• 한국마린엔지니어링학회:학술대회논문집
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• 한국마린엔지니어링학회 2005년도 후기학술대회논문집
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• pp.234-235
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• 2005

In this experiment study, to acquire elementary data for explaining to generate frost layer in the fin - tube evaporator. the experiment condition is to supply air on 0.3m/s, 0.6m/s, 0.9m/s and inlet air temperature is 15$^{circ}C$, 20$^{circ}C$, 25$^{circ}C$ , supplied air relative humidity is 70%, 80, 90%. And brine temperature in the copper tube was kept -15$^{circ}C$ because, generally cooling temperature range is constantly -15$^{circ}C$ in the heat exchanger for air conditioning system. in conclusion, through this experiment, we did compare with frost layer and frost thickness in each condition and examine these data

• 한국기계기술학회지
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• 제20권6호
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• pp.739-744
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• 2018

In this study, effects of reducing white smoke at a heat exchange system for white smoke reduction were studied in the winter season. For this purpose, the heat transfer processes on the exhaust air were investigated by Solidworks. Five wave heat exchangers of air-to-air and air-to-water type were applied for the exhaust air heat recovery. The analytical condition of the exhaust air was fixed and the computational analysis was performed according to the change of SA(supply air) inlet velocities. In order to evaluate the performance of the heat exchange system for white smoke reduction, W(water)/SA recovered capacities and the temperature/absolute humidity reduction rate were calculated. As SA inlet velocity increased, the exit temperature and absolute humidity of the mixing zone were reduced by up to about $40^{\circ}C$ and 0.12kg/kg respectively. Also, W/SA recovered capacities increased linearly up to about 35%.

• 한국마린엔지니어링학회:학술대회논문집
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• 한국마린엔지니어링학회 2005년도 전기학술대회논문집
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• pp.166-171
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• 2005

In this experiment study, to acquire elementary data for explaining to generate frost layer in the fin - tube evaporator. the experiment condition is to supply air on 0.3m/s, 0.6m/s, 0.9m/s and inlet air temperature is kept constantly $20^{\circ}C$, supplied air relative humidity is 70%, 80, 90%. And brine temperature in the copper tube was kept $-15^{\circ}C$ because, generally cooling temperature range is constantly $-15^{\circ}C$ in the heat exchanger for air conditioning system. in conclusion, through this experiment, we did compare with frost layer and frost quantity in each condition and examine these data

• 설비공학논문집
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• 제15권12호
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• pp.1049-1059
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• 2003

R410A is considered as an alternative refrigerant to R22 for air conditioners. An experimental investigation was made to study the characteristics of the heat transfer and pressure drop for R410A flowing in a fin-and-tube heat exchanger used for commercial air-conditioning units. Experiments were carried out under the conditions of inlet refrigerant temperature of 6$0^{\circ}C$ and refrigerant mass flux varying from 150 to 250 kg/$m^2$s for refrigerant side. The inlet air has dry bulb temperature of 35$^{\circ}C$, relative humidity of 40% and air velocity varying from 0.68 to 1.6 m/s. Experiments show that air velocity decreased by 16% is needed for R410A than that of R22 for subcooling temperature of 5$^{\circ}C$, which resulted in air-side pressure drop decrease of 15% for R410A as compared to R22. As a consequence, in order to provide the same design condition of a condenser, the fan requires lower electric-power consumption with R410A than that with R22.

• 설비공학논문집
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• 제15권7호
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• pp.595-603
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• 2003

R407C is considered as an alternative refrigerant to R22 for air conditioners. An experimental investigation was made to study the characteristics of the condensation heat transfer and pressure drop for R407C flowing in a fin-and-tube heat exchanger used for commercial air-conditioning units. Experiments were carried out under the conditions of inlet refrigerant temperature of 6$0^{\circ}C$ and refrigerant mass flux varying from 150 to 250 kg/$m^2$s for refrigerant side. The inlet air has dry bulb temperature of 35$^{\circ}C$ , relative humidity of 50% and air velocity varying from 0.8 to 1.6 m/s. Experiments show that air velocity increased by 25% is needed for R407C than that of R22 for subcooling temperature of 5$^{\circ}C$, which resulted in air-side pressure drop increase of 28.8% for R407C as compared to R22. As a consequence, in order to provide the same design condition of a condenser, the fan requires higher electric-power consumption with R407C than that with R22.

• 한국산학기술학회논문지
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• 제20권2호
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• pp.732-740
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• 2019

가습 소자를 이용한 증발식 가습은 건물이나 데이터 센터의 공조에 널리 사용되고 있다. 가습 소자의 성능은 가습 효율로 나타내는데 이 효율은 공기의 온습도나 물 온도에 무관하게 사용되고 있다. 본 연구에서는 데이터 센터와 건물 공조의 두 공기 조건에 대하여 셀룰로오스/PET, Glasdek의 두 소자를 사용하여 전벙 풍속과 물 온도를 변화시키며 일련의 실험을 수행하였다. 실험 결과 측정된 가습 효율은 공기 조건과 물 온도에 따라 다르게 나타났다. 심지어 건물 조건에서는 소자의 입구부에서 감습이 나타나기도 하였는데 그 이유는 공급수 온도가 입구 공기의 노점온도보다 낮았기 때문이었다. 건물 조건에서는 공급수 온도와 공기의 노점 온도 차이가 증가할수록 가습 효율은 감소하였다. 이로부터 가습 효율 모델을 적절히 세우려면 길이 방향으로 수분 전달량이 변화하는 입구 영역에 대한 해석이 중요하다고 판단된다. 셀룰로오스/PET 소자에 대하여 성능 해석을 수행한 결과 Sherwood 수는 적절히 예측하였으나 마찰 손실은 과대 예측하였다. 이는 해석시 채널 형상을 단순한 삼각형으로 가정하고 소자 표면에 형성된 액막의 영향을 무시한 때문으로 판단된다.

• 공업화학
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• 제19권1호
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• pp.73-79
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• 2008

본 연구에서는 핀-관 열교환기의 공기측 열전달, 마찰 그리고 물질특성을 조사하기 위하여 6종의 열교환기에 대하여 습조건에서 실험을 수행하였다. 실험에 사용된 핀은 루버형으로 핀피치, 관 열수 그리고 입구상대습도를 변화하였다. 루버핀-관 열교환기의 열전달계수와 마찰계수는 레이놀즈 수가 증가할수록 감소하였으며, 핀피치가 줄어들수록 열전달계수는 감소하였고 마찰계수는 증가하였다. 3열 열교환기의 열전달계수와 마찰계수의 핀피치 변화에 따른 영향은 2열 열교환기의 경우보다 덜 민감하였다. 그리고 유입공기의 상대습도에 대한 열전달계수와 마찰계수의 변화폭은 크지 않았다. 또한, 루버핀-관 열교환기의 물질전달계수는 핀피치가 감소할수록 줄어들었으나, 레이놀즈 수 변화에 따른 물질전달계수는 열전달계수와는 달리 관 열수에 따라 서로 다른 경향을 보였다. 유입공기의 상대습도가 높아질수록, 물질전달계수는 다소 줄어 들었다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2008년도 추계학술대회B
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• pp.3140-3141
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• 2008

The output power efficiency of the fuel cell system depends on the demanded current, stack temperature, air excess ratio, hydrogen excess ratio and inlet air humidity. Thus, it is necessary to determine the optimal operation condition for maximum power efficiency. In this paper, we developed a dynamic model of fuel cell system which contains mass flow model, diffusivity gas layer model, membrane hydration and electrochemistry model. In order to determine the maximum output power and minimum use of hydrogen in a certain power condition, response surface methodology (RSM) optimization based on the proposed PEMFC stack model is presented. The results provide an effective method to optimize the operation condition under varied situations.

• 한국수소및신에너지학회논문집
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• 제19권2호
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• pp.103-110
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• 2008

The most failure mode of PEM fuel cell is gas crossover caused by pinhole formation in MEAs. The degradation phenomena of MEA with pinholes were evaluated in various accelerated operation condition, such as OCV, low humidity and high partial pressure of oxygen. The performances of MEA with pinholes were almost same before and after normal 144 hours operation($70^{\circ}C$, $640mA/cm^2$, 65%RH $H_2/air$). The results of accelerated operation showed that OCV and low humidity condition more deteriorated MEA than gas crossover owing to pinholes. When oxygen was used as cathode gas, the pinholes of MEA were enlarged due to heat of combustion reaction on Pt catalyst of electrodes. This combustion reaction occurred at pinholes near gas inlet and resulted in local MEA failure.

• Journal of Advanced Marine Engineering and Technology
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• 제23권5호
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• pp.687-694
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• 1999

This study was conducted to develop new drying process for automatic control and marine engi-neering system. Air-water tests were carried out to investigate dryer performance. The dispersed flow in he dryer test apparatuses was also simulated by using a numerical code which solves the Dittus-Boelter equation for continuous liquid phase and the Reynolds equation of droplet motion for continuous liquid phase and the Reynolds equation of droplet motion for dispersed phase to predict droplet removal efficiency. Proper conditions for dehumidification were optimized by response ambient conditions. When the selected indexes were constrained in the range of 85-98% moisture content above $15^{\circ}$ and more than mass flow rates of moist air 750kg/h. The numerical results were compared with the experimental data pertaining to the removal effi-ciency at chamber stage and overall pressure drop along concentric tubes Good agreement was obtained as for the efficiency while relatively poor agreement was obtained for the relative humidity. The results also showed that the efficiency depended strongly on the relative humidity at the inlet condition which indicated the importance of estimating the heat exchanger length. Effects of some design parameters in both removal efficiency and breakthrough onset condition are discussed.