Coke formation on the surface of Ni/HZSM-5 and Ni-Cu/HZSM-5 catalysts during bio-oil hydrodeoxygenation

被引:144
|
作者
Li, Yu [1 ,2 ]
Zhang, Changsen [1 ,2 ]
Liu, Yonggang [1 ,2 ]
Tang, Songshan [1 ,2 ]
Chen, Guanghui [1 ,2 ]
Zhang, Ruiqin [1 ,2 ]
Tang, Xiaoyan [2 ]
机构
[1] Zhengzhou Univ, Coll Chem & Mol Engn, Zhengzhou 450001, Peoples R China
[2] Zhengzhou Univ, Res Inst Environm Sci, Zhengzhou 450001, Peoples R China
关键词
Bio-oil; Hydrodeoxygenation; Catalyst deactivation; Deposition of coke; PHASE BECKMANN REARRANGEMENT; ALIPHATIC ESTERS; CARBON; DEACTIVATION; CONVERSION; ZEOLITE; COKING; DEPOSITION; METHANOL; ALLOY;
D O I
10.1016/j.fuel.2016.10.047
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
Deactivation of zeolite catalysts due to coke deposition is a pronounced challenge in the hydrodeoxy-genation (HDO) of bio-oil. This paper reports on the mechanism of coke formation and catalyst regeneration for two catalysts (Ni/HZSM-5, Ni-Cu/HZSM-5). FT-IR, XPS and Raman spectroscopy characterizations indicate that catalyst deactivation can be divided into three main stages: (1) Lewis acid sites in HZSM-5 support are rapidly covered by oxygenated hydrocarbons. The Bronsted acid sites of HZSM-5 donate protons to oxygenates, leading to the formation of carbocations - precursors of soluble coke on the catalyst surfaces. (2) Soluble coke is then stacked to form disordered filament-like carbon strands that are similar to carbon nanotubes or graphite-like structures. (3) Filament-like carbon evolves into graphite carbon. At the same HDO temperature, more graphite particles are found on the Ni/HZSM-5 catalyst than on the Ni-Cu/HZSM-5 catalyst, indicating higher resistance for the coke formation for Ni-Cu/HZSM-5 catalyst. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:23 / 31
页数:9
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