• 한국신재생에너지학회:학술대회논문집
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• 2010.11a
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• pp.88.2-88.2
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• 2010

고분자전해질연료전지(PEMFC)의 성능은 고분자막의 이온전도도에 따라 큰 영향을 받으며 가습조건에 따라 연료의 수화정도에 비례하여 증가하는 경향을 보인다. 현재 고분자막을 가습하는 방법에는 여러 가지가 있는데, PEMFC에 많이 사용되고 있는 Bubbler 형태의 가습장치는 고온이 필요하며 가습 효율이 수동적인 단점을 가지고 있다. 이에 비해서 막을 이용한 가습방법은 스택의 냉각시스템을 이용하여 가습 시, 별도의 에너지가 필요하지 않다. 이에 본 연구에서는 비교적 저온에서도 가습 효율이 증대하고 시스템 간소화의 장점을 가진 막가습기를 제작하여 고분자전해질 연료전지에서 열 및 습도조절에 대한 효율성을 비교 연구하였다. 막가습기에 사용된 가습막의 두께에 따른 가습도 변화 및 유로 구조에 따른 압력강화를 관찰하였으며 막가습기를 판형 모듈 형태로 제작하여 고분자전해질연료전지에 적용하여 성능을 평가하였다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.35 no.4
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• pp.337-344
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• 2011

The humidification of reactant gases is crucial for efficiently operating PEM (polymer electrolyte membrane) fuel cell systems and for improving the durability of these systems. The recycle of the energy and water vapor of exhaust gas improves the system performance especially in the case of automotive application. The available humidification methods are steam injection, nozzle spray, humidification by enthalpy wheel, membrane humidifier, etc. However, these methods do not satisfy certain requirements such as compact design, efficient operation and control. In this study, a hybrid humidification system consisting of a membrane humidifier and exhaust-air recirculation units was developed and the humidification performance of this hybrid humidifier was analyzed. Finally, a new practical method for optimal design of PEM-fuel-cell humidification system is proposed.

• Proceedings of the Korean Society of Marine Engineers Conference
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• 2006.06a
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• pp.21-22
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• 2006

디젤엔진에서 배출되는 배기가스 중의 주요 오염물질 중의 하나인 NOx(질소산화물)는 대부분 고온의 연소 과정에서 발생하고, 발생량은 연소온도에 따라 결정되는 것으로 알려져 있다. 또한 연료의 연소 중에 물이 첨가되면 연소공기의 비열 증가에 의하여 연소온도가 감소하여 NOx 발생량이 급격하게 감소하게 되는데, 연소실에 물을 첨가하는 방법으로는 유화연료, 직접물분사, 흡기가습 등이 있다. 이중 흡기가습은 구조가 간단하면서 NOx 저감효율이 가장 높은 것으로 알려져 있다. 본 연구는 당사 고유모델 중형엔진인 힘센엔진에 흡기가습 기술을 적용하여 연소성능 및 NOx 저감효과 등을 시험하고, 흡기가습 시스템의 상용화 모델 개발을 위한 기초 데이터를 확보하기 위해 수행되었다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.35 no.12
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• pp.1249-1255
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• 2011

In modern large-scale semiconductor manufacturing clean rooms, the energy consumed by the outdoor air-conditioning system during heating, humidification, cooling, and dehumidification of the incoming outdoor air represents about 45% of the total air-conditioning load required to maintain a clean-room environment. In particular, the energy required for humidification of the outdoor air in winter is very high. Therefore, evaluation and comparison of the energy consumption in key humidification systems, viz., steam-humidification and water-spray-humidification systems, used in outdoor air-conditioning systems would be useful to reduce the outdoor air-conditioning load in clean rooms. In the present study, an experiment with an outdoor air flow of 1000 $m^3$/h was conducted to compare the air-conditioning process and energy consumption in outdoor air-conditioning systems with electrodeboiler steam humidifiers and air-washer water spray humidification systems. The experimental results showed that the water-spray-humidification-type outdoor air-conditioning system consumed less electrical power than did the steam-humidification-type system and was more energy efficient during winter.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.18 no.3
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• pp.7-13
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• 2017

A comfortable indoor environment is important considering that many hours are spent in residential or office space. A humidifier is used to control the indoor humidity. In particular, an element type humidifier has the advantage of a simple structure and low energy consumption. Two types of humidifiers - stationary or rotor - are commonly used for residential purposes. In this study, performance optimization was conducted for a rotor-type humidifying element used in a residential humidifier. The optimization included the rotation speed, water submersion depth, etc. The test range consisted of an open area to the air from 57 to 90%, rotation speed from 0.2 to 2.0 rpm, frontal air velocity from 0.5 to 2.5 m/s. The results showed that the optimal open area to air was 70%. On the other hand, the effects of the rotation speed on the moisture transfer rate was negligible. On the other hand, the pressure drop increased with increasing rotation speed. As the frontal air velocity increased, both the moisture transfer rate and pressure drop increased. The humidification capacity of the present element was 0.08 ~ 0.31 kg/hr. A comparison of the data with the theoretical results was made.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.40 no.1
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• pp.55-63
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• 2016

New materials and shapes for a humidifying element were developed which outperformed the widely used crisscross glass wool Glasdek media design. The new material consists of 50% cellulose and 50% PET. The parallel channel configuration was devised to reduce excessive pressure loss caused by the reduced height (from 7.0 mm to 5.0 mm) of the crisscross configuration. For the same crisscross configuration, the humidification efficiency of the cellulose/PET element was 26% higher than that of the glass wool element. For the same cellulose/PET material, humidification efficiency of the parallel channel configuration was 14% higher than that of the crisscross configuration. As for the pressure drops, the cellulose/PET element was 2-52% higher than those of the glass wool element. For the same cellulose/PET material, the pressure drop of the parallel channel configuration was 14% higher than that of the crisscross configuration. Data were compared against the predictions from existing correlations and those by the proposed model.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.41 no.9
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• pp.579-586
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• 2017

In this study, new materials and shapes for a residential humidifying element were investigated. These elements could replace the current Japanese folded-type rayon/PE elements. Samples were taken from three different materials - rayon/PET (50:50), kraft/PET (40:60), kraft/PET/carbon. Results showed that the humidification efficiencies of the new samples were lower than those of the Japanese product. The efficiencies were 59% for the Japanese product (rayon/PET), 62% for kraft/PET and 84% for kraft/PET/carbon. This could be due to lower rayon or kraft content in the present samples than that in the Japanese product. However, pressure drops in the present samples were significantly lower than that in the Japanese product, due to improved channel configuration. The humidification capacity at the same pumping power ($j_m/f^{1/3}$) was 60% to 82% higher for the kraft/PET/carbon sample compared with the Japanese product. Furthermore, the results are compared with theoretical predictions.

• 한국신재생에너지학회:학술대회논문집
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• 2009.11a
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• pp.170-170
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• 2009

AIP(Air Independent Propulsion)시스템에 적용되는 연료전지 스택의 경우 연료의 이용율을 극대화시키는 것이 매우 중요하다. 일반적인 연료전지 스택은 물배출과 성능의 안정화를 위해 이론적 요구량보다 양론적으로 많은 양을 공급하여, 반응에 사용되지 않고 배출되는 연료 가스가 많아 이용율이 낮다. 여러 단으로 구성되어 전 단에서 사용하고 남은 연료 가스를 다음 단에 재공급하여 사용하는 케스케이드 구조의 연료전지 스택을 적용하게 되면 연료이용율을 90% 이상으로 높일 수 있다. 그러나 연료전지 스택에서 반응에 의해 발생한 물과 응축된 가습수가 재공급되면 연료전지 스택의 성능과 내구성에 악영향을 주는 플러딩현상이 발생하게 된다. 반면 반응수와 응축수를 제거할 때 스택에 재공급되는 연료 가스의 가습수가 같이 제거되면 낮은 가습도로 스택에 공급되는 문제점도 있다. 따라서 연료 가스의 가습도를 잘 유지하면서 액화된 물만 원활하게 제거할 수 있는 기액분리기의 개발이 필요하다. 본 연구에서는 CFD(Computational Fluid Dynamics)해석을 활용하여 다양한 디자인의 기액분리기를 설계하고 실험을 통해 각 디자인의 장단점을 분석하였다. 결과를 바탕으로 최적의 기액분리기를 개발하고 제작 및 평가를 통해 성능을 검증하였다.

• Proceedings of the SAREK Conference
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• 2004.06a
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• pp.210-210
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• 2004

• Korean Chemical Engineering Research
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• v.48 no.3
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• pp.382-390
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• 2010

In this research hydrogen sulfide, ammonia and toluene were designated as the representative source of malodor and VOC, respectively, frequently generated at the compost manufacturing factory and publicly owned facilities. The optimum operating condition to treat the waste air(2 L/min) containing malodor was constructed using photocatalytic reactor/biofilter process with humidifier composed of fluidized aerobic anf anoxic reactor. The ammonia(300 ppmv) of fed-waste air was removed by 22, 55 and 23% at the stage of photocatalytic reactor, humidifier and biofilter, respectively. The toluene(100 ppmv) of fed-waste air was removed by 20, 10 and 70% at the stage of photocatalytic reactor, humidifier and biofilter, respectively. Therefore the water-soluble ammonia and the water-insoluble toluene were treated mainly at the stage of humidifier and biofilter, respectively. In addition, hydrogen sulfide(10 ppmv) was almost treated at the stage of photocatalytic reactor and its negligible trace was absorbed in humidifier so that it was not detected before biofilter process. The nitrate concentration of the process water from anoxic reactor was found lower by 3 ppm than that from fluidized aerobic reactor. Besides, the dissolved ammonia-nitrogen concentration of the process water from humidifier remained at the high value of 1,500-2,000 ppm, which may be attributed to the existence of ammonium chloride and other source of ammonium nitrogen.