• 제목/요약/키워드: Membrane inlet

검색결과 119건 처리시간 0.025초

이온 교환막 연료전지용 막 가습기의 물질전달 성능 실험 (Experimental Analysis of Mass Transfer Capability of Membrane Humidifier for PEMFC)

  • 탁현우;김경택;임석연;유상석
    • 한국수소및신에너지학회논문집
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    • 제23권1호
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    • pp.19-25
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    • 2012
  • The efficiency and life time of the Proton Exchange Membrane fuel cell (PEMFC) system is critically affected by incoming gas with humidity which should be maintained properly at normal operating conditions. Typically, incoming gas of automotive fuel cell is humidified by external humidifier but the characteristics of device is rarely reported. In this study, characteristics of water transfer in the membrane humidifiers have been experimentally investigated for flow rates of gas and for different flow arrangement under steady state condition. At first, capability of mass transfer through the membrane is examined at constant temperature. Then, the temperature distribution effect on the capability of mass transfer is tested over various inlet conditions. In summary, this research presents the mass transfer capability of hydrophilic membrane over various operating conditions.

날숨이 혼합된 물을 사용한 압축기없는 용존기체 분리기의 분리 특성 (Separation characteristics of separation devices using inlet water mixed with exhalation gases without a compressor)

  • 허필우
    • Journal of Advanced Marine Engineering and Technology
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    • 제40권9호
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    • pp.842-846
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    • 2016
  • 물속의 용존산소를 이용하면 물고기가 아가미를 이용하여 호흡하듯이 사람이 수중에서 호흡이 가능하지만, 물속에 포함된 용존산소의 양이 적기 때문에 필요한 산소량을 확보하는 문제가 해결되어야 한다. 우선 물의 유량을 증가시켜 분리되는 산소량을 증가하는 것이 가능하지만, 필요한 펌프와 멤브레인 그리고 주변기기의 용량 증가로 분리장치의 부피와 무게 그리고 소요비용도 함께 증가하게 된다. 이러한 문제를 효과적으로 해결하기 위해 많은 양의 산소를 포함하는 날숨의 특성을 이용하면 필요한 산소량을 효과적으로 확보할 수 있다. 일반적으로 날숨에 포함된 산소량은 공기보다 낮고, 이산화탄소 량은 공기보다 많은 것으로 알려져 있다. 본 연구에서는 용존기체 분리장치의 입력 단에 날숨을 혼합한 후, 용존기체 분리장치에서 산소를 포함하는 용존기체를 재분리하는 과정을 거치며, 이때, 입력단에 설치된 수중펌프의 동작으로 수압이 증가하므로, 이러한 수압을 갖는 물에 날숨을 혼합하기 위해서는 압축기가 요구되므로 분리장치의 무게와 부피 그리고 소비 전력이 증가하게 된다. 본 연구에서는 입력단의 압력을 감소시킴으로써 압축기를 사용하지 않고도 날숨을 물에 혼합하는 구조를 갖는 것이 특징이다. 실험을 통해 압축기를 사용하지 않고 날숨이 입력단의 물에 혼합되는 것이 가능함을 제시하였으며, 날숨이 입력단에 공급된 후 분리장치를 통해 분리된 기체의 분리특성을 제시하였다. 날숨을 사용함으로써 용존기체의 분리량이 크게 증가하였으며, 공급되는 날숨의 유량이 증가하면 분리되는 용존 기체의 양도 증가하였다.

수송용 연료전지 시스템 적용을 위한 기체-기체 막가습기 구조 최적화 (Structural Optimization of Gas-to-gas Membrane Humidifier for Fuel Cell Vehicle)

  • 이무석;김경주;신용철;김동현;서상훈;김현유
    • 한국수소및신에너지학회논문집
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    • 제21권2호
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    • pp.111-116
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    • 2010
  • In this study, the structural analysis was performed to optimize the membrane humidifier with hollow fiber membrane for polymer electrolyte membrane fuel cell system. The main design factors were considered by evaluating the humidifying performance according to various structural parameters such as packing density and length. The effects of operation conditions of membrane humidifier were also elucidated experimentally. Results imply that there are optimum points for the packing density and length of humidifier. It was also found that among operation conditions, relative humidity of wet exhaust gas and temperature of dry inlet gas have major effects on the humidifying performance.

중공사막을 적용한 2단 멤브레인 하이브리드 반응기에 의한 톨루엔 제거 (Removal of toluene using the 2-stage hollow fiber membrane-hybrid reactor)

  • 김진성;구소희;김태형;이명주;황선진
    • 상하수도학회지
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    • 제24권3호
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    • pp.287-293
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    • 2010
  • In this study, the toluene gas in VOCs was removed using bioreactor which applied with hollow fiber membrane and Pseudomonas sp. TDB-4. The EBRT of each reactor are controlled 60 sec(R-1) and 30 sec(R-2) and inlet tolune concentration of both R-1 and R-2 is controlled from 25ppm to 500 ppm. Up to 500 ppm of toluene concentration, the toluene removal efficiency of R-1 and R-2 are 92% and 81%, and theirs removal capacities are about 100 g/$m^3$/hr and 180 g/$m^3$/hr, respectively. In addition, according to this study, toluene removal efficiencies at the hollow fiber are approximately 70%(60 sec) and 45%(30sec).

Oxygen Transfer Rate Coefficient of Membrane Aeration Bioreactor for Vero Cell Culture

  • 전주미;정연호;김익환;이상종;장용근;전계택
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2002년도 생물공학의 동향 (X)
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    • pp.269-270
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    • 2002
  • Oxygen is a key substrate in animal cell metabolism and its consumption is thus a parameter of great interest for monitoring and control in animal cell culture bioreactor. The use of a gas-permeable membrane offered the possibility to provide the required quantity of oxygen into the culture. while avoiding problems of foaming or shear damage generally linked to sparging. For determining the optimum DO control strategy of this gas-permeable membrane aeration bioreactor, the oxygen transfer rate coefficient was measured with varying $N_2$ ratio in inlet air. The results showed that an increasing mass flow rate of nitrogen reduced the $K_La$ value. and 5% nitrogen in air did not result in any oxygen limitation.

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열공압 방식의 Polydimethylsiloxane 마이크로 밸브의 제작 및 특성 (Fabrication and Characteristics of Thermopneumatic-Actuated Polydimethylsiloxane Microvalve)

  • 김진호;조주현;한경희;김영호;김한수;김용상
    • 대한전기학회논문지:전기물성ㆍ응용부문C
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    • 제53권4호
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    • pp.231-236
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    • 2004
  • A normally open thermopneumaticc-actuated microvalve has been fabricated and their properties are investigated. The advantages of the proposed microvalve are of the low cost fabrication process and the transparent optical property using polydimethylsiloxane (PDMS) and indium tin oxide (ITO) glass. The fabricated microvalves with in-channel configuration are easily integrated with other microfluidic devices on the same substrate. The fabrication process of thermopneumatic-actuated microvalvesusing PDMS is very simple and its performance is very suitable for a disposable lab-on-a-chip. The PDMS membrane deflection increases and the flow rates of the microchannel with microvalvels decrease as the applied power to the ITO heater increases. The powers at flow-off are dependent on the membrane thickness and the applied inlet pressure but are independent of the channel width of microvalves. The flow rate is well controlled by the switching function of ITO heater and the closing/opening times are around 20 sec and 25 sec, respectively.

Development of a Peristaltic Micropump with Lightweight Piezo-Composite Actuator Membrane Valves

  • Pham, My;Goo, Nam-Seo
    • International Journal of Aeronautical and Space Sciences
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    • 제12권1호
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    • pp.69-77
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    • 2011
  • A peristaltic micropump with lightweight piezo-composite actuator (LIPCA) membrane valves is presented. The micropump contained three cylinder chambers that were connected by microchannels and two active membrane valves. A circular miniature LIPCA was developed and manufactured to be used as actuating diaphragms. The LIPCA diaphragm acted as an active membrane valve that alternate between open and closed positions at the inlet and outlet in order to produce high pumping pressure. In this LIPCA, a lead zirconium titanate ceramic with a thickness of 0.1 mm was used as an active layer. The results confirmed that the actuator produced a large out-of-plane deflection. During the design process, a coupled field analysis was conducted in order to predict the actuating behavior of the LIPCA diaphragm; the behavior of the actuator was investigated from both a theoretical and experimental perspective. The active membrane valve concept was introduced as a means for increasing pumping pressure, and microelectromechanical system techniques were used to fabricate the peristaltic micropump. The pumping performance was analyzed experimentally in terms of the flow rate, pumping pressure and power consumption.

Membrane Inlet-based Portable Time-of-flight Mass Spectrometer for Analysis of Air Samples

  • Kim, Tae-Kyu;Jung, Kyung-Hoon;Yoo, Seung-Kyo;Jung, Kwang-Woo
    • Bulletin of the Korean Chemical Society
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    • 제26권2호
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    • pp.303-308
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    • 2005
  • A miniaturized time-of-flight mass spectrometer with an electron impact ionization source and sheet membrane introduction has been developed. The advantages and features of this mass spectrometer include high sensitivity, simple structure, low cost, compact volume with field portability, and ease of operation. A mass resolution of 400 at m/z 78 has been obtained with a 25 cm flight path length. Under optimized conditions, the detection limits for the volatile organic compounds (VOCs) studied were 0.2-10 ppm by volume with linear dynamic ranges greater than three orders of magnitude. The response times for various VOCs using a silicone membrane of 127 $\mu$m thickness were in the range 4.5-20 s, which provides a sample analysis time of less than 1 minute. These results indicate that the membrane introduction/time-of-flight mass spectrometer will be useful for a wide range of field applications, particularly for environmental monitoring.

UF와 디스크필터를 전처리시설로 이용한 역삼투압해수담수설비의 평가 (Evaluation of Seawater Reverse Osmosis Desalination System with UF and Disk Filter as Pre-Treatment)

  • 양근모;임동훈;김준하;정형호
    • 대한기계학회논문집 C: 기술과 교육
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    • 제1권1호
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    • pp.59-68
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    • 2013
  • 본 연구에서는 한외여과막과 역삼투압막으로 이루어진 해수담수화장치를 구성하였다. 해수를 취수하여 디스크필터와 한외여과막을 이용한 전처리설비를 통과시켜 생산한 전처리수의 $SDI_{15}$와 탁도를 측정하여 역삼투압해수담수설비에 적합함을 밝혔다. 역삼투압해수담수설비의 부산물인 브라인을 전처리수와 혼합하여 역삼투압해수담수설비의 입구농도를 변화시켰다. 농도 변화실험에서, 해수농도가 역삼투압해수담수설비의 성능에 끼치는 영향을 실험으로 구하였다. 염배제율, 회수율, 생산수의 수질은 입구농도에 따라 많은 변화가 있었으며, 에너지소비량도 입구농도에 거의 선형적으로 상승하는 것을 실험으로 구하였다.

고온형 고분자전해질형 연료전지에서의 사형 유로와 평행 유로 성능비교에 대한 수치해석적 연구 (Numerical Study on Comparison of Serpentine and Parallel Flow Channel in High-temperature Proton Exchange Membrane Fuel Cells)

  • 안성하;오경민;주현철
    • 한국수소및신에너지학회논문집
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    • 제29권1호
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    • pp.41-55
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    • 2018
  • General polymer electrolyte fuel cell (PEMFC) operates at less than $80^{\circ}C$. Therefore liquid phase water resulting from electrochemical reaction accumulates and floods the cell which in turn increases the mass transfer loss. To prevent the flooding, it is common to employ serpentine flow channel, which can efficiently export liquid phase water to the outlet. The major drawback of utilizing serpentine flow channel is the large pressure drop that happens between the inlet and outlet. On the other hand, in the high temperature polymer electrolyte fuel cell (HT-PEMFC), since the operating temperature is 130 to $180^{\circ}C$, the generated water is in the state of gas, so the flooding phenomenon is not taken into consideration. In HT-PEMFCs parallel flow channel with lower pressure drop between the inlet and outlet is employed therefore, in order to circulate hydrogen and air in the cell less pumping power is required. In this study we analyzed HT-PEMFC's different flow channels by parallel computation using previously developed 3-D isothermal model. All the flow channels had an active area of $25cm^2$. Also, we numerically compared the performance of HT-PEMFC parallel flow channel with different manifold area and Rib interval against the original serpentine flow channel. Results of the analysis are shown in the form of three-dimensional contour polarization curves, flow characteristics in the channel, current density distribution in the Membrane, overpotential distribution in the catalyst layer, and hydrogen and oxygen concentration distribution. As a result, the performance of a real area fuel cell was predicted.