CeO2/Co3O4氧载体的制备及其甲烷化学链燃烧性能研究

Preparation of cerium-cobalt composite oxygen carrier and its performance in methane chemical looping combustion

  • 摘要: 制备了系列甲烷化学链燃烧用CeO2/Co3O4复合氧载体,采用XRD、H2-TPR、甲烷程序升温和恒温反应对氧载体进行了表征与评价。研究了不同CeO2的负载量对复合氧载体的结构、氧化还原性、产物选择性的影响。结果表明,氧化铈的添加不仅降低了氧载体的初始反应温度,还延长了有效反应时间,但铈添加量过高会降低产物CO2选择性,使甲烷向部分氧化进行。CeO2(30%)/Co3O4氧载体在650 ℃经20次循环后甲烷转化率和CO2选择性均未明显降低,表现出较高的活性和化学链循环稳定性。

     

    Abstract: A series of CeO2/Co3O4 composite oxygen carriers with different CeO2 loadings were prepared and characterized by XRD and H2-TPR. The performance of CeO2/Co3O4 as an oxygen carrier in methane chemical looping combustion was investigated in a fixed-bed reactor by temperature-programmed and isothermal reactions; the effect of CeO2 loading on the structure, activity and selectivity of the oxygen carrier was considered in detail. The results show that the addition of CeO2 can reduce the reaction temperature and increase the effective reaction time of the CeO2/Co3O4 oxygen carriers for methane oxidation. However, loading of excessive CeO2 may promote the partial oxidation of methane forming CO and H2 and leads to a decrease in the selectivity to CO2. The CeO2/Co3O4 composite oxygen carrier with a CeO2 loading of 30% (mol ratio) exhibits the highest activity and redox stability in the chemical looping combustion of methane; over it, methane can be quickly converted to CO2 and H2O with high selectivity (over 90%) at 650 ℃ and the reduced oxygen carrier can be fully recovered in O2 atmosphere. Moreover, no obvious decline in the conversion of methane and selectivity to CO2 is observed in the successive CH4-reduction and O2-oxidation redox process for over 20 cycles.

     

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