Biomass gasification with air in fluidized bed: Hot gas cleanup and upgrading with steam-reforming catalysts of big size

被引：0
|
作者：
Corella, J [1 ]
Caballero, MA [1 ]
Aznar, MP [1 ]
Gil, J [1 ]
机构：
[1] Univ Complutense Madrid, Dept Chem Engn, E-28040 Madrid, Spain
来源：
BIOMASS: A GROWTH OPPORTUNITY IN GREEN ENERGY AND VALUE-ADDED PRODUCTS, VOLS 1 AND 2 | 1999年
关键词：
D O I：
暂无
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：
Several commercial steam reforming (nickel-based) catalysts were tested for tar elimination and gas upgrading in biomass gasification with air in fluidized bed. The characteristic or novelty of this work is that the catalysts are not crushed or ground but are used in their commercial size and shape. Catalysts were tested at pilot scale in two fixed beds located in a slip flow downstream from the gasifier. The equivalence ratio used in the upstream gasifier and steam content in the flue gas have an important effect on the kinetics of the tar removal reaction.
引用
收藏
页码：933 / 938
页数：6
相关论文
共 50 条
  • [41] Influence of bed material coatings on the water-gas-shift reaction and steam reforming of toluene as tar model compound of biomass gasification
    Kuba, Matthias
    Havlik, Fabian
    Kirnbauer, Friedrich
    Hofbauer, Hermann
    BIOMASS & BIOENERGY, 2016, 89 : 40 - 49
  • [42] Fluidized bed air gasification of solid recovered fuel and woody biomass: Influence of experimental conditions on product gas and pollutant release
    Valin, Sylvie
    Ravel, Serge
    de Vincent, Philippe Pons
    Thiery, Sebastien
    Miller, Helene
    FUEL, 2019, 242 : 664 - 672
  • [43] Biomass gasification with air in an atmospheric bubbling fluidized bed. Effect of six operational variables on the quality of the produced raw gas
    Narvaez, I
    Orio, A
    Aznar, MP
    Corella, J
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (07) : 2110 - 2120
  • [44] Study of nickel-based catalysts in steam reforming of tar using simulated toluene as a model compound in hot-gas cleanup of syngas
    Ahmed, Talal
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2016, 251
  • [45] Prediction and Validation of Major Gas and Tar Species from a Reactor Network Model of Air-Blown Fluidized Bed Biomass Gasification
    Stark, Addison K.
    Bates, Richard B.
    Zhao, Zhenlong
    Ghoniem, Ahmed F.
    ENERGY & FUELS, 2015, 29 (04) : 2437 - 2452
  • [46] Study of air-steam gasification of spherocylindrical biomass particles in a fluidized bed by using CFD-DEM coupling with the multi-sphere model
    Zhang, Runhui
    Ku, Xiaoke
    Yang, Shuna
    ENERGY CONVERSION AND MANAGEMENT, 2023, 276
  • [47] Simulation of air-steam gasification of woody biomass in a bubbling fluidized bed using Aspen Plus: A comprehensive model including pyrolysis, hydrodynamics and tar production
    Pauls, Jennifer H.
    Mahinpey, Nader
    Mostafavi, Ehsan
    BIOMASS & BIOENERGY, 2016, 95 : 157 - 166
  • [48] Experimental Study on Product Gas and Tar Removal in Air-Steam Gasification of Corn Straw in a Bench-Scale Internally Circulating Fluidized Bed
    Guo, Shuai
    Wei, Xiao
    Li, Jian
    Che, Deyong
    Liu, Hongpeng
    Sun, Baizhong
    Wang, Qing
    ENERGY & FUELS, 2020, 34 (02) : 1908 - 1917
  • [49] Biomass gasification in a 100 kWth steam-oxygen blown circulating fluidized bed gasifier: Effects of operational conditions on product gas distribution and tar formation
    Meng, Xiangmei
    de Jong, Wiebren
    Fu, Ningjie
    Verkooijen, Adrian H. M.
    BIOMASS & BIOENERGY, 2011, 35 (07): : 2910 - 2924
  • [50] Effect of CaO on tar reforming to hydrogen-enriched gas with in-process CO2 capture in a bubbling fluidized bed biomass steam gasifier
    Udomsirichakorn, Jakkapong
    Basu, Prabir
    Salam, P. Abdul
    Acharya, Bishnu
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (34) : 14495 - 14504
12345