• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2009년도 하계학술발표대회 논문집
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• pp.533-538
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• 2009

The present study has been conducted to an analysis of two stage refrigeration cycle with alternative refrigerant R410A. In the analysis, single stage cycle (R22 and R410A) compared to COP changing with supercooling degree. Secondly, two stage refrigeration cycle is investigated to the existence of intercooler or supercooler. At results, supercooler contributes to the increase of cooling capacity and the decrease of COP.

• 한국산학기술학회논문지
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• 제9권2호
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• pp.264-269
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• 2008

본 논문은 수평 이중관식 열교환기 내 프레온계 냉매의 대체냉매인 탄화수소계 냉매(R-290과 R-600a)의 증발 열전달 계수에 대한 실험적 결과를 나타내었다. 증발기의 내관 내경은 각각 10.07 mm와 6.54 mm의 2가지를 사용하였다. 증발실험은 질량유속 $35.5{\sim}210.4\;kg/m^2s$이고, 냉각용량 $0.95{\sim}10.1\;kW$인 조건에서 수행하였다. 실험결과를 요약하면, 탄화수소계 냉매 R-290과 R-600a의 증발 열전달 계수가 프레온계 냉매 R-22보다 높았다. 즉, R-22의 증발 열전달 계수에 비해, R-290와 R600a는 각각 $56.7{\sim}70.1%$와 $46.9{\sim}59.7%$ 정도 높았다. 실험데이터와 종래의 상관식을 비교한 결과, 모든 냉매와 관경에 대해서 Kandlikar상관식이 가장 좋은 일치를 보였다.

• 설비공학논문집
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• 제22권5호
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• pp.268-274
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• 2010

Because both R-134a and R-600a are used as a refrigerant of a household refrigerator in the global market, the home-appliance industry needs an optimized cycle for both refrigerants. The objective of this study is to provide the design guideline on the optimization of a refrigeration system using both refrigerants. For both refrigerants, the performance characteristics of the refrigeration system were tested by varying refrigerant charge amount, capillary tube length, suction diameter and SLHX length. The tested refrigeration system was optimized at the refrigerant charge of 60 g and the capillary tube length of 3600 mm with R-134a, and the refrigerant charge of 34 g and the capillary tube length of 3900 mm with R-600a. The COP increased from 1.63 to 1.68 for R-134a and increased from 1.37 to 1.48 for R-600a, respectively, by applying the suction diameter expansion. In addition, the COP of the R-134a and R-600a system decreased by 2.3~2.4% as the SLHX length decreased by 300 mm.

• 설비공학논문집
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• 제10권1호
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• pp.56-65
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• 1998

In this paper, experimental investigation of capillary tube performance for R-407C is performed. The experimental setup is made of real vapor-compression refrigerating system. In this study, mass flow rate is measured for capillary tubes of various diameter and length as inlet pressure and degree of subcooling are changed. These data are compared with the results of a numerical model. The mass flow rates of the numerical model are less than by 14% compared with the measured mass flow rates. It is found that mass flow rate and length for R-407c are less than those of R-22 under the same condition. Also based on this experimental study and the numerical model, a set of capillary tube selection charts for R-407C is constructed.

• 설비공학논문집
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• 제5권1호
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• pp.73-83
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• 1993

Thermodynamic properties of alternatives for R12 and R22 were estimated and performances of refrigerating cycle using these refrigerants were compared. In this study, we adopt R134a, R22/R142b, R22/R152a, R22/R152a/R124 as alternatives for R12 and R32/R134a for R22. Thermodynamic properties of these refrigerants were estimated using modified CSD equation of state. Cycle simulations of the refrigerating system considering heat source were carried out in order to compare the performance of the system. R134a shows relatively lower COP than R12 but very similar VCR. R22/R142b(50/50 mass fraction), R22/R152a(10/90), R22/R152a/R124(30/25/45) are good for the substitutes of R12 and R32/R134a(30/70) is appropriate for that of R22 in view of COP and VCR.

• 설비공학논문집
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• 제17권7호
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• pp.649-658
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• 2005

Flow condensation heat transfer coefficients (HTCs) of R22, R410, Propane (R290) were measured inside a horizontal 9 hole aluminum multi-channel flat tube. The main test section in the refrigerant loop was made of a 0.53m long multi-channel flat tube of hydraulic diameter of 1.4 mm. Refrigerant was cooled by passing cold water through an annulus surrounding the test section. Data were obtained in qualities of $0.1\~0.9$ at mass flux of $200\~400kg/m^2s$ and heat flux of $7.3\~7.7kW/m^2$ at the saturation temperature of $40^{\circ}C$. All popular heat transfer correlations in single-phase subcooled liquid flow and flow condensation originally developed for large single tubes predicted the present data of the multi channel flat tube within $25\%$ deviation when effective heat transfer area was used in determining experimental data. This suggests that there is little change in flow characteristics and patterns when the tube diameter is reduced down to 1.4 mm diameter range. Hence, a modified correlation based on the present data was proposed which could be applied to small diameter tubes with effective heat transfer area. The correlation showed a mean deviation of less than $20\%$ for all data.

• 설비공학논문집
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• 제14권12호
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• pp.1039-1046
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• 2002

To investigate the characteristics of orifice as an expansion devices, the experimental apparatus was made and experiments are being peformed using R22 and R290. The main idea of this control method of refrigerant flow rate with coupled orifices is to control the ON/OFF state of T and Ball type orifice corresponding to the subdivided region of thermal load. When system requires minimum thermal load, both T and Ball type orifices are closed, but refrigerant can flow through small hole of T type orifice. In regular thermal load, when ball type orifice is closed, T type orifice is opened and mass flow rate increase more than OFF state of T type orifice, due to large diameter. In maximum thermal load, both T and Ball type orifices are open and the much refrigerant can flow. The flow characteristics on T type orifice and parallel-combined orifice are obtained in the subdivided region of thermal load.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2003년도 하계학술대회 논문집
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• pp.145-145
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• 2003

• International Journal of Air-Conditioning and Refrigeration
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• 제8권1호
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• pp.40-49
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• 2000

The capillary tube performance for R-407C is experimentally investigated. The experimental setup is a real vapor-compression refrigerating system. Mass flow rate is measured for various diameter and length while inlet pressure and degree of subcooling are changed. These data are compared with the results of a numerical model. The mass flow rate of the numerical model is about 14% less than the measured mass flow rate. It is found that mass flow rate and length for R-407C are less than those for R-22 under the same condition. Based on this experimental study and the numerical model, a set of design charts for capillary tube of R-407C is proposed.

• 에너지공학
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• 제15권4호
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• pp.243-249
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• 2006

본 실험적 연구는 슬릿휜-관열교환기의 냉매측 압력강하에 대하여 수행하였다. 응축기의 설계조건에서 미세휜관내 냉매 R22와 R134a의 압력강하에 대한 실험데이터와 앞서 제안한 상관관계식과 상호 비교하였다. 실험은 냉매 R22와 Rl34a의 응축기 입구온도 $60^{\circ}C$, 질량유속 $150{\sim}250\;kg/m^{2}s$ 범위에서 수행하였다. 공기의 유입조건은 건구온도 $35^{\circ}C$, 상대습도 40%이며, 공기유속의 범위는 $0.68{\sim}1.43\;m/s$이다. 실험결과 응축기의 과냉도 $5^{\circ}C$ 조건에서 R134a의 압력강하는 R22보다 $22{\sim}22.6%$ 높게 나타났으며, 냉매의 질량유속 $200{\sim}250\;kg/m^{2}s$의 범위에서 실험으로부터 측정한 R22와 Rl34a의 압력강하는 예측결과와 ${\pm}20%$내에 일치하였다.