• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 추계학술대회 초록집
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• pp.87.2-87.2
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• 2010

The steady and dynamic process model for an internal reforming molten carbonate fuel cell power plant is discussed in this paper. The dominant thermal and chemical dynamic processes are modeled for the stack module and balance-of-plant, including cathode gas preparation, heat recovery, heat loss (Each heat loss amount for the stack and MBOP is obtained from real plant data) and fuel processing. Based on dynamic model and control demand, PID controllers are designed in the whole system. By applying these controllers we can obtain temperature balance of stack and control system depending on changing steam to carbon ratio, air feed amount, and transient condition.

• 대한전기학회:학술대회논문집
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• 대한전기학회 1998년도 하계학술대회 논문집 A
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• pp.55-57
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• 1998

Molten carbonate fuel cell (MCFC) power plant is expected to be one of the most promising future power generation system for the electric utilities because of its high efficiency, environmental suitability and capability of using coal as fuel. To get such attractive performance, it is necessary to consider optimizing operation and gas recycling system. This paper describes the simulation results of 7 kW MCFC stack in KEPRI and the effects of the three possible gas recycling operations, i.e. cathode gas recycling, anode gas recycling, anode gas recycling with catalytic burner.

• 전력전자학회:학술대회논문집
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• 전력전자학회 2008년도 하계학술대회 논문집
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• pp.18-20
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• 2008

An electrical balance of plant(EBOP) of a 600kW molten carbonate fuelcell (MCFC) has to transit from grid-connected(GC) mode to grid-independent(GI) mode when a grid is in a fault conditions. A minimum transition time is limited by four cycle for a 600kW MCFC to ride through a grid fault. In this paper, we propose a control algorithm of a 600kW EBOP for a MCFC system. The EBOP has three operation modes, i.e., GC mode, GI mode, and grid-synchronized(GS) mode. The EBOP controls output currents in a GC mode and regulates output voltages in GI or GS mode. GS mode is defined as an interface between GC mode and GI mode to make a mode transition smooth, i.e., limitation of inrush currents, regulation of output voltages within ANSI standard. Simulations and experiments carried out to verify the effectiveness of the proposed control algorithm.

• 플랜트 저널
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• 제15권2호
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• pp.42-45
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• 2019

용융탄산염 연료전지는 폐열의 온도가 높아 하부 사이클을 구성하여 효율을 높일 수 있다. 이러한 목적으로 연료를 재순환하는 용융탄산염 연료전지에 하부 사이클로 증기 터빈 사이클을 적용한 선행 연구가 있었다. 본 연구는 하부 사이클을 증기 터빈 사이클에서 초임계 이산화탄소 사이클로 대체하는 것을 고려하였다. 그리고 출력을 비교하여 하부 사이클을 대체하는 것에 대한 검토를 하였다. 그 결과 현재 개발 단계의 초임계 이산화탄소 사이클의 출력은 증기 터빈 사이클보다 낮지만, 이론적으로 증기 터빈 사이클보다 출력이 더 커질 수 있음을 확인하였다. 만약 초임계 이산화탄소 사이클이 터빈의 등엔트로피 효율을 89%, 압축기의 등엔트로피 효율을 83%, 복열기의 유용도를 0.9의 수준으로 향상 시킨다면 증기 터빈 사이클과 동등한 출력을 낼 수 있다.

• 전력전자학회:학술대회논문집
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• 전력전자학회 2009년도 정기총회 및 추계학술대회 논문집
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• pp.120-122
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• 2009

발전용 연료전지 시스템은 수소와 산소를 공급받아 직류전기와 열로 변화시키는 연료전지 스택, 연료전지 스택에 연료와 공기를 공급해주는 MBOP(Mechanical Balance Of Plant), 연료전지의 출력을 계통에 연계시키는 EBOP(Electrical Balance Of Plant)로 구성된다. EBOP 시스템은 병렬 연결된 1.5MW PCU(Power Conversion Unit)로 구성되며, 각 PCU는 750kW 인버터가 병렬로 구성된다. 본 논문에서는 4병렬로 구성된 3MW급 연료전지용 EBOP의 병렬제어 알고리즘을 소개한다. 제안한 병렬제어 알고리즘은 과도응답이 빠르고 순환전류가 없는 제어특성을 가진다. 그리고 시뮬레이션과 실험으로 제안한 알고리즘의 성능을 확인한다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2005년도 제17회 워크샵 및 추계학술대회
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• pp.140-148
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• 2005

The molten carbonate fuel cell (MCFC) is endowed with the high potential especially in future electric power generation industry by its own outstanding characteristics. KEPCO (KEPRI) started a 100 kW MCFC system development program in 1993 and has been executed 100kW system develpilot plant successfully completed first phaseopment by 2005 on the basis of successful results of 25kW system development. In this program, the components and mechanical structure for 100 kW stack and system construction were completed on last year and now system pre - commissioning was being executed. A 100 kW MCFC power plant was constructed at the site of Boryeong Thermal Power Plant. A 100 kW MCFC system has characterized as a high pressure operation mode, CO2 recycle, and externally reforming power generation system. The 100 kW MCFC system consisted with stacks which was made by two 50 kW sub-stacks, 90 cells with 6,000 cm2 active area and BOP including a reformer, a recycle blower, a catalytic burner, an inverter, and etc. The system has been operated from 13th of September on this year and produced 50 kW AC under atmospheric pressure condition and expected to operate by the end of this year.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2008년도 추계학술대회B
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• pp.3049-3052
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• 2008

MCFC(molten carbonate fuel cell) power generation system is prime candidate for the utilization of fossil based fuels to generate ultra clean power with a high efficiency. In the MCFC power plant system, a combustor performs a role to supply high temperature mixture gases for cathode and heat for reformer by using the stack off-gas of the anode which includes a high concentration of $H_2O$ and $CO_2$. Since a combustor needs to be operated in a very lean condition and to avoid excessive local heating, catalytic combustor is usually used. The catalytic combustion is accomplished by the catalytic chemical reaction between fuel and oxidizer at catalyst surface, different from conventional combustion. In this study, a mathematical model for the prediction of internal flow and catalytic combustion characteristics in the catalytic combustor adopted in the MCFC power plant system is suggested by using the numerical methods. The numerical simulation models are then implemented into the commercial CFD code. After verifying result by comparing with the experimental data and calibrated kinetic parameters of catalytic combustion reaction, a numerical simulation is performed to investigate the variation of flow and combustion characteristics by changing such various parameters as inlet configuration and inlet temperature. The result show that the catalytic combustion can be effectively improved for most of the case by using the perforated plate and subsequent stable catalytic combustion is expected.

• 한국수소및신에너지학회논문집
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• 제20권3호
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• pp.202-207
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• 2009

A 75kW MCFC stack with the reactive area of 9,600cm$^2$ has been operated and validated in Boryeong thermal power plant. The 75kW MCFC stack was installed at the end of November 28, 2008 and started initial operation on December 23, 2008 after pretreated for about 20 days. At initial load operation, the stack showed the Open Circuit Voltage of 137V, which approaches the theoretical value. At the early stage of rated power operation, the stack displayed the voltage of 104V at the current of 754A and reached the maximum generating power of 78.5kW DC. This stack has been operated for 2,890 hours until April, 2009. In addition, the operation time of rated power records 1890 hours. This Operating result is scheduled to be reflected the design of l25kW stack.

• 대한기계학회논문집B
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• 제36권4호
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• pp.405-412
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• 2012

MCFC 발전시스템에서 연소기는 연료극의 배가스 중에 포함된 미반응 가스를 연료로 사용하여 공기극에 $H_2O$와 $CO_2$ 농도가 높은 고온의 혼합가스를 공급하는 역할을 한다. 하지만 이러한 배가스는 가연한계 이하로 내려가게 되어 통상적인 연소방식에 의한 완전연소가 어렵기 때문에 이를 해결하기 위하여 촉매연소기를 사용한다. 완전연소 및 이에 다른 공해물질의 저감 특성에 따라 최근 촉매연소는 환경친화적인 연소방식으로 주목받고 있다. 따라서 본 연구에서는 MCFC 발전시스템의 BOP 시스템에 적용되는 촉매연소기에 대한 실험연구를 수행하였다. 본문에서는 실험장치를 설명한 후 촉매연소 시스템의 설계변수, 즉, $H_2$ 연료 첨가에 따른 연료조성, 유입가스의 온도, 과잉 공기비, 촉매의 종류, 그리고 시동 스케줄에 따른 촉매연소 특성을 고찰하였다.