Additive WO2 promotes Ni - based catalyst for hydrogen production from auto-thermal reforming of acetic acid

催化作用 烧结 醋酸 脱氢 制氢 产量(工程) 碳纤维 吸附 化学 化学工程 无机化学 材料科学 物理化学 有机化学 冶金 复合材料 工程类 复合数
作者
Hui Chen,Wenjing Sun,Xiaomin Hu,Qi Wang,Tong Wu,Shuang An,Chenyu Ding,Congmei Chen,Lihong Huang,Ning Wang
出处
期刊:Fuel [Elsevier BV]
卷期号:339: 126914-126914 被引量:14
标识
DOI:10.1016/j.fuel.2022.126914
摘要

Nickel-based catalysts exhibit excellent initial activity in the auto-thermal reforming (ATR) of acetic acid (HAc) to produce hydrogen; meanwhile, deactivation issues, namely oxidation, sintering and carbon deposition, have not been fully addressed. Hence, we prepared a series of Ni–W/SiO2 catalysts and found the Ni-2W/SiO2 catalyst with 2 wt% W decoration presented the best catalytic activity and stability: the conversion rate of acetic acid was stable at 100 %, and the hydrogen yield remained at 2.8 mol-H2/mol-HAc with neither sintering nor carbon deposition. The excellent catalytic performance of Ni-2W/SiO2 was analyzed and can be attributed to the special properties of WO2 as followed: First, during the ATR process, WO2 species migrated to the surface of Ni phase and formed an interface, which resulted in strong interaction of WO2-Ni and relieved carbon deposition and sintering of Ni species; Second, the effect of electron donor by WO2 species on the WO2-Ni interface during the reduction procedure was found and preserved a stable proportion of Ni0 active species during the ATR process; Third, DFT and in-situ DRIFTS confirmed that CH3COOH tends to be enriched on the WO2 species of the WO2/Ni(1 1 1) interface rather than on the Ni(1 1 1) surface, promoting the adsorption and dehydrogenation of CH3COOH to intermediates of CH3COO* and H*, which is difficult to occur on WO3 species of the WO3/Ni(1 1 1) interface because of high reaction barrier.
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