• International Journal of Air-Conditioning and Refrigeration
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• 제14권1호
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• pp.7-13
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• 2006

Because the usage of CFC and HCFC based refrigerants are restricted due to the depletion of ozone layer, the $NH_3$ gas, in the experiment is evaluated to the performance characteristics for the superheat control to improve the energy efficiency. The experiment is carried out about the condensing pressure of refrigeration system from 1,500 kPa to 1,600 kPa through the degree of superheat from 0 to $10^{\circ}C$ at each condensing pressure. As a result, in the case of shell and tube type of heat exchanger, the COP is more efficient than other cases at the degree of superheat $1^{\circ}C$ at each condensing pressure. In the case of shell and disk type of heat exchanger, the COP is the most efficient at the degree of superheat 0.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2004년도 추계학술대회
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• pp.1264-1269
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• 2004

This research describes the application of hydrocarbon refrigerants for heat pump system which is needed for fish farm. Tested refrigerants are HCFC-22 and hydrocarbon refrigerants(CARE 50 and ASR-20). CARE 50 is mixture of R-290 and R-170, and ASR-20 is mixture of R-152a, R-290 and other additives. Heat pump consist of shell and tube heat exchanger, scroll compressor, expansion valve and accumulator. Manual expansion valve is used for testing of wide range evaporating temperature. Hydrocarbon refrigerants show a good performance as an alternative for HCFC-22 in the range of evaporating temperature from $-6^{\circ}C$ to $6^{\circ}C$.

• 한국컴퓨터정보학회논문지
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• 제28권1호
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• pp.121-127
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• 2023

본 연구에서는 질소화합물을 최적으로 줄일 수 있는 SCR에서 설계 조건과 CFD 해석 결과를 비교해 검토하고자 한다. 이를 위해 보일러의 쉘과 튜브 영역에 대해 설계 기준을 만족하고 있는지 CFD을 이용하여 해석하고 비교하였다. SCR 시스템에서 해석영역은 쉘 측은 가스·공기 열교환기 입구에서 출구까지이고, 튜브 측은 가스·공기 열교환기의 8개 튜브로 설정하였다. CFD 해석을 통해 SCR 시스템의 1차 촉매 면에서 가스의 속도 분포는 2.7%로 설계되었고, NH3/NOx 몰비 분포는 3.7%로 설계 기준을 만족하였다. 또한, 온도 분포의 균일성을 확인하였고 요구 조건인 260℃ 이상을 만족하였다. 촉매에 유입되는 가스의 각도는 2.9도로 설계 조건을 충족하였고, 그리고 발생하는 압력손실도 설계 요구조건을 만족하였다. 이러한 CFD 해석을 통해 각 영역별로 요구되는 설계조건을 만족하여 설계되어 최적으로 운전되고 있음을 확인하였다.

• 한국가스학회지
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• 제7권2호
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• pp.22-32
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• 2003

Al-황동은 기계적 특성 및 열전도성이 우수하고 해수 중에서 표면 보호피막을 형성하므로 부식저항성이 높아 해수를 냉각수로 사용하는 선박용 열교환기의 세관재로 널리 사용되고 있다 Al-황동 세관은 실제 사용 환경에서 굽힘 등에 의한 소성변형된 상태로 사용되는 경우가 많다. 이와 같은 소성변형에 의한 Al-황동 세관의 균열 파손사례는 선박의 오일탱크 내의 가열코일, 각종 열교환기의 세관 등에서 흔히 찾아 볼 수 있다. 또한 세관의 확관에 의한 밀봉 방법에 따라 세관의 변형에 의한 잔류응력 및 어패류 혼입에 의한 해수 유입부의 국부적인 유속증가 등에 기인하여 Al-황동 세관의 균열 및 침식 등의 파손사례가 보고되고있다. 본 연구에서는 $3.5\%$ NaCl. + $0.1\%\;NH_4OH$ 수용액을 시험편 표면에 5 m/s로 액분사하의 가속실험에서 Al-황동 세관의 응력부식균열 거동에 미치는 응력의 영향에 대하여 고찰하였다.

• 한국공작기계학회논문집
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• 제14권4호
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• pp.69-74
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• 2005

Nowadays CFC and HCFC refrigerants are restricted because they causes to depletion of ozone layer. Accordingly, an experiment is apply to the $NH_3$ gas for refrigerant to study the performance characteristic and to improve the energy efficiency. An experiment are carried out for the condensed pressure in a range from 14.5bar to 16bar and for degree of superheat in a range from 0 to $10^{\circ}C$ at each condensed pressure. As the result of experiment, when degree of superheat is $1^{\circ}C$ and condensed pressure is 14.5bar, the refrigeration system showed the high performance.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2008년 영문 학술대회
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• pp.804-809
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• 2008

In this study, the cooling performance of a C/C composite material structure with metallic cooling tubes fixed by elastic force without chemical bonding was evaluated experimentally using combustion gas in a rocket combustor. The C/C composite chamber was covered by a stainless steel outer shell to maintain its airtightness. Gaseous hydrogen as a fuel and gaseous oxygen as an oxidizer were used for the heating test. The surface of these C/C composites was maintained below 1500 K when the combustion gas temperature was about 2900 K and heat flux to the combustion chamber wall was about 9 $MW/m^2$. No thermal damage was observed on the stainless steel tubes which were in contact with the C/C composite materials. Results of the heating test showed that such a metallic-tube-cooled C/C composite structure is able to control the surface temperature as a cooling structure(also as a heat exchanger), as well as indicating the possibility of reducing the amount of the coolant even if the thermal load to the engine is high. Thus, application of the metallic-tube-cooled C/C composite structure to reusable engines such as a rocket-ramjet combined cycle engine is expected.

• 설비공학논문집
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• 제11권1호
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• pp.48-60
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• 1999

An experimental study on the performance enhancement of a screw-compressor-type chiller with 100kW of nominal cooling capacity has been carried out. Performance test facility was developed to investigate the effects of a partial modification from the existing chiller on the performance. By replacing the existing shell-and -tube heat exchangers with plate heat exchangers, the cooling capacity is increased by 15~18% and the COP is also increased by 19~21% depending on the operation temperature range. Charging mixed refrigerant R22/R142b(80 : 20) instead of R22 into the chiller with plate heat exchangers improves the cooling capacity by 4% and the COP very largely by 30%. Each contribution of the plate evaporator, plate condenser, and mixed refrigerant to the performance enhancement is examined by analyzing the refrigeration cycle and the heat transfer processes. It is also shown that the chiller performance can be improved by adapting 2-stage-compression cycle using an economizer.

• Journal of Advanced Marine Engineering and Technology
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• 제40권3호
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• pp.157-164
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• 2016

본 연구에서는 SI 공정 시스템에서 헬륨 가열 장치에 대한 설계와 건조 데이터 확보를 위한 파이롯 규모의 헬륨 가열 장치 시스템에 대한 예비 설계 및 해석을 수행하였다. 헬륨 가열기는 LPG연소로를 활용하도록 설계하였고, 열유동 해석을 수행한 결과, 열교환기 출구측에서 LPG 연소가스의 유속이 약 40 m/s가 되었다. 최대온도는 6개의 베플이 설치된 경우가 4개의 베플이 설치된 경우보다 높게 나타나며, 이는 6개의 베플일 때 연소가스에서 헬륨가스로의 열전달이 좋아질 것임을 의미한다. 더불어, 베플수가 많아지면 LPG 연소가스의 유량을 감소시킬 수 있어 연료비용을 저감할 수도 있음을 의미한다. 다만, 베플수를 무한정 증가시키면 입출구의 압력차가 증가되기 때문에 최적의 베플수 선정이 중요하다. 열유동 해석에 이어 수행한 구조해석에서는 헬륨의 유량을 3.729 mol/s, 출구 온도를 $910^{\circ}C$로 유지할 경우 관의 양 끝단에서 지지하는 경우 중간부분의 팽창률이 3.86 mm임을 확인하였다. LPG 연소로 헬륨 가열시스템에서 shell & tube type의 열교환기를 적용하여 $135^{\circ}C$의 헬륨이 $910^{\circ}C$로 가열하여 유출하기 위해서 약 $1300^{\circ}C$의 연소가스 온도 및 52 g/s의 연소가스 유량이 확보되어야 함을 확인하였다.

• Nuclear Engineering and Technology
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• 제56권8호
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• pp.3315-3329
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• 2024

Small Modular Reactors (SMRs) adopt the Helically Coiled Once-Through Steam Generators (OTSG) extensively for its compactness and higher heat transfer efficiency. As a heat exchanger between the primary side (reactor coolant system) and the secondary side (feedwater and steam system) of nuclear steam supply system, the inlet/outlet conditions both of shell side and tube side of OTSGs have significant impacts on overall system response. Considering the flexible operation of SMRs and heat application by extracting steam, a simulation tool for accurate prediction of the OTSG dynamic behaviors would be required for optimizing design and control. In this study, the OTSG dynamic simulation model has been developed. Mathematical governing equation has been derived by using moving boundary approach and a simulation module has been developed by using Modelica Language. The developed module has been compared with publicly available experimental results and benchmarked with MARS-KS calculation results. Also, it has been incorporated into the integrated SMR model (i.e., reactor core, primary side, secondary side) and dynamic behaviors with reactivity feedback and heat balancing have been investigated. In both of steady-state and transient conditions, it shows the promising accuracy.

• 대한기계학회논문집B
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• 제33권8호
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• pp.596-603
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• 2009

The performance of proton exchange membrane fuel cell (PEMFC) is seriously changed by the humidification condition which is intrinsic characteristics of the PEMFC. Typically, the humidification of fuel cell is carried out with internal or external humidifier. A membrane humidifier is applied to the external humidification of residential power generation fuel cell due to its convenience and high performance. In this study, a simple static model is constructed to understand the physical phenomena of the membrane humidifier in terms of geometric parameters and operating parameters. The model utilizes the concept of shell and tube heat exchanger but the model is also able to estimate the mass transport through the membrane. Model is constructed with FORTRAN under Matlab/$Simulink^{(R)}$ $\Box$environment to keep consistency with other components model which we already developed. Results shows that the humidity of wet gas and membrane thickness are critical parameters to improve the performance of the humidifier.