• 설비공학논문집
• /
• 제21권2호
• /
• pp.87-93
• /
• 2009

Slim telecommunication cabinet cooler, equipped with parallel flow heat exchangers and operating with R-22, is developed. The performance is compared with imported one, equipped with fin-tube heat exchangers and operating with R-134a. Test results show that the newly-developed cooler increases the cooling capacity by 6% and EER by 33%. The refrigerant charge for the developed cooler is 500g compared with 1250g for the imported one. The adoption of parallel flow heat exchanger appears to have reduced the refrigerant charge. In addition, it is shown that the reduced air flow rates through parallel heat exchangers as compared with those through fin-tube heat exchangers are beneficial to the reduction of the equipment noise.

• 한국연소학회:학술대회논문집
• /
• 한국연소학회 2000년도 제20회 KOSCO SYMPOSIUM 논문집
• /
• pp.169-177
• /
• 2000

The catalytic heat exchanger, which integrates two functions of heat generation and heat exchange into one equipment, was designed and its characteristics were investigated by the experiment and numerical simulation. The surface of the fin tube was deposited with Pd catalyst. The conversion of the mixture in the catalytic heat exchanger was more significantly affected by the inlet velocity of the mixture than by the inlet temperature and equivalence ratio of the mixture. It was found that the catalytic surface area of the fin tubes should be sufficiently increased to make the combustion intensity of the catalytic heat exchanger as high as possible. Results showed that the fin tubes, placed in the triangularly staggered form, should be adjusted so that the mixture flows uniformly over all the catalytic fin surfaces. Numerical simulation results demonstrated that the flow pattern of the mixture significantly affected the conversion of the mixture.

• 설비공학논문집
• /
• 제1권1호
• /
• pp.64-72
• /
• 1989

Laminar natural convection heat transfer from a horizontal heat exchanger tube with one infinitely long vertical plate fin has been studied by a finite-difference numerical procedure. In predicting convective heat transfer from a circular tube, the thermal boundary condition at solid fluid interface is usually assumed to be isothermal. However, in reality, the thermal boundary condition is not isothermal, and the tube has the thickness and the conductivity. So the temperature at the interface is not known a priori to the calculation. This problem has the conjugate phenomena which occur between the tube conduction and external natural convection, and between the fin conduction and external natural convection. Numerical results are obtained to determine the effects of the conductivity of solid wall and the thickness of tube wall on heat transfer. It is found that the conduction causes significant influence on the natural convection heat transfer at low K and high ${\delta}$.

• 대한기계학회논문집
• /
• 제11권2호
• /
• pp.279-286
• /
• 1987

본 논문에서는 수평관 내부의 체적평균온도를 가진유체의 난류강제대류에서 열전달이 일어나는 경우에 대하여 핀이 없는 수평전도관, 하향 핀이 부착된 수평전도 관 그리고 상향 핀이 부착된 수평전도관의 열전달 특성을 수치계산으로 연구하고 Mach -Zehnder 간섭계를 이용하여 실험하였고 수치해석과 실험결과를 비교하여 타당성을 확 인하였다.

• 한국연소학회:학술대회논문집
• /
• 한국연소학회 2012년도 제45회 KOSCO SYMPOSIUM 초록집
• /
• pp.115-118
• /
• 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.

• Journal of Advanced Marine Engineering and Technology
• /
• 제38권6호
• /
• pp.615-624
• /
• 2014

핀-튜브 열교환기는 산업용 보일러, 라디에이터, 냉동기 등에 많이 사용되고 있어 열교환기의 성능향상을 위한 다양한 연구가 진행되고 있다. 본 연구에서는 Plain형 핀-튜브 열교환기에 대해 가로피치, 와류발생기위치, 튜브표면의 돌기형상 및 돌기개수 등의 변화에 따른 열전달 및 압력강하 특성을 이론적으로 해석하였다. CFD 해석시 경계조건으로는 SST 난류모델을 적용하였으며, 튜브표면의 온도는 333 K이고, 입구측 공기의 온도와 속도는 423~438 K, 1.5~2.1 m/s로 가정하였다. 해석결과로는 열전달계수는 가로피치에 대한 영향은 큰 차이가 없으며, 열전달특성은 와류발생기 설치가 튜브 전방부에 위치할수록 양호한 것으로 나타났다. 또한 튜브표면의 돌기형상은 열전달 및 압력강하 특성에서 원형이 톱니형과 삼각형보다 적절하였으며, 16개 원형 돌기형상이 가장 양호하였다.

• 에너지공학
• /
• 제16권3호
• /
• pp.149-154
• /
• 2007

본 연구에서는 슬릿 휜-관 열교환기의 공기측 압력강하 특성을 실험적으로 고찰하였다. 물을 작동유체로 사용한 기존의 실험은 공기측 압력강하에 대해 일관된 방법을 제시하지 못하고 있다. 따라서 본 연구에서는 R22를 적용하여 휜-관 열교환기의 전표면과 습표면에 공기측의 압력강하 특성을 나타내는 표준 방법을 제시하고자 하였다. 기존의 실험 상관식과 본 연구에서 제시한 실험 데이터를 증발기와 응축기의 설계조건에서 레이놀즈수와 f-factor의 관계식으로 나타내었다. 본 실험은 공기의 속도가 $0.38{\sim}1.6\;m/s$ 일 때 냉매의 질량 유속 범위를 $150{\sim}250\;kg/m^2s$하여 수행하였다.

• 한국전산유체공학회:학술대회논문집
• /
• 한국전산유체공학회 2010년 춘계학술대회논문집
• /
• pp.163-166
• /
• 2010

Numerical analysis is conducted to design the high temperature heat exchanger of Stirling engine by using the commercial CFD solver FLUENT. The fin-tube type of heat exchanger numerical calculation is conducted by changing the shape, number and material of fin shape of working fluid channel, etc in three-dimensional combustion field. Adjusted one-way constant velocity is used as the representative velocity of oscillating flow. The optimum design of heat exchanger considering the heat trasfer capability is suggested by using the calculation results.

• 대한기계학회:학술대회논문집
• /
• 대한기계학회 2004년도 추계학술대회
• /
• pp.1046-1051
• /
• 2004

A plate-fin-tube heat exchanger used for a $SF_{6}$ gas-insulated transformer is extremely important since the dissipation of the heat generated from inside coils has a significant effect on the performance as well as the durability of the transformer. The heat exchanger consists of corrugated plate fins and staggered array tube bundles for coolant. In order to find out heat transfer and pressure drop characteristics, series of numerical analyses for plate fins with enhanced surface geometries were conducted. Based on the results of the numerical analyses, an improved model of the plate fin has been proposed.

• 설비공학논문집
• /
• 제12권4호
• /
• pp.414-421
• /
• 2000

This study was discussed about the thermal characteristics of finned tube heat exchanger having two row used in the air-conditioning application. Pressure drop and heat transfer coefficient were measured and investigated for the 3 times models of plain fin. Also the temperature distribution and heat conduction in the fin was measured by using the liquid crystal method. The surface temperature of rear row was nearly constant, and heat conduction in the fin was stronger near the front row than the rear row.