Hydrogenation of phenol by defective ZSM-5 supporting Ni catalyst to produce cyclohexanol

被引:5
|
作者
Guo, Longhui [1 ]
Chen, Xiaozhou [1 ]
Zhou, Shuaishuai [1 ]
Yu, Xin [1 ]
Qiao, Congzhen [1 ]
Tian, Yajie [1 ]
机构
[1] Henan Univ, Sch Energy Sci & Technol, Zhengzhou 450046, Peoples R China
基金
中国国家自然科学基金;
关键词
Zeolite modification; Hydrogenation; Phenol; Cyclohexanol; Ni; SELECTIVE HYDROGENATION; ZEOLITE CRYSTALS; BETA-ZEOLITE; ACID SITES; HYDRODEOXYGENATION; NANOPARTICLES; PERFORMANCE; MONOMERS;
D O I
10.1016/j.fuel.2024.131384
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Cyclohexanol is an essential intermediate in the chemical industry, which can be produced from hydrogenation of phenol. In this work, a defective ZSM-5 zeolite supporting Ni catalyst (Ni/D-ZSM) is prepared by sequenced nitric acid treatment, impregnation, and reduction. In conversion of phenol, the highly dispersed Ni with strong interaction with the defective Si-OH delivers relative higher adsorption and spillover of active hydrogen, thus promoting the hydrogenation of phenol. Moreover, owing to the unique coordination environment of Ni in defective ZSM-5 zeolite with moderate acid properties, the desorption of intermediate cyclohexanol is promoted. The turnover frequency (TOF) calculated based on the yield of cyclohexanol and amount of metal reveals that, the Ni/D-ZSM sample by 48 h acid treatment (Ni/D-ZSM-48) delivers TOF values up to 17.73 x 10(-3)<middle dot>s(-1). The designed Ni/D-ZSM-48 catalyst with relative low Ni loading of similar to 5 wt% delivers equivalent (slightly higher) production rates of cyclohexanol with the ever-reported noble-metal samples (Rh, Ru etc.) and significantly higher than the transition-metal based catalysts.
引用
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页数:8
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