• International Journal of Automotive Technology
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• 제7권7호
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• pp.867-872
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• 2006

Fuel cells are devices that convert chemical energy directly into electrical energy. Owing to the high efficiency of the fuel cells, a large number of research work have been done during these years. Among many kinds of the fuel cells, a polymer electrolyte membrane fuel cell is such kind of thing which works under low temperature. Because of the specialty, it stimulated intense global R&D competition. Most of the major world automakers are racing to develop polymer electrolyte membrane fuel cell passenger vehicles. Unfortunately, there are still many problems to be solved in order to make them into the commercial use, such as the thermal and water management in working process of PEMFCs. To solve the difficulites facing the researcher, the analysis of the inner mechanism of PEMFC should be implemented as much as possible and mathematical modeling is an important tool for the research of the fuel cell especially with the combination of experiment. By regarding some of the assumptions and simplifications, using the finite element technique, a two-dimensional electrochemical mode is presented in this paper for the further comparison with experimental data. Based on the principals of the problem, the equations of electronic charge conservation equation, gas-phase continuity equation, and mass balance equation are used in calculating. Finally, modeling results indicate some of the phenomenon in a unit cell, and the relationships between potential and current density.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2000년도 추계종합학술대회 논문집(2)
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• pp.349-352
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• 2000

In this paper, a SIMD 64bit MAC (Multiply -Accumulate) unit is designed. It is composed of two 32bit MAC unit which supports SIMD 16bit operations. As a result, It can process two 32bit MAC operations or four 16bit operations in one cycle. Proposed MAC unit is described in Verilog HDL. After functional verification is performed, MAC unit is synthesized and optimized with 0.35$\mu\textrm{m}$ standard cell library. The synthesis result shows that this MAC unit can operate at 80㎒ of clock frequency in 85$^{\circ}C$, 3.0V, worst case process and 125㎒ of clock frequency at 25$^{\circ}C$, 3.3V, typical case process. It achieves 320Mops of performance, and is suitable for embedded DSP processors.

• 신재생에너지
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• 제2권2호
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• pp.50-59
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• 2006

An experimental and numerical study is carried out to investigate the performance and the efficiency humidifying Membrane Electrolyte Assembly and having the double-layered catalyst in a fuel cell system which is taken into account the physical and thermal concept. Based on the principals of the problem, the equation of electronic charge conservation equation, gas-phase continuity equation, and mass balance equation are used for the numerical calculation. A unit cell for $200cm^2$ MEA is assembled and measured for finding better operational situation. After finding the optimal condition, 10 cell stacked PEMFC is fabricated. For the performance evaluation, V-I and power curves are examined in detail by changing the condition of humidity, temperature, pressure, thickness of catalyst and oxidant. It is found that the power is maximized around 500W at 80A.

• 전기화학회지
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• 제10권4호
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• pp.283-287
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• 2007

한국에너지기술연구원에서는 중온 ($700{\sim}800^{\circ}C$) 작동용 연료극 지지체 평관형 SOFC 스택을 구성하는 단위 번들을 개발했다. 연료극 지지체 평관형 셀은 Ni/YSZ 서밋 연료극 지지체 튜브, 8몰% $Y_2O_3$ stabilized $ZrO_2$ (YSZ) 전해질, $LaSrMnO_3$ (LSM)과 LSM-YSZ composite 및 $LaSrCoFeO_3(LSCF)$로 구성된 다중층 공기극으로 구성됐다. 제조된 연료극지지체 평관형 셀은 유도 브레이징 법에 의해 페리틱 (ferritic) 금속 캡에 접합됐고, 공기극의 전류집전을 위해 공기극 외부에 Ag 선 및 $La_{0.6}Sr_{0.4}CoO_3(LSCo)$ paste를 이용했으며, 연료극의 전류집전은 Ni felt, wire, 그리고 paste를 이용했다. 단위 번들을 만들기 위한 연료극 지지체 평관형 셀의 반응 면적은 셀 당 $90\;cm^2$ 이었으며, 2개의 셀이 병렬로 연결되어 1개의 단위 번들이 됐고, 총 12개의 단위 번들이 직렬로 연결되어 스택을 구성한다. 공기 및 3%의 가습된 수소를 산화제 및 연료로 사용한 단위 번들의 운전 결과 최대 성능은 $800^{\circ}C$에서 $0.39\;W/cm^2$의 출력이 나타났다. 본 연구를 통해 연료극 지지체 평관형 SOFC 셀의 기본 기술과 KIER 만의 독특한 연료극 지지체 평관형 SOFC 스택을 구성하는 단위 번들의 개념을 확립할 수 있었다.

• 한국수소및신에너지학회논문집
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• 제29권5호
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• pp.442-449
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• 2018

Research on High temperature polymer electrolyte fuel cell (HT-PEMFC) has actively been conducted all over the world. Since the HT-PEMFC can be operated at a high temperature of $120-180^{\circ}C$ using phosphoric acid-doped polybenzimidazole (PBI) electrolyte membrane, it has considerable advantages over conventional PEMFC in terms of operating conditions and system efficiency. However, If the thermal distribution is not uniform in the stack unit, degradation due to local reaction and deterioration of lifetime are difficult to prevent. The thin plate separator reduces the volume of the fuel cell stack and improves heat transfer, consequently, enhancing the cooling effect. In this paper, a large area flow field of thin plate separator for HT-PEMFC is designed and sub-stack is fabricated. We have studied stack performance evaluation under various operating conditions and it has been verified that the proposed design can achieve acceptable stack performance at a wide operating range.

• Korean Chemical Engineering Research
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• 제45권4호
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• pp.391-395
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• 2007

술폰화한 폴리에테르에테르케톤(sPEEK)과 나피온(Nafion) 아이오노머를 혼합한 새로운 전극 바인더를 제조하여 DMFC 용 음극 바인더로서 적용 가능성을 고찰하였다. 새롭게 제조한 혼합 바인더는 높은 수소 이온 전도도와 메탄올 전달 속도 및 낮은 용해도와 우수한 기계적 물성을 나타냈다. 이를 도입한 음극에서 혼합 바인더 함량에 따른 셀 성능을 고찰하였으며, 10 wt% 혼합 바인더를 도입한 음극으로 구성된 셀이 가장 우수한 성능을 나타냈다.

• 전기화학회지
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• 제5권1호
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• pp.27-29
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• 2002

본 연구는 메탄올과 공기를 이용하여 상온, 상압에서 전기를 발생시키는 휴대폰용 전원공급 장치의 개발에 관한 것이다. 이 장치는 직접 메탄을 연료전지(DMFC)와 Back-up전지가 병렬로 연결되어 있어, 통화시 소요 전력의 최대 $50\%$ DMFC가 공급하고 나머지 부분은 Back-up 전지가 공급한다. 또한 통화 대기시에는 DMFC가 $100\%$ 필요 전력을 공급하고, 잉여 전력으로 Back-up전지를 충전한다. 상기 DMFC는 유효면적이 $9cm^2$인 8개의 단위전지가 직렬로 연결되어 있으며, 휴대폰의 작동 전압 범위인 2.5-3.9V의 전압을 출력한다.

• 연구논문집
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• 통권23호
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• pp.45-56
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• 1993

In order to acquire more comprehensive understanding of textile composites, the processing-microstructure-performance relationships for a variety of material systems, reinforcing schemes and processing technologies should be established. In this paper, emphasis is placed on the integrated analysis of three-dimensional (3-D) 2-step braided composites. The analysis includes the geometric model of unit cells, identification of key process parameters and processing windows due to limiting geometries of yarn jamming, and prediction of elastic constants of the composite. The coordinate transformation and averaging of stiffness and compliance constants are utilized in the prediction of elastic constants. Since there are several types of unit cells in the thickness and width directions of the composites, characterization of mechanical properties is based upon the macro-cell, which occupies the entire cross-section and the unit pitch length of the sample. The performance map demonstrates that a wide range of elastic properties can be achieved by varying the geometric and process parameters.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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• pp.87.1-87.1
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• 2011

The residential Fuel Cell system has high efficiency of 85% with transferring natural gas to electrical power and heat, directly and it is a friendly environmental new technology in that $CO_2$ emission can reduce 40% compared with conventional power generator and boiler. The residential fuel cell system consists of two main parts which have electrical and hot storage units. The electrical unit contains a fuel processor, a stack, an inverter, a control unit and balance of plant(BOP), and the cogeneration unit has heat exchanger, hot water tank, and auxiliaries. 5kW class fuel process was developed and tested from 2009, it was evaluated for long-term durability and reliability test including with improvement in optimal operation logic. Stack development was crried out through improvement of design and evaluation protocol. Development of system controller was successfully accomplished through strenuous efforts and original control logic was optimized in 5kW class PEMFC system. In addition, we have been focused on development of system process and assembly technology, which bring about excellent improvement of reliability of system. The 5kW class PEMFC system was operated under dynamic conditions for 1,000 hours and it showed a good performance of total efficiency and durability.

• 한국환경보건학회지
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• 제22권3호
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• pp.98-102
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• 1996

This study investigated performance of the phenol degradation and reaction characteristics according to variation of phenol volumetric loading rates and dilution rates in suspension and PACT reactors using Pseudomonas sp. B3. 1. Removal efficiencies of the PAC unit indicated about 100 % with phenol volumetric loading rates from 0.4 phenol $kg/ma^3\cdot d$ to 1.2 phenol $kg/m^3\cdot d$, however, which of the suspension reactor showed about 100% with from 0.2 phenol $kg/m^3\cdot d$ to 0.75 phenol $kg/ma^3\cdot day$. 2. The cell density slightly was decreased from 298.2 mg/l to 272 mg/l, when dilution rate for suspension was reactor increased from 0.4 to 1.41 1/d, and also the cell density suddenly was decreased to 145.5 mg/l and was washed out at the dilution rate higher than 1.60 1/d. But the cell density for the PAC unit was linearly decreased with dilution rate of from 0.8 to 3.0 1/d, and showed 220.75 mg/l at maximum dilution rate. 3. The phenol utilization rate was increased from 0.008 to 0.031 phenol g/l$\cdot$h, when dilution rate for suspension reactor was increased from 0.4 to 1.5 1/d, however, the rate for the PAC unit was linearly increased from 0.017 to 0.061 phenol g/l$\cdot$h as variation changes from 0.017 to 0.061 phenol g/l$\cdot$h dilution rate.