Self-sustained operation of a kWe-class kerosene-reforming processor for solid oxide fuel cells
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作者:
Yoon, Sangho
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Korea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South KoreaKorea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South Korea
Yoon, Sangho
[1
]
Bae, Yoongmyeon
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Korea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South KoreaKorea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South Korea
Bae, Yoongmyeon
[1
]
Kim, Sunyoung
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Korea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South KoreaKorea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South Korea
Kim, Sunyoung
[1
]
Yoo, Young-Sung
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Korea Elect Power Corp, Korea Elect Power Res Inst, Strateg Technol Lab, Renewable Energy Res Grp, Taejon 305380, South KoreaKorea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South Korea
Yoo, Young-Sung
[2
]
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[1] Korea Adv Inst Sci & Technol, Dept Mech Engn, Taejon 305701, South Korea
[2] Korea Elect Power Corp, Korea Elect Power Res Inst, Strateg Technol Lab, Renewable Energy Res Grp, Taejon 305380, South Korea
in this paper, fuel-processing technologies are developed for application in residential power generation (RPG) in solid oxide fuel cells (SOFCs). Kerosene is selected as the fuel because of its high hydrogen density and because of the established infrastructure that already exists in South Korea. A kerosene fuel processor with two different reaction stages, autothermal reforming (ATR) and adsorptive desulfurization reactions, is developed for SOFC operations. ATR is suited to the reforming of liquid hydrocarbon fuels because oxygen-aided reactions can break the aromatics in the fuel and steam can suppress carbon deposition during the reforming reaction. ATR can also be implemented as a self-sustaining reactor due to the exothermicity of the reaction. The We self-sustained kerosene fuel processor, including the desulfurizer, operates for about 250 h in this study. This fuel processor does not require a heat exchanger between the ATR reactor and the desulfurizer or electric equipment for heat supply and fuel or water vaporization because a suitable temperature of the ATR reformate is reached for H2S adsorption on the ZnO catalyst beds in desulfurizer. Although the CH4 concentration in the reformate gas of the fuel processor is higher due to the lower temperature of ATR tail gas, SOFCs can directly use CH4 as a fuel with the addition of sufficient steam feeds (H2O/CH4 >= 1.5), in contrast to low-temperature fuel cells. The reforming efficiency of the fuel processor is about 60%, and the desulfurizer removed H2S to a sufficient level to allow for the operation of SOFCs. Published by Elsevier B.V.