Pretreated olivine as tar removal catalyst for biomass gasifiers: investigation using naphthalene as model biomass tar

被引:240
作者
Devi, L [1 ]
Ptasinski, KJ [1 ]
Janssen, FJJG [1 ]
机构
[1] Eindhoven Univ Technol, Dept Chem Engn & Chem, Lab Chem Reactor Engn, Environm Technol Grp, NL-5600 MB Eindhoven, Netherlands
关键词
biomass; tar removal; model tar; naphthalene; olivine; pretreatment;
D O I
10.1016/j.fuproc.2004.07.001
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Biomass is considered as a potential source of renewable energy. One of the major problems for biomass gasification is the presence of tar in the product gas. We are investigating catalytic behaviour of olivine as a prospective bed additive for biomass gasifiers for tar removal. In the present paper, the pretreatment of olivine is investigated to improve its activity. Pretreatment method includes heating olivine at 900degreesC in the presence of air for different treatment times. The catalytic activity of olivine is investigated via steam-reforming reaction of naphthalene as model biomass tar compound. Improvement in naphthalene conversion of around 30% is observed with 1 h of pretreatment. Also effect of pretreatment time is investigated. With increasing pretreatment time, conversion increases; more than 80% naphthalene conversion is observed with 10 h of pretreatment time for olivine. Both steam and dry reforming reaction of naphthalene forms more than 50% gaseous products over 10 h pretreated olivine. Besides the gaseous products and light tars, polymerization reactions occur producing higher tars in small quantity. Naphthalene conversion under syngas mixture is somewhat lower than that of only in steam and CO2. Apparent activation energy of 187 kJ mol(-1) is determined for 10 h pretreated olivine under gasification-gas mixture. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:707 / 730
页数:24
相关论文
共 32 条
  • [1] ABUELRUB Z, 2002, P 12 EUR BAIOM C BIO, P607
  • [2] ALDEN H, 1994, ADV THERMOCHEMICAL B, P216
  • [3] Use of amino phase adsorbent for biomass tar sampling and separation
    Brage, C
    Yu, QZ
    Chen, GX
    Sjostrom, K
    [J]. FUEL, 1997, 76 (02) : 137 - 142
  • [4] Steam reforming model compounds of biomass gasification tars:: conversion at different operating conditions and tendency towards coke formation
    Coll, R
    Salvadó, J
    Farriol, X
    Montané, D
    [J]. FUEL PROCESSING TECHNOLOGY, 2001, 74 (01) : 19 - 31
  • [5] CORELLA J, 1988, RESEARCH IN THERMOCHEMICAL BIOMASS CONVERSION, P754
  • [6] Hydrogen production from biomass gasification on nickel catalysts - Tests for dry reforming of methane
    Courson, C
    Udron, L
    Swierczynski, D
    Petit, C
    Kiennemann, A
    [J]. CATALYSIS TODAY, 2002, 76 (01) : 75 - 86
  • [7] Development of Ni catalysts for gas production from biomass gasification. Reactivity in steam- and dry-reforming
    Courson, C
    Makaga, E
    Petit, C
    Kiennemann, A
    [J]. CATALYSIS TODAY, 2000, 63 (2-4) : 427 - 437
  • [8] Hydrogen by catalytic steam reforming of liquid byproducts from biomass thermoconversion processes
    Czernik, S
    French, R
    Feik, C
    Chornet, E
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (17) : 4209 - 4215
  • [9] Kinetics of nickel-catalyzed purification of tarry fuel gases from gasification and pyrolysis of solid fuels
    Depner, H
    Jess, A
    [J]. FUEL, 1999, 78 (12) : 1369 - 1377
  • [10] A review of the primary measures for tar elimination in biomass gasification processes
    Devi, L
    Ptasinski, KJ
    Janssen, FJJG
    [J]. BIOMASS & BIOENERGY, 2003, 24 (02) : 125 - 140