In this paper, cycle performance analysis of two-stage compression two-stage expansion refrigeration system using eco-friendly refrigerants is presented to offer the basic design data for the operating parameters of the system. Eco-friendly refrigerant R600a(Isobutane) for freon refrigerant R22 were used working fluids in this study. The coefficient of performance(COP) of R600a is about 5% greater than that of R22 two-stage compression refrigeration system in the range of evaporation temperature –30℃∼-60℃. The coefficient of performance of two-stage compression and two-stage expansion refrigeration system decreases with the increasing condensation temperature and superheating degree but increases with the increasing evaporation temperature, subcooling degree and mass flow rate ration of intercooler.

This paper considers the influence of internal heat exchanger and capillary tube on the efficiency of small refrigeration system using eco-friendly refrigerants such as R290, R600a, R1270, and R717. A refrigeration system using such internal heat exchanger and capillary tube may improve performance, but may degrade performance. Therefore, this paper used a mathematical model in a normal state to understand performance characteristics as to what change occurs when internal heat exchanger and capillary tube are attached to eco-friendly refrigerant based on R134a. In addition, the effects of operating conditions such as refrigerant flow rate, evaporation temperature, condensation temperature, subcooling degree internal heat exchanger length and capillary tube length were analyzed. The result showed that the evaporation temperature, condensation temperature, subcooling degree, internal heat exchanger length and capillary tube length had an effect on the refrigeration capacity and compression power. Therefore, it is necessary to design a refrigeration cycle using an eco-friendly refrigerant by grasping these effects in detail.

In this paper, the performance characteristics of a cryogenic refrigeration system used in fields such as HMR(Home Meal Replacement) that require ultra-low temperatures of -50℃ using natural refrigerants according to the recent enforcement of the Atmosphere Environment Conservation Act were investigated. For this purpose, a 2-stage compression refrigeration system using R744(CO2) and a cascade refrigeration system using R747/R404A and R747/R717(NH3) were applied. The COP(coefficients of performance) of each refrigeration system were compared according to changes in evaporation and condensation temperature, subcooled and superheated degree. Although the coefficient of performance of the 2-stage compression refrigeration system using R744 was superior to that of the cascade refrigeration system, 2-stage refrigeration system was considered that various problems should be solved in practical terms. In addition, the COP of R744/R717 for various operating conditions showed similar results to R744/R404A, so the possibility of alternativeness could be confirmed in the cascade refrigeration system.

This paper focuses on the simulation of refrigeration cycle equipped with the adiabatic capillary tube, which is widely used in small vapor compression refrigeration systems. The present simulation is based on fundamental conservation equations of mass, energy and momentum. These equations are solved through an iterative process. The adiabatic capillary tube model is based on homogeneous flow model. This model is used to understand the natural refrigerants flow behavior inside the adiabatic capillary tube. Transport properties and thermodynamic of natural refrigerants are calculated by using EES(Engineering Equation Solver) program. The operating factors considered in this paper include condensation temperature, evaporation temperature, inner diameter tube and sub-cooling degree of the adiabatic capillary tube. Our simulation results are summarized as follows: as the size of the inner diameter tube increases, the pressure drop in the capillary tube decreases while the length of the capillary tube increases. We found that R-290 decreases by 20-22% on average, and R-600a significantly decreases below 50%, while R-1270 increases 17-19% on average, compared to R-134a.

In this paper, cycle performance analysis of two-stage compression and two-stage expansion refrigeration system using Natural refrigerants is presented to offer the basic design data for the operating parameters of the system. Alternative natural refrigerant R290(Propane), R600(Butane), R717(Ammonia), R1270(Propylene) for freon refrigerant R22 were used working fluids in this study. The operating parameters considered in this study included evaporation temperature, condensation temperature, subcooling degree, superheating degree, and mass flow rate ratio of inter-cooler. The main results were summarized as follows : The COP of two-stage compression and two-stage expansion refrigeration system increases with the increasing subcooling degree and mass flow rate ration of inter-cooler, but decreases with the increasing evaporating temperature, condensing temperature and superheating degree. Therefore, subcooling degree, mass flow rate ratio of inter-cooler of two-stage compression and two-stage expansion refrigeration system using alternative nreon refrigerants have an effect on COP of this system.

In this paper, cycle performance analysis of two-stage compression and one-stage expansion refrigeration system using alternative Freon refrigerants is presented to offer the basic design data for the operating parameters of the system. Pure alternative Freon refrigerant R32, R134a and near NARM(Non-Azeotropic Refrigerants Mixtures) R404A, R407C, R410A and ARM(Azeotropic Refrigerant Mixtures) R507A were used working fluids in this study. The operating parameters considered in this study included evaporation temperature, condensation temperature, subcooling degree, superheating degree, mass flow rate ratio of inter-cooler. The main results were summarized as follows : The COP of two-stage compression and one-stage expansion refrigeration system increases with the increasing subcooling degree and mass flow rate ration of inter-cooler, but decreases with the increasing evaporating temperature, condensing temperature and superheating degree. Therefore, subcooling degree, mass flow rate ratio of inter- cooler of two-stage compression and one-stage expansion refrigeration system using alternative Freon refrigerants have an effect on COP of this system.

In this paper, cycle performance analysis of cascade refrigeration system using alternative FREON refrigerants are presented to offer the basic design data for the operating parameters of the system. The operating parameters considered in this study include subcooled and superheated degree, and evaporating and condensing temperature, temperature difference of cascade heat exchanger in cascade refrigeration system. The COP of cascade refrigeration system increases with the increasing subcooled degree, but there is no significant changes with the increasing superheated degree. The COP of cascade refrigeration system depends on evaporating and condensing temperatures of cascade heat exchanger. Therefore, subcooled degree, evaporating and condensing temperature of cascade heat exchanger using alternative FREON refrigerants have an effect on the COP of this system. In this paper, COP of cascade refrigeration system using R23 for low temperature system and R507A for high temperature system is higher 8 ~ 29 % than using R13 for low temperature system and R22 for high temperature system.

In this paper, cycle performance analysis of cascade refrigeration system using natural refrigerants R744 for low temperature cycle, and R290, R600, R600a, R717 for high temperature cycle are presented to offer the basic design data for the operating parameters of the system. The operating parameters considered in this study include subcooled and superheated degree, and condensing and evaporating temperature, temperature difference of cascade heat exchanger in cascade refrigeration system. The COP of cascade refrigeration system increases with the increasing subcooled degree, but there is no significant changes with the increasing superheated degree. The COP of cascade refrigeration system depends on evaporating and condensing temperatures of cascade heat exchanger. The COP of cascade refrigeration system using natural refrigerants is similar to the COP using freon refrigerant (R23 / R22). Points to be considered are th security, the attached facilities for natural refrigerants than COP.

The most common types of refrigerants used in automobiles today usually include HCFCs and HFCs, which have the potential of ozone depletion or the greenhouse effect. Although environmentally friendly refrigerants are being developed, there is still a lack of safety and high-cost problems for new refrigerants. This study was conducted to determine the flow of refrigerants from automotive air conditioners and examine their potential problems and a proper management plan. The number of automobiles manufactured, the number of automobiles in use, and end-of-vehicle flow were examined through available statistics and reports. The material flow of refrigerants has been determined by the life cycle of automobiles and the unit requirements of the refrigerants used in automobiles. Based on the results, in 2014, there were approximately 1,017 tons of refrigerants introduced from the manufacturing stage of automobiles, and about 395 tons of refrigerants leaked from the use stage. After the use stage, only 13 tons of refrigerants were delivered to treatment facilities and 195 tons were emitted into the atmosphere during the dismantling process. As a result, in South Korea in 2014, a large amount of refrigerants (590 tons) was estimated to have been leaked into the atmosphere from automotive air conditioners during the use and dismantlement stage. Several preventive measures for refrigerants should be properly enforced by introducing economic incentives as well as a monitoring system with strengthened laws and policies.

Proper management of refrigerant mixtures containing chlorine and fluorine are gaining worldwide interest in the recent years as, they contribute to global warming and ozone depletion. according to the Montreal Protocol, developed nations have substituted HCFCs in refrigerators and air conditions synthetic greenhouse gas (SGGs) refrigerants such as, R-10 (CCl4), R-23 (CHF3), and R-134a (CH2FCF3). SGGs contribute to the increasing global warming potential. incineration, conventional treatment method of R-134a leads generation of Freon gas, due to excess air during the deacon reaction and due to the flame inhibition of the halogen compound. Therefore, this study proposes on the effective thermal treatment (high-temperature pyrolysis) of R-134a using numerical analysis. R-134a is usually known to have reaction characteristics which degrade only at temperatures reaches 800℃ and contains sufficient moisture in the furnace, HFC-134a refrigerant is treated efficiently by following chemical reaction. C2H2F4+4H2O → 4HF+3H2+3CO2, 4HF+2Ca(OH)2 → 2CaF2+4H2O in this study numerical calculation is performed for the relevant variables. As a result, very positive preliminary results showed about HFC-134a refrigerant treatment. Base on this, in the following study, organized variable research and demonstration experiment will be performed.