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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
来源:
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.
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页码:23 / 31
页数:9
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