Pyrolysis of metal impregnated biomass: An innovative catalytic way to produce gas fuel

被引:105
作者
Bru, K.
Blin, J.
Julbe, A.
Volle, G.
机构
[1] CIRAD, UPR 42 Biomasse Energie, Foret, F-34398 Montpellier 5, France
[2] UMII, CNRS UMR 5635, Inst Europeen Membranes, F-34095 Montpellier, France
关键词
biomass pyrolysis; catalytic conversion; hydrogen;
D O I
10.1016/j.jaap.2006.08.006
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
An innovative way of catalysis was investigated for its potential to reduce the amount of condensable hydrocarbons produced during the pyrolysis of oak wood. The experiments were carried out in a horizontal tubular reactor, fed with a controlled flow rate of nitrogen and equipped with accessories to collect char, liquid and gaseous products. Pyrolysis was performed at 700 degrees C with different wood sample series impregnated with either Ni or Fe nitrates (in aqueous solution) and by varying the metal concentration in the wood. In the blank run the biomass was acid-washed to determine the impact of demineralization. The influence of the metal type and content introduced into the wood to reduce the fraction of condensable organic compounds produced during pyrolysis was determined. Depending on the experimental conditions, the gas yield increases from 20.0 to 33.1%. Condensable hydrocarbons are cracked into gaseous components and the concentration of H, is significantly increased, by 260% compared to the reference sample. In particular, the Ni-loaded wood samples give much higher H, yields than the Fe-loaded ones under similar conditions but less toxic products are formed with the latter. These results show that biomass impregnation with either nickel or iron salts is a promising way to reduce the fraction of condensable organic compounds produced during pyrolysis. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:291 / 300
页数:10
相关论文
共 87 条
  • [1] The aryl ether bond reactions with H-donor solvents: Guaiacol and tetralin in the presence of catalysts
    Afifi, AI
    Chornet, E
    Thring, RW
    Overend, RP
    [J]. FUEL, 1996, 75 (04) : 509 - 516
  • [2] The technical feasibility of biomass gasification for hydrogen production
    Albertazzi, S
    Basile, E
    Brandin, J
    Einvall, J
    Hulteberg, C
    Fornasari, G
    Rosetti, V
    Sanati, M
    Trifirò, F
    Vaccari, A
    [J]. CATALYSIS TODAY, 2005, 106 (1-4) : 297 - 300
  • [3] ANTONINI G, 1998, Patent No. 9803744
  • [4] Gasification of brown coal and char with carbon dioxide in the presence of finely dispersed iron catalysts
    Asami, K
    Sears, P
    Furimsky, E
    Ohtsuka, Y
    [J]. FUEL PROCESSING TECHNOLOGY, 1996, 47 (02) : 139 - 151
  • [5] STEAM GASIFICATION OF BIOMASS WITH NICKEL SECONDARY CATALYSTS
    BAKER, EG
    MUDGE, LK
    BROWN, MD
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (07) : 1335 - 1339
  • [6] INFLUENCE OF PHYSICAL AND CHEMICAL-PARAMETERS ON WOOD PYROLYSIS
    BEAUMONT, O
    SCHWOB, Y
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (04): : 637 - 641
  • [7] Internal steam reforming of methane over Ni-based electrode in solid oxide fuel cells
    Belyaev, VD
    Politova, TI
    Marina, OA
    Sobyanin, VA
    [J]. APPLIED CATALYSIS A-GENERAL, 1995, 133 (01) : 47 - 57
  • [8] An overview of fast pyrolysis of biomass
    Bridgwater, AV
    Meier, D
    Radlein, D
    [J]. ORGANIC GEOCHEMISTRY, 1999, 30 (12) : 1479 - 1493
  • [9] THE TECHNICAL AND ECONOMIC-FEASIBILITY OF BIOMASS GASIFICATION FOR POWER-GENERATION
    BRIDGWATER, AV
    [J]. FUEL, 1995, 74 (05) : 631 - 653
  • [10] 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