• 유체기계공업학회:학술대회논문집
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• 유체기계공업학회 2003년도 유체기계 연구개발 발표회 논문집
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• pp.245-250
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• 2003

In order to control indoor air quality and save energy, it is needed to install a suitable ventilation system equipped with heat exchanger for heat recovery. The purpose of this research is to find the performance of paper heat exchanger for exhaust heat recovery, which exchanges latent heat as well as sensible heat. Experimental apparatus comprises heat exchanger model, constant temperature and humidity chamber, fan and measurement systems for temperature, pressure and flow rate. Thermal performance and pressure loss of the paper heat exchanger are measured and compared at various air velocities and outdoor conditions. Experimental results show that paper heat exchanger can recover $50{\sim}70%$ of the enthalpy difference between supply and exhaust air.

• 설비공학논문집
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• 제20권6호
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• pp.372-380
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• 2008

In order to control indoor air quality and save energy, it is needed to install a suitable ventilation system equipped with heat exchanger for heat recovery. Paper heat exchanger can recover $50{\sim}70%$ of the enthalpy difference between supply and exhaust air. The purpose of this research is to obtain the experimental correlations for the friction factor, heat transfer coefficient, mass transfer coefficient and permeance of paper heat exchanger, which can be used to predict the performance of the paper heat exchanger. Pressure drops at various velocities, and sensible and latent heat transfer rates at various dry-bulb temperatures, relative humidities and specific humidities are measured to derive experimental correlations. The results of prediction using correlations show fairly good agreement with the experimental data obtained in the actual operating conditions.

• 설비공학논문집
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• 제2권2호
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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.

• 설비공학논문집
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• 제26권1호
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• pp.48-54
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• 2014

A refrigeration dehumidifier with a recuperative heat exchanger is theoretically analyzed. The recuperative heat exchanger is located between the two air streams from and to the dehumidifying coil, and reduces the sensible heat load in dehumidification process. A simple model is developed to predict performance of the dehumidifier. The model predicts that the recuperative heat exchanger is effective especially in the low humidity condition, where the sensible heat load is relatively large. It is predicted that, by adopting a recuperative heat exchanger, a maximum 30~110% increase in COP is possible for indoor air at $27^{\circ}C$, and 40~60% relative humidity.

• Journal of Advanced Marine Engineering and Technology
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• 제20권5호
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• pp.76-81
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• 1996

In this paper, a calculation method for fin efficiency of continuous fin is introduced. The continuous fin of in-line and staggered arrangement was divided into many sectors and fin efficiencies of each sectors were calculated by assuming that each sectors be the circular fins. To get the converged fin efficiency which is averaged by the each areas, the number of sectors was increased. The results were compared with equivalnet method by varying the aspect ratios in both cases of in-line and staggered tube arrangement and showed some differences of fin efficiencies.

• 설비공학논문집
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• 제9권4호
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• pp.517-526
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• 1997

This study is focused on the development and selection of the optimal cool tube system to maximize its thermal performance. Cool tube is devised to reduce the heating and cooling load of building by preheating or refreshing of intake air with buried pipes. Finite volume method is adopted to solve the conduction problem between the cool tube and earth. We examine the cool tube system for two operating periods, a short term(12 hours) and a long term(3 months). The results of short term operations reveal that condensation significantly influences and raises the exit air temperature. For long term operations, optimum conditions of cool tube system are obtained with variations of flow-rate, depth, length and diameter of cool tube.

• 대한기계학회논문집B
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• 제39권9호
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• pp.743-749
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• 2015

본 연구의 목적은 간접식 증발냉각 장치의 성능을 예측하고, 장치를 공기조화기의 배기열 회수에 적용하였을 경우의 에너지 절약효과를 분석하는 것이다. 플라스틱 열교환기를 사용한 간접식 증발냉각장치의 성능 상관식을 여러가지 조건에서 얻어진 실험 데이터로부터 구하였으며, 이 상관식을 이용하여 환기와 외기의 조건을 변화시켜가면서 장치의 성능변화를 예측하였다. 또한 간접식 증발냉각장치의 배기열 회수에 의한 에너지 절약효과를 우리나라 몇개 도시의 표준기상데이터를 사용하여 분석하였다. 여름철 배기열 회수를 위한 현열냉각장치의 사용율은 평균 44.3%이며 증발냉각장치의 사용율은 96.7% 이다. 증발냉각장치의 배기열 회수에 의한 에너지 절약은 현열냉각장치에 비해서 훨씬 높으며, 서울의 경우 약 3.89 배로 나타났다.

• 에너지공학
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• 제8권4호
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• pp.525-532
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• 1999

한국형 차세대 원자로는 ABB-CE사의 System 80+의 설계개념을 근간으로 하여 표준화된 원자로의 계통설계를 추진하고 있다. 본 연구에서는 차세대 원자로 정지냉각계통의 운전시 요구되는 인허가 요건등제반 조건을 충족시킬 수 있는지를 해석하였다. 또한 운전시 필요한 열교환기의 유효면적과 원자로 기기냉각수 유량등 기본적인 설계자료를 산출하여 차후 차세대 원자로 정지냉각계통의 상세설계 업부를 수행하는데 필요한 기초자료를 제시하여 핵증기공급계통 (NSSS)의 기술개발을 이루는데 목적이있다. 차세대 원자로는 울진 3, 4호기 열출력 2.825MWth 에 비해 열출력이 4,000MWth 로 증가되어 정지냉각계통의 관련서례자료를 새로 산출해야하므로 정지냉각계통의 냉각능력을 평가하는 KDESCENT 전산코드를 이용하여 원자로 노심의 잔열과 정지냉각계통의 현열을 제거할 수 있는 최소 유량을 제시하였으며 주요 구성기기인 열교환기, 펌프, 밸브 및 기타 기기의 기능 및 정지냉각계통의 운전절차를 고찰하였다.

• 대한기계학회논문집B
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• 제20권12호
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• pp.3938-3948
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• 1996

This study is related with the experimental investigation on the heat transfer and pressure drop characteristics of the fin-and-tube heat exchangers with three different interrupted fins and a plane fin for air-conditioning application. Experiments were conducted accordingly following the appropriate development process. Geometry similitude experiment was introduced to predict the performance of fins, and prototype experiment was also performed to confirm the validity of geometry similitude experimental results. However, these experimental results were limited to the sensible heat transfer characteristics of the heat exchangers. Hence, additional experiment was performed using refrigerant to investigate the latent heat transfer characteristics. This paper presents an appropriate process for the development of a new type heat exchanger. Sensible and latent heat transfer characteristics for each fin configuration is also provided along with the optimal fin configuration.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 춘계학술대회논문집B
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• pp.276-281
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• 2000

A simulation program using the mass transfer correlation was constructed to analyze 1-D simplified condensing flow across the tube bank. Higher efficiency was anticipated by reducing the flue gas temperature down below the dew point where the water vapor in the flue gas is condensed at the surface of the heat exchanger; that is, the heat transfer by the latent heat is added to that by the sensible heat. Thus, there can be an optimum operating condition to maximize the heat recovery from the flue gas. The temperature rises of the flue gas and the cooling water between the inlet and the outlet of the tube bank were compared with the experimental data reported previously. The predicted results agree well with the experimental data. Using this simulation program, the parametric studies have been conducted fur various operating conditions, such as the velocities and temperatures of the vapor/gas mixture and the cooling water, the number of the rows, and the conductivity of the wall material.