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Numerical Simulation of SOFC System Performance at 90 Fuel Utilization with or without Anode Off-gas Recycle for Enhancing Efficiency

机译:使用或不使用阳极废气再循环以提高效率时,燃料利用率为90%时SOFC系统性能的数值模拟

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To investigate the possibility to enhance electrical efficiency, performance of methane-fueled 10 kW SOFC systems was numerically simulated with calculated voltage-current-density curves at 750°C of a single cell with a bipolar plate, which approximated a stack performance. Operation at 90% fuel utilization (U_f) with anode off-gas recycle (AGR) and with steam reforming (no recycle) led to 75-67 %-LHV and 72-66 %-LHV DC electrical efficiencies at 0.05-0.40 A/cm~2, respectively. System simulations considering heat loss from a stack clarified that 750°C stack temperature can be maintained at 0.12-0.40 A/cm~2 and 64-59 % and 63-59 % net AC electrical efficiency will be attainable at U_f = 90% with and without AGR, respectively. Furthermore, enhancement of net AC efficiencies was found to be 10 percentage points at those current densities against ones of a conventional system using steam reforming at U_f = 73 %.
机译:为了研究提高电效率的可能性,使用计算出的双极板单电池在750°C的电压-电流-密度曲线,对甲烷供气的10 kW SOFC系统的性能进行了数值模拟,其近似于电池组的性能。在阳极废气再循环(AGR)和蒸汽重整(无再循环)的情况下以90%的燃料利用率(U_f)运行可在0.05-0.40 A /的条件下产生75-67%-LHV和72-66%-LHV的直流电效率cm〜2考虑到烟囱热量损失的系统仿真表明,可以将750°C烟囱温度保持在0.12-0.40 A / cm〜2,在U_f = 90%的情况下,可以实现64-59%和63-59%的净交流电效率。和没有AGR。此外,发现在那些电流密度下,相对于使用U_f = 73%的蒸汽重整的常规系统,交流电的净交流效率提高了10个百分点。

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