催化作用
合成气
氧化物
尖晶石
无机化学
氧化钒
化学
物理吸附
氧气
三元运算
克罗米亚
材料科学
钒
有机化学
冶金
程序设计语言
计算机科学
作者
Fanhui Meng,Guinan Yang,Baozhen Li,Zhong Li
标识
DOI:10.1016/j.apcata.2022.118884
摘要
A series of XMnGa (X=Al, Zn, Ce and V) oxides and VMnGa( y ) with various V/(V+Mn+Ga) atomic ratios were prepared by the co-precipitation method, and mixed with SAPO-34 to prepare bifunctional catalyst for syngas conversion to light olefins (STO). ( In-situ ) XRD, N 2 physisorption, SEM, TEM, H 2 -TPR, CO-TPD, H 2 -TPD, XPS and in-situ DRIFTS were selected for characterization. VMnGa(0.1) oxide sample exhibits the highest CO conversion and olefins space-time yield, while the other ternary metal oxides show poor CO conversion or low selectivity. The introduction of suitable amount of V into MnGa oxide formed Mn 2 VO 4 spinel structure. VMnGa(0.1) possesses high amounts of desorbed CO, which is due to the formation of more oxygen vacancies on metal oxide surface. The structure evolution of VMnGa(0.1) in pretreatment atmosphere of H 2 and syngas (H 2 /CO=2:1) was studied and the catalytic performance for STO was compared; moreover, the structure-activity and reaction intermediate during the reaction were revealed. • XMnGa (X=Al, Zn, Ce or V) oxide and VMnGa( y ) with various V contents are prepared • VMnGa(0.1) oxide generates more oxygen vacancy benefiting CO and H 2 adsorption • H 2 pretreatment on VMnGa(0.1) only affects initial CO conversion and selectivity • VMnGa(0.1)/SAPO-34 shows higher catalytic performance than the other samples • CH 3 O* was the reaction intermediate over VMnGa(0.1) oxide during the reaction
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