First-principles-based microkinetic simulations of syngas to methanol conversion on ZnAl2O4 spinel oxide

被引:18
作者
Hu, Wen-De [1 ]
Wang, Chuan-Ming [1 ]
Wang, Yang-Dong [1 ]
Ke, Jun [1 ]
Yang, Guang [1 ]
Du, Yu-Jue [1 ]
Yang, Wei-Min [1 ]
机构
[1] Sinopec Shanghai Res Inst Petrochem Technol, State Key Lab Green Chem Engn & Ind Catalysis, Shanghai 201208, Peoples R China
基金
中国国家自然科学基金; 中国博士后科学基金;
关键词
Syngas to methanol; ZnAl2O4 spinel oxide; Surface structure; Reaction kinetics; Microkinetic simulations; SITU FT-IR; LIGHT OLEFINS; HETEROGENEOUS CATALYSIS; BIFUNCTIONAL CATALYSTS; SELECTIVE CONVERSION; TO-HYDROCARBONS; ZINC ALUMINATE; 1ST PRINCIPLE; SYNTHESIS GAS; PORE-SIZE;
D O I
10.1016/j.apsusc.2021.151064
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Identifying active site structure and unveiling corresponding reaction pathways are crucial issues to construct compatible reactive components in bifunctional catalysts for direct syngas conversion. Herein, the active surface structure and the reaction mechanism of syngas conversion to bridging intermediate methanol on ZnAl2O4 spinel oxide are systematically investigated by combining density functional theory calculations and microkinetic simulations. The hydmxylated oxygen-rich surfaces of ZnAl2O4 are demonstrated and their stabilities decreases as (100)-B-1/4H > (111)-B-3/8H > (110)-B-1/4H. Four reaction pathways differentiating in the adsorption site of CO and the participation style of H-2 on these surfaces are kinetically compared. We reveal that ZnAl2O4(111) is the active surface for syngas conversion; CO bonding on O site is activated more readily in a stepwise way to CH2O and the concerted pathway is then followed for CH2O to methanol. On ZnAl2O4(100) and ZnAl2O4(110) surfaces, the Non-Horiuti-Polanyi pathway in which gaseous H-2 reacting directly with CO or CH2O becomes kinetically more important. The Zn-O site of ZnAl2O4(111) is essential to dissociate H-2 hetemlytically and stabilize key intermediate CHO. We show that the reaction rate decreases with the CO conversion, and the simulated reaction rate (similar to 13 s(-1)) at 8% conversion agrees quite well with the experimental one (similar to 20 s(-1)) under the typical reaction conditions. The predicted activity plots with temperature and CO conversion highlight the driving essentiality of zeolite component in bifunctional catalysts for syngas conversion.
引用
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页数:14
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