• Proceedings of the Korea Society for Energy Engineering kosee Conference
• /
• 1995.11a
• /
• pp.115-115
• /
• 1995

다중 효용관식 증발기는 보통의 증발기에서 응축하여 제거하는 증기를 다음 효용관의 가열원으로 재사용하는 것으로 그 자체로도 에너지 절감효과가 있는 것으로 알려져 있다[1,2,4]. 기계식증기 재압축 증발기는 보통 증발기에서 응축시켜 제거하는 발생 증기를 압축하여 고온의 증기로 만든 다음 가열원으로 재이용하는 장치로 이에 대한 효용은 문헌에 잘 나타나있다[3,4]. 여기서는 다중효용관과 증기 재압축기를 조합한 증발기 중에서 Forward feed 방식의 다중효응관에 증기 재압축기를 부착한 경우에 대하여 타당한 물질수지, 열수지, 전열 식, 상평형식을 소개하였다. 또한 압축기의 용량을 결정하기 위한 단열압축공정의 지배방정 식을 소개하였다. 원료의 조건, 효용관의 수 및 총전열온도차가 주어지면 상기의 지배방정식의 해를 구할 수 있는데. 본연구에서는 Gauss-Seidel의 연속치환법을 이용하였다. 이와 같이 지배방적식의 해를 구하면 효용관의 면적, 압축펌프의 용량, 각효용관 입출구의 조건 등이 계산된다. 다중효용관 기계식 증기 재압축 증발장치의 최적화를 위하여는 효용관의 전열면적당 가격과 압축펌프의 용량당 가격 그리고 펌프를 운전하는데 필요한 전력의 요금 등의 자료가 요구된다. 총전열온도차에 따른 운전비와 시설비의 합이 최소가 되는 점이 최적 총전열온도차가 되는데 이 점을 구할 때에는 수치적으로 안정한 이분법을 이용하였다. Borland C++를 이용하여 프로그램하였으며 윈도우즈 환경에서 수행되게 하였다. 사용자 쉽게 이용할 수 있게 하기 위하여 각종 필요한 데이터를 입력할 수 있는 Edit box가 화면에 나타나게 하였다. 또한 입력된 데이터를 저장하거나 불려올 수 있는 메뉴, 입력된 데이타를 이용하여 효용관의 면적과 압축기의 용량을 계산하거나 효용관의 수가 주어졌을 때 총전열온도차를 최적화하는 것을 선택할 수 있는 메뉴 그리고 계산 결과를 파일로 혹은 프린트로 출력할 것을 선택할 수 있는 메뉴가 있다. 사용자는 해당되는 데이타를 입력한후 마우스로 원하는 작업의 메뉴를 선택하면 된다.

• Journal of the Korea Academia-Industrial cooperation Society
• /
• v.16 no.11
• /
• pp.7736-7744
• /
• 2015

Considering the significant waste of industrial energy, effective use of low temperature waste heat is extremely important. In this study, a heat pump cycle with double effect and double stage was realized, which escalates the hot water temperature from $50^{\circ}C$ to $70^{\circ}C$ using $160^{\circ}C$ high temperature heat source and $17^{\circ}C$ low temperature heat source. The steam generated in the first generator condenses in the first condenser generating steam in the second generator. The steam condenses in the second condenser and is provided to the second evaporator. Part of the water out of the second evaporator is supplied to the first evaporator, which evaporates using low temperature waste heat. The evaporated steam enters the first absorber and the second evaporator. The steam out of the second evaporator is absorbed into the solution at the second absorber. The hot water temperature is raised in the second condenser and in the second absorber. Proper flow rates and UA values, which satisfied temperature lift $20^{\circ}C$ and COP 1.6, were deduced through trior and error. The COP increases as the temperature of the high temperature water increases, hot water temperature decreases and flow rate increases, waste water temperature and flow rate increases, solution circulation rate decreases. On the other hand, the temperature rise of the hot water increases as the temperature of the high temperature water increases, hot water temperature increases and flow rate decreases, waste water temperature and flow rate increases, solution circulation rate increases. In addition, the COP and hot water temperature rise increase as UAs of the heat exchangers increase.

• Journal of the KSME
• /
• v.33 no.11
• /
• pp.942-950
• /
• 1993

이 글에서는 자동차용 에어컨의 냉매 규제에 따른 대체냉매의 적용시 에어컨의 성능 변화를 이 론적으로 예측하여 보고, 냉매의 대체에 따른 응축기의 변경에 의한 성능 특성을 실험 결과로 설명하였다. 기존의 응축기(SPC)를 SCC로 교체함으로써 대체냉매를 사용하는 시스템에서 열전 달성능의 향상을 꾀할 수 있었다. 자동차용 에어컨에서 냉매의 교체에 따라 변경이 예상되는 부품으로는 응축기를 비롯하여 증발기, 팽창밸브, 수액기건조제, 압력스위치, 배관호스류, 압축기 압축기오일, 팬모터 등이 될 수 있다. 이러한 요소부품의 변경을 위해 연구개발되어야 할 기술 로는 먼저 운전 및 성능을 고려한 각 부품의 설계기술과 제작기술의 개발이 필요하다. 특히 자 동차의 내구연한의 확장에 따른 에어컨의 내구성 및 신뢰성의 문제는 지속적으로 연구되어야 할 것이다.

• Transactions of the Korean Society of Mechanical Engineers B
• /
• v.40 no.11
• /
• pp.705-715
• /
• 2016

In this study, the cycle performance of an air conditioner with multi-indoor units is analyzed and simulated. The cycle performance could be predicted through the integration of mathematical formulation for these devices. The condenser pressure is obtained by an iteration process to match the mass flow rates of the compressor and the expansion valve and the evaporator pressure is determined by an iteration process, in which the suction super heat is tracing the targeted super heat. The required software was developed by system programming. the software algorithm is extended to predict the cycle performance of an air conditioner system with multi-indoor units, and then the numerical results are compared with experimental results. This mathematical model is validated from the result of experiments conducted on 8.3kW air conditioner. The errors in capacity, electronic power, and COP are found to be within 10% in general.

• Proceedings of the KSME Conference
• /
• 2000.04b
• /
• pp.19-24
• /
• 2000

The objective of this study is to develope a computer simulation model and estimate theoretically the transient performance characteristics of heat exchangers in an automotive air-conditioning system. To do that, the mathematical modelling of heat exchangers, such as evaporator and condenser, is presented first of all. For detail calculation, evaporator and condenser are divided into many sub-sections. Each sub-section is an elemental volume for transient modelling. The elemental volume is assumed to consist of three components, refrigerant, tube with fin, and air, and various properties including temperatures of three components are determined step along sub-sections. The properties of refrigerant R134a and air are calculated directly in the program. The heat transfer coefficients and pressure drop in single or two phase are also calculated by suitable empirical correlations. The overall tendencies of the simulation results were agreed well with those of actual situation.

• Journal of the Korea Academia-Industrial cooperation Society
• /
• v.14 no.3
• /
• pp.1003-1010
• /
• 2013

In this study, a simulation program was developed, which predicts the performance of cold-air forced circulation type air cooled showcase. The showcase has an excellent display effect in addition to preserving the grocery. In the program, the compressor was analyzed using performance data supplied by the manufacturer and the capillary tube pressure drop was analyzed using a homogeneous model. The evaporator and condenser were analyzed by dividing the heat exchangers into small elements, where energy balance and appropriate heat transfer correlations were used. A showcase model with two 3/4 HP compressors, capillary tubes of 1.6 mm inner diameter, a fin-and-tube evaporator and condenser was tested, and the results are compared with the predicted values. It is shown that both evaporation and condensation temperatures are adequately predicted by the program.

• Proceedings of the Korean Nuclear Society Conference
• /
• 1998.05b
• /
• pp.539-544
• /
• 1998

MEO 공정에서 발생하는 질산폐액으로 부터 고농도 질산을 회수하기 위한 증발및 증류 공정특성을 연구하였다. 증발율이 20 이상인 경우 질산회수가 최대가 되는 특정 염농도가 존재함을 알 수 있었다. 증발율이 25인 경우 증발공정에서 발생한 묽은 질산용액을 12 M의 고농도 질산용액으로 농축하기 위한 증류탑을 계산하였다. 그 결과 증류탑은 효을이 70%인 9개의 단으로 구성되고, 환류비 0.25, 재비기 열량 2.7 kW, 응축기 열량 0.4 kW의 운전조건을 도출하였다.

• Journal of Energy Engineering
• /
• v.10 no.3
• /
• pp.253-265
• /
• 2001

This paper investigates a PI control problem for the evaporator superheat, i.e., temperature difference between the two-phase region and the exit region of an evaporator, for multi-type air-conditioning/refrigeration system. Mathematical model describing the characteristics of compressor, condenser, evaporator, and electronic expansion valve are first derived. Then, two transfer function from the current input applied to an electronic expansion valve to the wall-temperatures of an evaporator tube at two-phase region and superheated region, respectively, are derived. The stability of the closed loop system with the PI controller designed it analyzed by using Nyquist stability criterion. Simulation results are provided.

• Solar Energy
• /
• v.15 no.1
• /
• pp.29-38
• /
• 1995

This paper concerns the study of a two-stage binary absorption cycle employing the refrigerant/absorbent combinations of $LiBr/H_2O$ and $NH_3/H_2O$. This cycle consists of coupling two single-effect absorption cycles so that the first stage absorber and condenser produces heating water to evaporate refrigerant in the evaporator of the second stage. The effect of operating variables such as evaporator temperature, condenser and absorber temperature, and generator temperature on the coefficient of performance and temperature lift have been studied for two-stage binary absorption heat pump systems. It is found that this cycle has a large temperature lift at $105^{\circ}C$ of optimum generator temperature to obtain $50^{\circ}C$ of condenser temperature.

• Journal of Advanced Marine Engineering and Technology
• /
• v.35 no.8
• /
• pp.1001-1008
• /
• 2011

This paper describes an analysis on performance and exergy of R744-R404A cascade refrigeration system with internal heat exchanger to optimize the design for the operating parameters of this system. The operating parameters considered in this study include subcooling and superheating degree, internal heat exchanger and compression efficiency, evaporation and condensation temperature in the R744 low- and R404A high- temperature cycle, respectively. The main results are summarized as follows : As the evaporation temperature of cascade heat exchanger increases, the COP of R404A high-temperature cycle increases. But the COP of R744 low-temperature cycle decreases, and the COP of total cascade cycle is almost constant. As cascade evaporation temperature increase, the exergy loss in the R404A condenser and the R744 internal heat exchanger is the largest and the lowest among all components, respectively. Therefore, the exergy loss in the condenser and compressor of R404A must be decreased to enhance the COP of R744-R404A cascade refrigeration system.