In this paper a system combining a diesel reformer using catalytic partial oxidation （CPOX） with the Solid Oxide Fuel Cell （SOFC） for Auxiliary Power Unit （APU） applications is modeled with respect to the coolin...In this paper a system combining a diesel reformer using catalytic partial oxidation （CPOX） with the Solid Oxide Fuel Cell （SOFC） for Auxiliary Power Unit （APU） applications is modeled with respect to the cooling effect provided by internal reforming of methane in anode gas channel. A model mixture consisting of 80% n-hexadecane and 20%..!-methylnaphthalin is used to simulate the commercial diesel. The modelling consists of several steps. First, equilibrium gas composition at the exit of CPOX reformer is modelled in terms oxygen to car- bon （O/C） ratio, fuel utilization ratio and anode gas recirculation. Second, product composition, especially methane content, is determined for the me.th.an, ation process at the operating temperatures ra：ng!ng from 500 ℃to 520 ℃.Finally, the cooling power provided by internal reforming of methane in SOFC fuel channel is calculated for two concepts to increase the methane content of the diesel reformate. The results show that the first concept, operating the diesel reformer at low O/C ratio and/or, recirculation rat!o, is not realizable due to high probability of coke formation, whereas the second concept, combining a methanation process with CPOX, can provide a significant cool- ing effect in addition to the conventional c？oling concept which needs higher levels of excess air.展开更多
基金Supported by the Ministry of the Environment, Climate Protection and the Energy Sector, Baden-Wuettermberg
文摘In this paper a system combining a diesel reformer using catalytic partial oxidation （CPOX） with the Solid Oxide Fuel Cell （SOFC） for Auxiliary Power Unit （APU） applications is modeled with respect to the cooling effect provided by internal reforming of methane in anode gas channel. A model mixture consisting of 80% n-hexadecane and 20%..!-methylnaphthalin is used to simulate the commercial diesel. The modelling consists of several steps. First, equilibrium gas composition at the exit of CPOX reformer is modelled in terms oxygen to car- bon （O/C） ratio, fuel utilization ratio and anode gas recirculation. Second, product composition, especially methane content, is determined for the me.th.an, ation process at the operating temperatures ra：ng!ng from 500 ℃to 520 ℃.Finally, the cooling power provided by internal reforming of methane in SOFC fuel channel is calculated for two concepts to increase the methane content of the diesel reformate. The results show that the first concept, operating the diesel reformer at low O/C ratio and/or, recirculation rat!o, is not realizable due to high probability of coke formation, whereas the second concept, combining a methanation process with CPOX, can provide a significant cool- ing effect in addition to the conventional c？oling concept which needs higher levels of excess air.
