Nickel-based catalysts for tar reduction in biomass gasification

被引:39
作者
Wu, Chunfei [1 ]
Williams, Paul T. [1 ]
机构
[1] Univ Leeds, Energy & Resources Res Inst, Leeds LS2 9JT, W Yorkshire, England
来源
BIOFUELS-UK | 2011年 / 2卷 / 04期
基金
英国工程与自然科学研究理事会;
关键词
D O I
10.4155/BFS.11.113
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
Biomass, regarded as a renewable energy resource, will play an important role for the sustainable development of society, environment and economics. The presence of tar in the gases produced from biomass gasification limits the application of the gaseous products, since the tar can cause blockages, plugging, corrosion and catalyst deactivation. Nickel-based catalysts are known to be effective in biomass gasification for tar reduction to produce synthesis gases because of their comparative lower cost and effective catalytic reactivity. In this paper, several types of nickel-based catalysts reported for biomass gasification are reviewed in relation to their preparation, reaction conditions and stability for the biomass/tar gasification process.
引用
收藏
页码:451 / 464
页数:14
相关论文
共 114 条
[21]   PREPARATION AND CHARACTERIZATION OF NICKEL ALUMINUM MIXED OXIDES OBTAINED BY THERMAL-DECOMPOSITION OF HYDROTALCITE-TYPE PRECURSORS [J].
CLAUSE, O ;
REBOURS, B ;
MERLEN, E ;
TRIFIRO, F ;
VACCARI, A .
JOURNAL OF CATALYSIS, 1992, 133 (01) :231-246
[22]   PREPARATION AND THERMAL REACTIVITY OF NICKEL CHROMIUM AND NICKEL ALUMINUM HYDROTALCITE-TYPE PRECURSORS [J].
CLAUSE, O ;
GAZZANO, M ;
TRIFIRO, F ;
VACCARI, A ;
ZATORSKI, L .
APPLIED CATALYSIS, 1991, 73 (02) :217-236
[23]   Biomass gasification with air in a fluidized bed:: Exhaustive tar elimination with commercial steam reforming catalysts [J].
Corella, J ;
Orío, A ;
Toledo, JM .
ENERGY & FUELS, 1999, 13 (03) :702-709
[24]   Olivine or dolomite as in-bed additive in biomass gasification with air in a fluidized bed: Which is better? [J].
Corella, J ;
Toledo, JM ;
Padilla, R .
ENERGY & FUELS, 2004, 18 (03) :713-720
[25]   Improved yield parameters in catalytic steam gasification of forestry residue; optimizing biomass feed rate and catalyst type [J].
Corujo, Andrea ;
Yerman, Luis ;
Arizaga, Beatriz ;
Brusoni, Mariana ;
Castiglioni, Jorge .
BIOMASS & BIOENERGY, 2010, 34 (12) :1695-1702
[26]   Hydrogen by catalytic steam reforming of liquid byproducts from biomass thermoconversion processes [J].
Czernik, S ;
French, R ;
Feik, C ;
Chornet, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (17) :4209-4215
[27]   An investigation of alumina-supported catalysts for the selective catalytic oxidation of ammonia in biomass gasification [J].
Darvell, LI ;
Heiskanen, K ;
Jones, JM ;
Ross, AB ;
Simell, P ;
Williams, A .
CATALYSIS TODAY, 2003, 81 (04) :681-692
[28]   Hydrogen production from crude pyrolysis oil by a sequential catalytic process [J].
Davidian, Thomas ;
Guilhaume, Nolven ;
Iojoiu, Eduard ;
Provendier, Helene ;
Mirodatos, Claude .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2007, 73 (1-2) :116-127
[29]   Biomass gasification with steam in fluidized bed: Effectiveness of CaO, MgO, and CaO-MgO for hot raw gas cleaning [J].
Delgado, J ;
Aznar, MP ;
Corella, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) :1535-1543
[30]   Pretreated olivine as tar removal catalyst for biomass gasifiers: investigation using naphthalene as model biomass tar [J].
Devi, L ;
Ptasinski, KJ ;
Janssen, FJJG .
FUEL PROCESSING TECHNOLOGY, 2005, 86 (06) :707-730