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Dry reforming of methane in an atmospheric pressure plasma fluidized bed with Ni/γ-Al2O3 catalyst

机译:Ni /γ-Al2O3催化剂在常压等离子体流化床中甲烷的重整

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The synergetic effect of catalyst and cold plasma on dry reforming of methane was investigated in a plasma fluidized bed with Ni/γ-Al2O3 catalyst. As a comparison, the experiments in the plasma packed bed were also carried out. The cold plasma was generated by the dielectric barrier discharge (DBD) at atmospheric pressure. Both contact modes between plasma and catalytic particles promoted the catalyst activity at low temperatures (e.g., 673 K). In the plasma fluidized bed, the synergetic effect of the catalyst and the plasma was clearly identified from 648 K to 798 K. The synergetic effect characterized by the conversion ratio of synergetic results to the sum of the results of only using plasma and only using catalyst showed that the plasma fluidized bed behaved better than the plasma packed bed within a certain temperature range. For the versatile flow regimes in the fluidization of catalysts, the plasma fluidized bed found great potential in plasma enhanced chemical processes by manipulating the gas-solid two-phase flows in the plasma environment.
机译:在Ni /γ-Al2O3催化剂流化床中,研究了催化剂和冷等离子体对甲烷干重整的协同作用。作为比较,还进行了在等离子填充床中的实验。冷等离子体是在大气压下通过电介质势垒放电(DBD)生成的。等离子体和催化颗粒之间的两种接触方式都促进了低温(例如673 K)下的催化剂活性。在等离子流化床中,从648 K到798 K清楚地识别出催化剂和等离子体的协同作用。协同作用的特征是协同结果的转化率与仅使用等离子体和仅使用催化剂的结果之和结果表明,在一定温度范围内,等离子流化床的性能优于等离子填充床。对于催化剂流化中的多种流动方式,通过控制等离子体环境中的气固两相流,等离子体流化床在等离子体增强化学过程中发现了巨大的潜力。

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