• 한국수소및신에너지학회논문집
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• 제29권1호
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• pp.11-18
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• 2018

A high efficiency integrated reforming system for improving the efficiency of the 5 kW PEMFC system used as the back up power of building was studied. The separated reforming system consisted of three parts - A steam reformer with two stage concentric circular shape, a heat exchanger type steam generator and a CO shift reactor. Temperature and steam carbon ratio (SCR) were control variables during operation. The operating conditions were optimized based on the thermal efficiency of the steam reformer as reformate gas composition changes at different temperature. In experiments, water was fully vaporized in the steam generator up to SCR 3.5 and the maximum thermal efficiency was achieved at the operating temperature around $700^{\circ}C$ in the steam reforming reactor. With the results of the separated reforming system research, we improved the shape of high efficiency integrated reformer. The performance evaluation of the integrated reformer was based on optimized operating conditions in SCR 3.5. As a result, the developed integrated reforming system maintained an efficiency of 76% and constant performance over 3,000 hours.

• Korean Chemical Engineering Research
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• 제49권5호
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• pp.516-520
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• 2011

휴대용 고분자전해질 연료전지의 수소발생용으로써 $NaBH_4$는 많은 장점을 갖고 있다. 본 연구에서는 $NaBH_4$ 가수분해 반응의 수소 수율에 대해 연구하였다. $NaBH_4$ 가수분해 반응의 수소 수율에 미치는 촉매 형태, 온도, $NaBH_4$ 농도, NaOH 농도 등의 영향에 대해 실험하였다. 촉매는 Co-P/Cu, Co-B/Cu와 Co-P-B/Cu를 사용하였는데 이들 촉매 종류에 따라 $NaBH_4$ 가수분해 반응의 수소 수율에 미치는 영향은 거의 없었다. $60^{\circ}C$ 이하의 온도에서 $NaBH_4$ 농도가 증가하면 부산물과 $NaBH_4$에 의해 겔이 형성되면서 가수분해 반응의 수소 수율이 감소였다. 겔 형성에 의해서 $NaBH_4$ 가수분해 반응 속도와 수소 총 발생량이 감소하였다. 안정화제인 NaOH를 첨가하면 겔 형성을 촉진해 수소 수율을 감소시켰다.

• 전기화학회지
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• 제9권2호
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• pp.89-94
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• 2006

Nafion/poly(ether(amino sulfone)) acid-base 블렌드 고분자 전해질 막을 제조하여 이온전도도, 디메틸 에테르(DME) 투과도를 측정하였으며 이를 이용하여 직접 DME 연료전지 특성을 연구하였다. Poly(ether(amino sulfone)) (PEAS)는 아민기의 치환도가 $0.6\sim2.0$인 것을 합성하였다. Nafion/PEAS 블렌드 전해질 막은 Nafion과 PEAS를 DMF에 용해시켜서 캐스팅하는 방법으로 제조하였다. 블렌드 전해질막은 $100^{\circ}C$ 이상에서도 이온전도도가 계속 증가하였다. Nafion/PEAS-0.6(85:15) 블렌드 전해질막은 $50^{\circ}C$ 이상에서의 수소 이온전도도가 recast Nafion보다 더 높게 나타났으며 $120^{\circ}C$에서의 수소 이온전도도는 $1.42\times10^{-1}S/cm$로 측정되었다. PEAS의 아민기가 많이 치환될수록 블렌드 전해질막의 DME 투과도와 이온전도도는 비례적으로 감소하는 것을 확인할 수 있었다. $100^{\circ}C$ 이상 가압 조건에서 Nafion/PEAS 블렌드 전해질막을 사용한 직접 DME 연료전지(DDMEFC)의 최대 전력밀도가 같은 조건에서 Nafion 115를 사용한 것보다 약 50%증가하였다. 이와 같은 DDMEFC의 성능 향상은 블렌드 전해질막이 Nafion과 비교하여 고온에서의 이온전도도가 향상되었고 DME투과도가 감소하였기 때문인것으로 해석된다.

• 한국세라믹학회지
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• 제43권12호
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• pp.812-822
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• 2006

This study amis to investigate the functional analysis of anode and cathode materials in Anode supported Solid Oxide Fuel Cell. The concentration polarization of single cell was investigated with CFD (Computational Fluid Dynamics) method for the case of the different morphology by using four types of unit cell and discussed to reduce the concentration polarization. The concentration polarization at anode side effected the voltage loss in Anode supported Solid Oxide Fuel Cell and increased contact areas between fuel gas and anode side could reduce the concentration polarization. For intermediate temperature operation, Anode-supported single cells with thin electrolyte layer of YSZ (Yttria-Stabilized Zirconia) were fabricated and short stacks were built and evaluated. We also developed diesel and methane autothermal reforming (ATR) reactors in order to provide fuels to SOFC stacks. Influences of the $H_2O/C$ (steam to carbon ratio), $O_2/C$ (oxygen to carbon ratio) and GHSV (Gas Hourly Space Velocity) on performances of stacks have been investigated. Performance of the stack operated with a diesel reformer was lower than with using hydrogen as a fuel due to lower Nernst voltage and carbon formation at anode side. The stack operated with a natural gas reformer showed similar performances as with using hydrogen. Effects of various reformer parameters such as $H_2O/C$ and $O_2/C$ were carefully investigated. It is found that $O_2/C$ is a sensitive parameter to control stack performance.

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2011년도 춘계학술대회 논문집
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• pp.1497-1498
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• 2011

• 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.

• Macromolecular Research
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• 제12권6호
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• pp.545-552
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• 2004

The long-term stability of sulfonic acid-containing polyimides has been investigated. The hydrolytic degradation of homopolyimide and the block copolyimide comprising $27\;mol\%$ of 2,2'-bis(trifluoromethyl)benzidine and $9\;mol\%$ of m-phenylenediamine (BTFMB27mPl0[7/(3+1)]), was quantified through viscosity measurements and FT-IR spectroscopic analyses. The viscosity decrease with respect to time and the degradation rate were similar. The degrees of degradation with respect to time under ambient conditions and at elevated temperature in water were monitored by FT-IR spectroscopy. A new absorption peak was observed at $1786\;cm^{-1},$ which we corresponds to the presence of anhydride end groups formed by hydrolytic scission of the imide rings.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 추계학술대회 초록집
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• pp.91.1-91.1
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• 2010

The Reforming system is an effective method to generate hydrogen which uses for fuel cell system. The purpose of this study is to present characteristics of an autothermal reformer at various operating conditions and to investigate ideal conditions for reforming efficiency. Dominant chemical reactions are Full Combustion, Steam Reforming reaction, Water-Gas Shift reaction and Direct Steam Reforming reaction. Operating parameters of the autothermal reformer are inlet temperature, Oxygen to Carbon Ratio, Steam to Carbon Ratio and Gas Hourly Space Velocity. Autothermal reformer is filled with catalysis of a packbed-bed type. Using numerical approach, we have investigated on various reaction conditions.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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• pp.328-330
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• 2009

1 kW class Polymer Electrolyte Fuel Cell(PEFC) co-generation systems have been developed from 2001 and evaluated for improvement of efficiency, durability and reliability of the system. This paper introduce new version system including with excellent reliability, durability and user friendly applications. Its electrical and overall efficiency showed 35 % and 80 %, respectively, and noise level of the system was less than 45 dB. In addition, this system have various functions such as load change, $N_2$ less purge, low emission and low temperature operation ($-15^{\circ}C$) through development of operation logic. This system was designed for convenient installation in indoor and outdoor due to the compactness of size and the separation of electrical and heat recovery units, which means a user can select the size of heat recovery unit.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 추계학술대회 논문집
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• pp.31-34
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• 2007

Fuel cell with high electric efficiency has many probabilities of commercial use. Especially, polymer electrolyte or proton exchange membrane fuel cell (PEMFC) which is a low operating temperature and has less influence on $CO_2$ concentration is considered the power generation system of small building and household. We calculated the optimal operational plans of 1 kW household PEMFC power system based on daily electric and heat demand patterns of various size of apartments. Calculated results show that the economic feasibility of PEMFC power system is very sensitive to the cost policy of electricity and natural gas.