잠수 전 또는 후에 사용된다. 계측기는 화재 발생시 영향을 받지 않은 공간 또는 냉매가 충전되는 장소에 사용된다. 오늘날 여러 종류의 특별한 잠수함이 존재한다. 정찰 업무를 통해 세계 평화를 유지하고 특별한 임무를 수행하는 것보다 덜 복잡한 목적을 지닌 잠수함도 있다. 그러나 선원들이 안전한 내부 환경 속에서 바다 속을 항해하고 계속 그 응용 범위를 확장하기 위하여 앞에서 언급한 장비들 또는 그 변형들이 사용되어야 한다.