Catalytic upgrading of coal pyrolysis tar over char-based catalysts

被引:168
作者
Han, Jiangze [1 ,2 ]
Wang, Xingdong [1 ]
Yue, Junrong [1 ]
Gao, Shiqiu [1 ]
Xu, Guangwen [1 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
基金
对外科技合作项目(国际科技项目); 中国国家自然科学基金;
关键词
Coal pyrolysis; Catalytic upgrading; Tar quality; Char-based catalyst; BIOMASS GASIFICATION GAS; VICTORIAN BROWN-COAL; AROMATIC-HYDROCARBONS; VOLATILE MATTER; NI CATALYSTS; ZIRCONIA; LIGNITE; VOLATILIZATION; HYDROCRACKING; REDUCTION;
D O I
10.1016/j.fuproc.2014.01.033
中图分类号
O69 [应用化学];
学科分类号
070301 [无机化学];
摘要
Catalytic upgrading of coal pyrolysis tar was investigated in a dual-stage reactor over char and metal-impregnated char (Co-char, Ni-char, Cu-char, Zn-char). The catalytic upgrading caused the lower total tar yield and the higher non-condensable gas yield but the fraction of light tar (boiling point <360 degrees C) obviously increased to allow slightly higher total yield of light tar. When the catalytic upgrading was at 600 degrees C over a layer of char having a mass of 20% of the tested coal, the resulting light tar fraction in the tar increased by 25% in comparison with the coal pyrolysis only at 600 degrees C Over the metal-impregnated char, which was 5% of the tested coal in mass, good upgrading effect was obtained at 500 degrees C. The catalytic tar-upgrading activity decreased in an order of Co-char > Ni-char > Cu-char > Zn-char, and over Ni-char the realized light tar yield and its content in the tar increased by 17.2% and 32.7%, respectively. The upgrading effect also lowered the contents of element N and S in the resulting tar by 45.6% and 43.5%, respectively. NH3-TPD clarified that the order in acidity of the char-based catalysts was the same as for the upgrading activity shown above. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:98 / 106
页数:9
相关论文
共 37 条
[1]
Thermal decomposition of low-density polyethylene in the presence of iron and copper chlorides [J].
Blazso, M ;
Zelei, B .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1996, 36 (02) :149-158
[2]
High tar reduction in a two-stage gasifier [J].
Brandt, P ;
Larsen, E ;
Henriksen, U .
ENERGY & FUELS, 2000, 14 (04) :816-819
[3]
THE TECHNICAL AND ECONOMIC-FEASIBILITY OF BIOMASS GASIFICATION FOR POWER-GENERATION [J].
BRIDGWATER, AV .
FUEL, 1995, 74 (05) :631-653
[4]
Production of aromatic hydrocarbons from Mae-Moh lignite [J].
Chareonpanich, M ;
Boonfueng, T ;
Limtrakul, J .
FUEL PROCESSING TECHNOLOGY, 2002, 79 (02) :171-179
[5]
EFFECT OF CATALYSTS ON YIELDS OF MONOCYCLIC AROMATIC-HYDROCARBONS IN HYDROCRACKING OF COAL VOLATILE MATTER [J].
CHAREONPANICH, M ;
ZHANG, ZG ;
NISHIJIMA, A ;
TOMITA, A .
FUEL, 1995, 74 (11) :1636-1640
[6]
CATALYTIC HYDROCRACKING REACTION OF NASCENT COAL VOLATILE MATTER UNDER HIGH-PRESSURE [J].
CHAREONPANICH, M ;
TAKEDA, T ;
YAMASHITA, H ;
TOMITA, A .
FUEL, 1994, 73 (05) :666-670
[7]
A review of the primary measures for tar elimination in biomass gasification processes [J].
Devi, L ;
Ptasinski, KJ ;
Janssen, FJJG .
BIOMASS & BIOENERGY, 2003, 24 (02) :125-140
[8]
Catalytic steam reforming of biomass tar over iron- or nickel-based catalyst supported on calcined scallop shell [J].
Guan, Guoqing ;
Chen, Gang ;
Kasai, Yutaka ;
Lim, Eldin Wee Chuan ;
Hao, Xiaogang ;
Kaewpanha, Malinee ;
Abuliti, Abudula ;
Fushimi, Chihiro ;
Tsutsumi, Atsushi .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2012, 115 :159-168
[9]
The reduction and control technology of tar during biomass gasification/pyrolysis: An overview [J].
Han, Jun ;
Kim, Heejoon .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2008, 12 (02) :397-416
[10]
Reforming of Volatiles from the Biomass Pyrolysis over Charcoal in a Sequence of Coke Deposition and Steam Gasification of Coke [J].
Hosokai, Sou ;
Norinaga, Koyo ;
Kimura, Tokuji ;
Nakano, Masaki ;
Li, Chun-Zhu ;
Hayashi, Jun-ichiro .
ENERGY & FUELS, 2011, 25 (11) :5387-5393