• 대한기계학회논문집B
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• 제38권8호
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• pp.677-685
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• 2014

직접 탄소 연료전지(DCFC)는 석탄을 비롯한 탄소계 연료의 화학에너지를 직접 전기로 변환시킨다. 특히, 약 10 년 전에 고체산화물 전해질을 사용하고 연료극 매개체로 용융탄산염을 사용하는 고성능 직접탄소 연료전지 시스템이 제안되었다. 이 시스템의 경우, 운전 온도가 증가할수록 고체산화물 전해질의 이온 전도도가 향상되고 전기화학 반응이 활성화되어 성능이 향상되나, 연료극 매개체의 화학적인 안정성 문제발생이 우려된다. 본 연구에서는 탄소-탄산염 혼합 매개체의 고온 안정성을 이해하기 위한 일련의 실험을 수행하였다. 질소 또는 이산화탄소 분위기에서 카본블랙과 혼합된 $Li_2CO_3$와 $K_2CO_3$의 TGA 분석을 수행하였으며, 가열 과정에서 시료로부터 생성되는 가스 성분을 분석하였다. 이러한 결과를 해석하기 위하여, 탄산염의 열분해와 탄산염 등에 의하여 가속화되는 탄소 가스화 반응을 고려한 화학반응 모델을 제시하였으며, 실험 결과로부터 구한 매개체의 중량 손실과 가스 생성을 정성적으로 설명하였다.

• 한국수소및신에너지학회논문집
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• 제13권1호
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• pp.24-33
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• 2002

기존 Ni-10w/o Cr 연료극과 성능은 대등하면서 creep 저항성이 뛰어난 연료극을 제조하기 위하여 Ni-5w/o Al 합금 연료극의 제조 공정을 연구하였다. 소성 분위기에 따라 완전산화 방법과 부분산화 방법으로 나누어 제조된 전극들의 미세구조 변화를 관찰하였으며, 실험 결과 부분산화 방법으로 제조한 Ni-5w/o Al 합금 연료극이 가장 우수한 소결 및 creep 저항성을 나타내었다. 이는 연료극이 산화물 분산강화 구조를 갖기 때문으로 부분산화 방법으로 제조한 Ni-5w/o Al 합금 연료극을 장착한 단전지의 경우 기계적 안정성 및 전극 안정성이 향상되었다.

• 한국수소및신에너지학회논문집
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• 제28권2호
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• pp.156-165
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• 2017

This study quantitatively assessed the environmental impacts of fuel cell (FC) systems by performing life cycle assessment (LCA) and analyzed their energy efficiencies based on energy return on investment (EROI) and electrical energy stored on investment (ESOI). Molten carbonate fuel cell (MCFC) system and polymer electrolyte membrane fuel cell (PEMFC) system were selected as the fuel cell systems. Five different paths to produce hydrogen ($H_2$) as fuel such as natural gas steam reforming (NGSR), centralized naptha SR (NSR(C)), NSR station (NSR(S)), liquified petroleum gas SR (LPGSR), water electrolysis (WE) were each applied to the FCs. The environmental impacts and the energy efficiencies of the FCs were compared with rechargeable batteries such as $LiFePO_4$ (LFP) and Nickel-metal hydride (Ni-MH). The LCA results show that MCFC_NSR(C) and PEMFC_NSR(C) have the lowest global warming potential (GWP) with 6.23E-02 kg $CO_2$ eq./MJ electricity and 6.84E-02 kg $CO_2$ eq./MJ electricity, respectively. For the impact category of abiotic resource depletion potential (ADP), MCFC_NGSR(S) and PEMFC_NGSR(S) show the lowest impacts of 7.42E-01 g Sb eq./MJ electricity and 7.19E-01 g Sb eq./MJ electricity, respectively. And, the energy efficiencies of the FCs are higher than those of the rechargeable batteries except for the case of hydrogen produced by WE.

• 대한기계학회논문집B
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• 제41권11호
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• pp.727-734
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• 2017

이산화탄소의 농도를 줄이는 방법 중 하나로 전기화학을 이용하여 이산화탄소를 고부가 가치인 탄소로 전환하는 연구가 진행 중이다. 본 연구에서는 4.0 V, $600^{\circ}C$의 실험 조건에서 은, 니켈, 백금, 이리듐 전극을 사용하였다. 720분 동안 이산화탄소의 전환을 수행하였으며, 각 전극에서 생성된 탄소는 열중량 분석 및 XRD 분석을 수행하였다. 이산화탄소의 전환 및 생성 탄소의 양은 은, 백금, 니켈, 이리듐으로 나타났다. 열중량 분석을 통해 각 전극에서 생성된 탄소는 유사한 열 반응성을 가지며, XRD 분석을 통해 전극의 반응성에 따라 탄소의 결정성이 달라짐을 확인할 수 있었다. 은 전극은 전기화학적 전환 성능은 가장 높지만 약한 내구성을 보이며, 전극의 반응성 및 내구성을 고려하였을 때 백금이 4개의 재질 중에서 가장 적합함을 확인하였다.

• 한국재료학회지
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• 제11권8호
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• pp.666-670
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• 2001

용융탄산염 연료전지(MCFC)의 상용화에 있어서 가장 큰 문제점으로 지적되고 있는 분리판 wet-seal부의 내식성 향상을 위해 AISI 316L 스테인레스강에 Ni은 전기도금법으로, Y과 Al은 e-beam PVD법으로 피복하여 Ni/Y/Al충을 형성시켰다.$ 800^{\circ}C$ 환원분위기에서 5시간의 열처리를 통해 NiAlY 합금층을 얻을 수 있었으며, 그 후 $650^{\circ}C$ 용융탄산염내에서 as-received AISI 316L 스테인레스강과 200시간의 침지실험을 퉁해 내식성이 비교.평가되었다. SEM/EDS를 통한 단면 관찰 결과, Y의 첨가에 의해 치밀한 산화막을 형성하여 분리판 wet-seal부의 내식성을 향상시킬 수 있었다.

• 한국수소및신에너지학회논문집
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• 제16권2호
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• pp.170-179
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• 2005

Electrolyte loss is considered as one of the major obstacles limiting the life time of molten carbonate fuel cells (MCFCs). Unit cells with an effective area of 100 $cm^2$ were prepared and were operated to determine the optimum matrix thickness which contains the maximum amount of electrolyte without serious preformance loss caused by high resistance. Matrices with different thickness, 1.45, 1.8, and 2.3 mm, were used in unit cells and those cells were operared about 5000, 10000, and 4000 hrs. The unit cell used 1.8 mm thick matrix showed 0.85 V (at 150 mA/$cm^2$) as the intial performance and this cell voltage is not lower than the cell voltage obtained in the cell with 1 mm thick matrix. This cell was operated for 10000 hrs. The cell used 1.45 mm thick matrices showed 16.6 % in the electrolyte loss after 5000 hr operation. In the case of the cell with 2.3 mm thick matrix, the initial cell voltage was below 0.80 V (at 150 mA/$cm^2$). For thermal cycle test, the gas crossover amount of unit cell used 1.8 mm thick matrix was much less than that of the cell with 1.0 mm thick matrix.

• Journal of Electrochemical Science and Technology
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• 제9권3호
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• pp.195-201
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• 2018

To enhance the performance of cathodes at low temperatures, a Cu-coated cathode is prepared, and its electrochemical performance is examined by testing its use in a single cell. At $620^{\circ}C$ and a current density of $150mAcm^{-2}$, a single cell containing the Cu-coated cathode has a significantly higher voltage (0.87 V) during the initial operation than does that with an uncoated cathode (0.79 V). According to EIS analysis, the high voltage of the cell with the Cu-coated cathode is due to the dramatic decrease in the high-frequency resistance related to electrochemical reactions. From XPS analysis, it is confirmed that the Cu is initially in the form of $Cu_2O$ and is converted into CuO after 150 h of operation, without any change in the state of the Ni or Li. Therefore, the high initial cell voltage is confirmed to be due to $Cu_2O$. Because $Cu_2O$ is catalytically active toward $O_2$ adsorption and dissociation, $Cu_2O$ on a NiO cathode enhances cell performance and reduces cathode polarization. However, the cell with the Cu-coated cathode does not maintain its high voltage because $Cu_2O$ is oxidized to CuO, which demonstrates similar catalytic activity toward $O_2$ as NiO.

• 한국수소및신에너지학회논문집
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• 제20권1호
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• pp.31-37
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• 2009

An ejector is a machine utilized for mixing fluid, maintaining a vacuum, and transporting fluid. The Ejector enhances system efficiency, are easily operated, have a mechnically simple structure, and do not require a power supply. Because of these advantages, the ejector has been applied to a variety of industrial fields such as refrigerators, power plants and oil plants. In this work, an ejector was used to safely recycle anode tail gas in a 5 kW Molten Carbonate Fuel Cell system at KEPRI(Korea Electric Power Research Institute). In this system, the ejector is placed at mixing point between the anode tail gas and the cathode tail gas or the fresh air. Commercial ejectors are not designed for the actual operating conditions for our fuel cell system. A new ejector was therefore designed for use beyond conventional operating limits. In this study, the entrainment ratio is measured according to the diametrical ratio of nozzle to throat in the designed ejector. This helps to define important criteria of ejectors for MCFC recycling.

• 한국재료학회지
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• 제13권2호
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• pp.126-132
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• 2003

In order to evaluate the corrosion resistance at the anode side separator for molten carbonate fuel cell, STS316 and SACC-STS316 (chromium and aluminum were simultaneously deposited by diffusion into STS316 authentic stainless steel substrate by pack-cementation process) were applied as the separator material. In case of STS316, corrosion proceeded via three steps ; a formation step of corrosion product until stable corrosion product, a protection step against corrosion until breakaway occurs, a advance step of corrosion after breakaway. Especially, STS316 would be impossible to use the separator without suitable surface modification because of rapid corrosion rate after formation of corrosion product, occurs the severe problem on stability of cell during long-time operation. Whereas, SACC-STS316 was showed more effective corrosion resistance than the present separator, STS316 due to the intermetallic compound layer such as NiAl, Ni3Al formed on the surface of STS316 specimen. And it is anticipated that, in order to use SACC-STS316 alternative separator at the anode side, coating process, which can lead to dense coating layer, has to be developed, and by suitable pre-treatment before using it, very effective corrosion resistance will be achieved.

• 한국수소및신에너지학회논문집
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• 제19권5호
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• pp.367-376
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• 2008

To obtain the data of the pressure loss and differential pressure at the inside of the stack that was composed of 126 cells with 7,500 cm2 electrode area, 75kW molten carbonate fuel cell system has been operated. Computational fluid dynamics was applied to estimate reactions and thermal fluid behavior inside of the stack that was adopted with internal manifold type separator. The pressure loss coefficient K showed 72.29 to 84.01 in anode and 6.34 to 8.75 in cathode at low part of cells at the inside of 75 kW MCFC stack respectively. Meanwhile, the pressure loss coefficient of the higher part of cells at the interior of the stack showed 15.36 and 56.44 in anode and cathode respectively. These results mean that there is no big total pressure difference between anode and cathode at the inner part of 75 kW MCFC stack. This result will be reflected in 250kW MCFC system design.