• Korean Journal of Air-Conditioning and Refrigeration Engineering
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• v.15 no.12
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• pp.1007-1017
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• 2003

An experimental study on the air-side pressure drop and heat transfer coefficient of slit fin-tube heat exchanger has been carried out. The data reduction methodology for air-side heat transfer coefficients in the literature is not based on a consistent approach. This paper focuses on new method of data reduction to obtain the air-side performance of fin-tube heat exchanger using R22 and recommends standard procedures for dry and wet surface heat transfer estimation in fin-tube heat exchanger having refrigerant on the tube-side. Results are presented as plots of friction f-factor and Colburn j -factor against Reynolds number based on the fin collar outside diameter and compared with previous studies. The data covers a range of refrigerant mass fluxes of 150∼250 kg/$m^2$s with air flows at velocity ranges from 0.3 m/s to 0.8 m/s.

• Journal of the KSME
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• v.34 no.11
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• pp.859-866
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• 1994

석유화학플랜트에서 운용되는 반응로, 저장탱크, 열교환기 등의 압력용기 그리고 배관 등의 시 설물은 장기간 사용함에 따라 고온, 고압, 부식성 분위기, 열응력, 피로 등 여러 가지 요인으로 경년열화되어 노후화 된다. 일반적으로 이들 설비들에서 작용하는 유체나 가스의 누출은 화재나 폭발과 같은 재해 뿐만아니라 주위 환경을 오염시켜 공해를 유발하게 되며, 이들 시설물에 대한 신뢰성 및 안전성 확보는 국가기간 산업에서 매우 중요하며 이와 관련된 장치의 설계, 시공 뿐만 아니라 시험검사 및 평가기술 측면에서도 중요시되고 있다. 플랜트 시설물에 대한 가동중 주기적인 안전진단은 현상의 파악 뿐만 아니라 인명과 재산의 손실을 미연에 예방하고 경제적 이고 효율적인 운영계획 수립에 필수적인 것이다. 이 글에서는 국내 석유화학플랜트의 검사현 황을 알아보고 앞으로 플랜트의 효율적 운영 및 안전 운전을 위한 가동중검사 기술 및 개선대 책에 대하여 기술하고자 한다.

• Journal of the Korean Society of Combustion
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• v.14 no.3
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• pp.24-28
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• 2009

To improve its efficiency, most of the industrial furnace had been used recuperator. However, commonly used metal recuperator is not suitable under condition of temperature higher than $1000^{\circ}C$. The other hand, ceramic recuperator is able to use in high temperature condition. In the present study, the design program based on the basic heat exchanger design theory, and CFD modelling are applied to ceramic recuperator to verify the design results. Using design program to find the optimum design factor on the variation of recuperator condition. The result of this study are as follows : Thinner fin-plate thickness reduces pressure drop and increases heat-transfer rate, However, thin plate or plate with thin thickness(< 5 mm) is difficult to manufacture, due to limited mechanically strength.

• Journal of Power System Engineering
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• v.17 no.6
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• pp.54-62
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• 2013

A numerical analysis is performed to evaluate mass flow balance in the heat exchanger for the dehumidifier. To improve the mass flow balance for maximum heat transfer performance, inlet, outlet and baffle are changed. Mass flow balance is evaluated by non-uniformity of flow which is the same concept with the standard deviation. Usually, there will occur many paths between the inlet and the outlet, however, it will follow shortest and low resistance ways. The uniform distribution of flow is numerically analyzed for several types of heat exchangers. Making the shortest way between the inlet and the outlet is most important factor. Two types of heat exchangers are installed in the dehumidifier and 4 cases of Type A heat exchangers and 3 cases of Type B heat exchangers are evaluated and optimized. The result of this research is applied to design heat exchanger for commercial dehumidifiers.

• Transactions of the Korean Society of Mechanical Engineers
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• v.9 no.6
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• pp.795-800
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• 1985

The ideal Brayton cycle has been analyzed with the heat exchange processes between the working fluid and the heat source and the sink while their heat capacity rates are constant. The power fo the cycle can be expressed in terms of a temperature of the cycle and the heat capacity rate of the working fluid. There exists an optimum power condition where the heat capacity rate of the working fluid has a value between those of the heat source and the heat sink, and the cycle efficiency is determined by the inlet temperatures of the heat source and the sink.

• Proceedings of the KSME Conference
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• 2007.05a
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• pp.296-299
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• 2007

KAERI is in the process of carrying out the Nuclear Hydrogen Development and Demonstration (NHDD) Program. The indirect cycle gas cooled reactors that produce heat at temperatures in the order of $950^{\circ}C$ are being considered in the NHDD program. For the indirect gas cooled reactors, the intermediate hear exchanger (IHX) and hot gas duct (HGD) are the main components. For the NHDD program we are in the process of establishing a conceptual design of the IHX and HGD. The pre-conceptual design activities in this study dealt with a preliminary design of the IHX and the HGD including strength and thermal expansion evaluation of the main components.

• 한국신재생에너지학회:학술대회논문집
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• 2006.11a
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• pp.202-205
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• 2006

최근 지열원 열펌프 시스템 설치가 해마다 평균 10-30%젓도 꾸주히 증가하고 있다 주요 연구동향은 토양열전도 측정, 지열히트펌프 시스템 전주기 성능평가 하이브리드 시스템의 초기비용 저감과 이러한 지열원 열펌프 시스템 설계방법분야 개발에 대해 초점이 맞춰지고 있다. 특히 국내에서 현재 시공되어진 많은 시스템들이 부실시공의 문제에 노출되고 있으며 이러한 시점에서 현재의 저가 입찰제도 보다는 외국 사례와 같은 성능확인 제도로의 전환 및 많은 연구가 필요하다. 성능확인제도는 사전 성능 예측과 사후 성능 확인 검증으로 구성되며 본 기술현안 보고서는 최근 국내외 연구동향 및 사전 성능 예측과 사후 성능 검증 관하여 정리하여 본다.

• Journal of Institute of Convergence Technology
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• v.7 no.1
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• pp.19-22
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• 2017

SI process is one of the most advanced thermochemical water splitting cycles enabling mass production of hydrogen without emitting carbon dioxide when coupled to nuclear heat energy. The highest temperature (close to $1000^{\circ}C$) required in SI process is well matched with the outlet temperature of a coolant circulating a high-temperature gas-cooled reactor at around $950^{\circ}C$. In Section 3, some heat exchangers are included to recover heats from process flows at high temperature. In this work, we designed a heat exchanger based on the $1Nm^3/hr$ $H_2$ production capacity using commercial tools for chemical process design.

• 한국연소학회:학술대회논문집
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• 2012.11a
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• pp.115-118
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• 2012

The configurations of the heat exchanger of the boiler can be determined from the trade-off between the heat transfer area which is related to the capital cost and the pressure drop which is related to operating cost. In this study, 3.5 ton/hr small size marine boiler having concentric annuli tubes is the design boiler. To determine the optimizing point, according to diameter, number, length of tube, heat transfer, pressure drop, operating cost and capital cost have been calculated. Also, when the fin tube is replaced by the bare tube design parameters changed have been calculated.

• Korean Journal of Air-Conditioning and Refrigeration Engineering
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• v.2 no.2
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• pp.85-98
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• 1990

Method of optimum design of a compact sensible plate-fin heat exchanger for the heat recovery of exhaust gas from the air conditioning space was developed in consideration of the econamics of investment cost and profit according to the installation of heat exchanges. In the counterflow heat exchanger, the frontal area was fixed and the length of heat exchanger was optimized in order to maximize the net gain according to the setting of the heat exchanger. In the cross flow heat exchanger, the size of the exchanger was also optimized to maximize the net gain.