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Kinetics of steam and CO_2 gasification with high ash fusion temperature coal char under elevated pressure

机译:高灰熔融温度煤焦在高压下蒸汽和CO_2气化动力学

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A high ash fusion temperature (AFT) coal char was gasified with steam and CO2 under elevated pressure in a modified pressurized thermogravimetric analyzer. The ambient pressure varied from 0.5 MPa to 3 MPa. It was found that activation energy E-a (char-CO2 reaction) was from 214.19 kJ/mol to 240.35 kJ/mol, and activation energy Ea (char-steam reaction) was from 170.02 kJ/mol to 174.02 kiimol by using shrinking core model. The factor of partial pressure influence (n) was 0.44 and 0.54 for CO2 and steam gasification, respectively. The results proved that the high AFT coal (U coal) has poor gasification reactivity by comparing with other research and provided complete kinetic data for developing the entrained flow gasification technology using high AFT coal
机译:在改进的加压热重分析仪中,在升高的压力下,用蒸汽和CO2将高灰熔融温度(AFT)的煤焦气化。环境压力在0.5 MPa至3 MPa之间变化。通过收缩核模型,发现活化能E-a(炭-CO 2反应)为214.19kJ / mol至240.35kJ / mol,活化能Ea(炭-蒸汽反应)为170.02kJ / mol至174.02kiimol。对于CO2和蒸汽气化,分压影响因子(n)分别为0.44和0.54。结果表明,与其他研究相比,高AFT煤(U煤)的气化反应性较差,为开发高AFT煤的气流床气化技术提供了完整的动力学数据。

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