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煤热解与甲烷蒸汽重整耦合过程焦油在碳基镍催化剂上的原位催化提质

王政委 魏宝勇 吕剑楠 王一鸣 武云飞 杨赫 胡浩权

燃料化学学报2022,Vol.50Issue(2):129-142,14.
燃料化学学报2022,Vol.50Issue(2):129-142,14.DOI:10.1016/S1872-5813(21)60169-X

煤热解与甲烷蒸汽重整耦合过程焦油在碳基镍催化剂上的原位催化提质

In-situ catalytic upgrading of tar from integrated process of coal pyrolysis with steam reforming of methane over carbon based Ni catalyst

王政委 1魏宝勇 1吕剑楠 1王一鸣 1武云飞 1杨赫 1胡浩权1

作者信息

  • 1. 大连理工大学化工学院煤化工研究所,精细化工国家重点实验室,辽宁大连116024
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摘要

Abstract

In order to improve the tar quality by decreasing the heavy tar content and ensuring high tar yield, in-situ catalytic upgrading of tar from the integrated process of coal pyrolysis coupled with steam reforming of methane was conducted over carbon (KD-9) based Ni catalyst. The results show that at 650 ℃, the tar yield of CP-SRM over 5Ni/KD-9 is 24.4%, which is a little lower than that of without catalyst, while the light tar yield (i.e.,18.9%) is 1.4 times higher than that of without catalyst, and the content of C2, C3 and C4 alkyl used as a substitute for benzene significantly increases tar yields by 0.5, 0.6 and 4.0 times, respectively. The content of phenols and naphthalenes in tar also increases dramatically after upgrading. Isotope tracer approach combined with the mass spectra of typical components was employed in exploring the mechanism of the upgrading process. The results show that 5Ni/KD-9 catalyzes coal tar cracking and SRM at the same time. Small free radicals such as ·CHx, ·H and ·OH generated by SRM can combine with free radicals from tar cracking, thus avoiding excessive cracking of tar.

关键词

煤热解/催化提质/焦油/甲烷蒸汽重整/同位素示踪

Key words

coalpyrolysis/catalyticupgrading/tar/steamreformingofmethane/isotopetracer

分类

化学化工

引用本文复制引用

王政委,魏宝勇,吕剑楠,王一鸣,武云飞,杨赫,胡浩权..煤热解与甲烷蒸汽重整耦合过程焦油在碳基镍催化剂上的原位催化提质[J].燃料化学学报,2022,50(2):129-142,14.

基金项目

The project was supported by NSFC and Shanxi Provincial Government of China(U1710105). (U1710105)

燃料化学学报

OA北大核心CSCDCSTPCD

2097-213X

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