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CH4-CO2 reforming over Ni/Al2O3 aerogel catalysts in a fluidized bed reactor

机译:Ni / Al2O3气凝胶催化剂在流化床反应器中的CH4-CO2重整

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摘要

Ni/Al2O3 aerogel catalysts were synthesized by a sol-gel method combined with a supercritical drying route.The catalytic performances of the catalysts in methane reforming with CO2 were investigated in a quartz micro-reactor.The results indicated that the aerogel catalyst showed higher specific surface area and higher dispersivity of nickel species than those of impregnation catalyst.The excellent catalytic performances and stabilities were achieved over the aerogel catalysts in the fluidized bed reactor.Comprehensive characterization with TG,XRD and FESEM revealed that the aerogel catalyst in the fluidized bed had much lower carbon deposition than that in the fixed bed.The fluidization of the aerogel catalyst greatly improved the contact efficiency of gas-solid phase,which accelerated the gasification of the deposited carbon.In contrast,the deactivation of the aerogel catalyst was caused by the carbon deposition due to the catalyst without moving in the fixed bed.Moreover,decreasing activity of the impregnation catalyst in the fluidized bed resulted from the poor fluidization state of catalyst particles and low effective active sites on surface of catalyst.
机译:采用溶胶-凝胶法结合超临界干燥路线合成了Ni / Al2O3气凝胶催化剂,在石英微反应器中研究了CO2重整甲烷催化剂的催化性能,结果表明该气凝胶催化剂具有较高的比重。比浸渍催化剂具有更大的表面积和较高的镍分散性。流化床反应器中的气凝胶催化剂具有优异的催化性能和稳定性。TG,XRD和FESEM的综合表征表明,流化床中的气凝胶催化剂具有气凝胶催化剂的流化大大提高了气固相的接触效率,从而加速了沉积碳的气化。相反,气凝胶催化剂的失活是由固相床引起的。由于催化剂的碳沉积而不在固定床中移动。催化剂在流化床中的渗透性是由于催化剂颗粒的流化状态差和催化剂表面的有效活性位低所致。

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