• 한국세라믹학회지
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• 제45권12호
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• pp.772-776
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• 2008

The Korea Electric Power Research Institute (KEPRI) has been developing planar solid oxide fuel cells (SOFCs) and power systems for combined heat and power (CHP) units. The R&D work includes solid oxide fuel cell (SOFC) materials investigation, design and fabrication of single cells and stacks, and kW class SOFC CHP system development. Anode supported cells composed of Ni-YSZ/FL/YSZ/LSCF were enlarged up to $15{\times}15\;cm^2$ and stacks were manufactured using $10{\times}10\;cm^2$ cells and metallic interconnects such as ferritic stainless steel. The first-generation system had a 37-cell stack and an autothermal reformer for use with city gas. The system showed maximum stack power of about $1.3\;kW_{e,DC}$ and was able to recover heat of $0.57{\sim}1.2\;kW_{th}$ depending on loaded current by making hot water. The second-generation system was composed of an improved 48-cell stack and a prereformer (or steam reformer). The thermal management subsystem design including heat exchangers and insulators was also improved. The second-generation system was successfully operated without any external heat source. Under self-sustainable operation conditions, the stack power was about $1.3\;kW_{e,DC}$ with hydrogen and $1.2\;kW_{e,DC}$ with city. The system also recuperated heat of about $1.1\;kW_{th}$ by making hot water. Recently KEPRI manufactured a 2kW class SOFC stack and a system by scaling up the second-generation 1kW system and will develop a 5kW class CHP system by 2010.

• 한국수소및신에너지학회논문집
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• 제24권5호
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• pp.401-412
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• 2013

The paper is to study on the simulation of the micro/macroscale thermo-electrochemical model of a single cell of anode-supported SOFC with direct internal reforming. The coupled heat and mass transport, electrochemical and reforming reactions, and fluid flow were simultaneously simulated based on mass, energy, charge conservation. The micro/macroscale model first calculates the detailed electrochemical and direct internal reforming processes in porous electrodes based on the comprehensive microscale model and then solve the macroscale processes such as heat and mass transport, and fluid flow in SOFCs with assumption of fully-developed flow in gas channel. The simulation results evaluate the overall performance by analyzing distributions of mole fraction, current density, temperature and microstructural design in co/counter flow configurations.

• Korean Membrane Journal
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• 제8권1호
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• pp.13-20
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• 2006

The production of CO-free hydrogen streams for feeding PEM-Fuel Cells using catalytic zeolite membrane reactors was analysed by means of selective oxidation. Tubular FAU (Na-Y) zeolite membranes, prepared by a secondary growth method and Pt-loaded, were used in a flow-through MR configuration. The catalytic tests were carried out at $200^{\circ}C$ and at different pressures with a simulated dry reformate shifted gas mixture ($H_2$ ca. 60%, CO 1 %, plus $O_2,\;N_2,\;CO_2$). The operative $O_2/CO$ stoichiometric equivalent feed ratio was ${\lambda}= 2$. These catalytic tests, reducing the CO concentration down to $10{\sim}50$ ppm, verified the possibility of MR integration after using a low temperature water-gas shift unit of a fuel processor to convert hydrocarbons into hydrogen-rich gas.

• 한국수소및신에너지학회논문집
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• 제23권4호
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• pp.293-299
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• 2012

The serpentine flow channel is widely used in polymer electrolyte membrane fuel cells (PEMFCs) to prevent flooding phenomena because it effectively removes liquid water in the flow channel. The pressure drop between inlet and outlet increases as compared with straight channels due to minor losses associated with the corners of the turning configurations. This results in a strong pressure gradient between adjacent channels in specific regions, where some amount of reactant gas can be delivered to catalyst layers by convection through a gas diffusion layer (GDL). The enhancement of the convective flow in the GDL, so-called bypass flow, affects fuel cell performance since the bypass flow influences the reactant transport and thus its concentration over the active area. In the present paper, for the bipolar plate design, a simple analytic model has been proposed to predict the bypass flow in the serpentine type flow channels and validated with three-dimensional numerical simulation results.

• 한국기계가공학회지
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• 제21권1호
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• pp.66-72
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• 2022

The Mooney-Rivlin second order optimal strain energy function derived through uniaxial tensile test and analysis was applied to a gasket to confirm the internal stress and surface pressure generated during compression. The Taguchi method, a statistical technique, was used to design the optimum shape of the gasket, and through characteristic evaluation, the optimum shape of the gasket was obtained when the reference plane (T: 0.15 mm), contact surface (W: 1.00 mm), and curvature (R: 0.30 mm) were used. It was determined that the optimum shape yields a von Mises stress of 4.83 MPa, and the contact pressure stress is 20.14 MPa, which satisfies breakage and sealing requirements. In the future, we plan to manufacture a jig that can measure surface pressure to conduct comparative verification studies between the test results and analysis results.

• 한국수소및신에너지학회논문집
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• 제34권2호
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• pp.196-204
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• 2023

This study performed the numerical analysis of the internal flow phenomena of 1 kWe-class solid oxide fuel cell (SOFC) stacks with internal manifold type and planar cells using commercial computational fluid dynamics (CFD) software, Star-CCM+. In particular, the locations where the turbulent phenomena occur inside the SOFC stack were investigated. In addition, the laminar flow model and the standard k-ε turbulent model were used to calculate the SOFC stack, separately. And, the calculation results of both laminar and turbulent models were compared. The calculation results showed that turbulent phenomena occurred mainly in the cathode flow. Especially, the turbulent phenomena were found in the cathode inlet/outlet region, and local turbulence occurred in the end plate near the inlet pipe.

• 한국수소및신에너지학회논문집
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• 제34권2호
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• pp.212-225
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• 2023

This study presents a modularized process of a hybrid renewable energy system that combines photovoltaic power and wind power to supply stable power in a unit area (1 km²). The water electrolysis process and fuel cells process also contributes to the supply of the stable power. The entire system can constantly supply power of 4.39 MW/km². Actual meteorological data is used for simulation.

• 한국수소및신에너지학회논문집
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• 제6권2호
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• pp.53-63
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• 1995

차세대의 새로운 발전방식인 용융탄산염형 연료전지 시스템개발 사업중 실용 스택개발을 위하여 전극유효연적이 $100cm^2$ 인 단위전지를 10단 적층한 Cross Flow형 MCFC스택을 제작하고 2성능측정설비를 구성하여 장기운전시험을 실시하였다 연료로는 $H_2/CO_2/H_2O$의 비율을 72%/18%/10% 로 조성한 가스를 이용하고 산화제가스로는 $O_2/CO_2$ 및 $Air/CO_2$ 비율이 33%/67%, 70%/30%가 되는 가스를 이용하여 운전할때의 초기성능 및 15A($150mA/cm^2$) 정부하 상태에서의 장기운전시험시의 전압 강하율을 조사하였다. 운전시간 310시간이 경과된 후의 스택전압은 8.39V이었고 이때의 출력은 125.8W를 보여주었다. 한편 1845시간이 경과한후 공기를 산화제로 이용하는 경우 전압은 6.95V로서 출력 104W를 나타내고 있다. 초기성능치에 의한 에너지 변환효율은 이용율이 40%인 경우 29.65%이었고 80%로 증가하는 경우 약 51.5%가 된다. 1840시간의 경과한때 까지의 전압 강하율은 약 52.4mV/1000hr로서 이전의 스택보다는 전압강하율이 감소되고 있으며 스택의 성능 저하의 주요한 요인은 개회로 전압의 저하로 내부단락동에서 기인하는 것으로 여겨진다. 또한 장기운전사 스택내부에서의 단위전지 전압분포가 균일하지 않음을 알 수 있어 이에 대한 개선을 필요로 한다.

• 전기화학회지
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• 제25권4호
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• pp.174-183
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• 2022

높은 에너지 밀도와 고순도 수소 생산의 측면에서 고분자 전해질 연료전지와 수전해가 주목받고 있다. 고분자 전해질 연료전지 및 수전해를 위한 촉매층은 귀금속 계열의 전기 촉매와 이오노머 바인더로 구성되어 있는 다공성 전극이다. 이 중 이오노머 바인더는 촉매층 내 이온 전도를 위한 3차원 네트워크 형성과 전극 반응에 필요한 또는 생성되는 물질들의 이동을 위한 기공 형성에 중요한 역할을 수행한다. 상용 과불소계 이오노머의 활용 측면에서 이오노머의 함량, 이오노머의 물성, 그리고 이를 분산시킬 분산 매체에 촉매층의 성능 및 내구성이 크게 달라진다. 현재까지 고분자 전해질 연료전지용 촉매층을 위한 이오노머의 활용 방법은 많은 연구가 진행되어왔으나 고분자 전해질 수전해 적용 방면에서는 촉매층 연구가 다소 미비한 실정이다. 본 총설에서는 현재까지 보고된 연료전지 측면에서의 이오노머 바인더 활용 연구결과를 요약하였으며, 수소 경제 시대의 가속화를 위해서 고분자 전해질 수전해 핵심요소 중 하나인 촉매층용 이오노머 바인더에 관한 연구에 유용한 정보를 제공하고자 한다.

• Korean Chemical Engineering Research
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• 제54권1호
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• pp.11-15
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• 2016

무인항공기가 장시간 비행하기 위해서는 배터리보다 고분자전해질 연료전지(PEMFC)가 적합하다. 본 연구에서는 PEMFC에 수소를 공급하는 $NaBH_4$가수분해 반응 시스템에 대해 연구하였다. $NaBH_4$가수분해 반응 시스템의 무게를 감소시키기 위해 수소수율 향상, 응축수 회수, 안정적인 수율 유지 등에 대해 실험하였다. 반응기 압력제어를 함으로써 수소 수율을 3.4% 향상시켰다. 수소를 공랭하여 PEMFC 스택에 공급하는 과정에서 발생하는 응축수를 $NaBH_4$ 저장조에 회수하였다. 이 과정에서 응축수가 $NaBH_4$분말을 용해시켜 보충됨으로써 14%의 무게 감량효과가 있었다. 2.0 L/min의 속도로 수소를 발생시킬 때 Co-P-B촉매 2.0 g을 사용해서 10시간동안 96% 수소수율로 $NaBH_4$가수분해 반응 시스템을 안정적으로 구동하였다.