Characterization and catalytic performance of Fe3Ni8/palygorskite for catalytic cracking of benzene

被引:33
作者
Liu, Haibo [1 ,3 ]
Chen, Tianhu [1 ]
Chang, Dongyin [1 ]
Chen, Dong [1 ]
He, Hongping [2 ,3 ]
Yuan, Peng [2 ]
Xie, Jingjing [1 ]
Frost, Ray L. [3 ]
机构
[1] Hefei Univ Technol, Sch Resource & Environm Engn, Hefei, Peoples R China
[2] Chinese Acad Sci, Guangzhou Inst Geochem, Guangzhou, Guangdong, Peoples R China
[3] Queensland Univ Technol, Discipline Nanotechnol & Mol Sci, Fac Sci & Technol, Brisbane, Qld 4001, Australia
基金
高等学校博士学科点专项科研基金;
关键词
Palygorskite; Awaruite; Benzene; Hydrogen yield; Catalytic cracking; Activity component; IRON-CONTAINING CATALYSTS; STEAM GASIFICATION; MODERATE TEMPERATURES; METHANE DECOMPOSITION; BIOMASS GASIFIERS; PARTIAL OXIDATION; REMOVAL CATALYST; TAR ELIMINATION; NI CATALYSTS; GAS;
D O I
10.1016/j.clay.2012.04.005
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Catalytic decomposition is a very attractive way to convert tar components into H-2, CO and other useful chemicals. The performance of Fe3Ni8/PG (palygorskite, PG) reduced in hydrogen at different temperatures for the catalytic decomposition of benzene has been assessed. Benzene was used as the model biomass tar. The effects of calcination atmosphere, temperatures and benzene concentration on catalytic cracking of benzene were measured. The results of XRD (X-Ray Diffraction), TEM (Transmission Electron Microscope), TPR (Temperature Program Reduction), TPSR (Temperature Program Surface Reduction), TC (Total Carbon), the reactivity component and reaction mechanism over Fe3Ni8/PG for catalytic cracking of benzene are discussed. The results showed particles of awaruite (Fe, Ni) about 2-30 nm were found on the surface of palygorskite by TEM when the calcination temperature was 600 degrees C. Particles with size smaller than 30 nm were obtained on all prepared Fe3Ni8/PG catalysts as shown by XRD. The nanoparticles proved to be the reactive component for catalytic cracking of benzene and the increase of active particle size caused the decrease in the reactivity of Fe3Ni8/PG. Fe3Ni8/PG annealed in hydrogen at 600 degrees C was proved to have the best reactivity in experiments (45% hydrogen yield). High concentration benzene (448 g/m(3)) accelerated the formation of carbon deposition. However, iron oxide decreases carbon deposition and increases the stability of catalyst for catalytic cracking of benzene. The application of Fe3Ni8/PG catalysts was proved a very effective catalyst for the catalytic cracking of benzene. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:135 / 140
页数:6
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共 42 条
  • [1] A comparison of Rh/CeO2/SiO2 catalysts with steam reforming catalysts, dolomite and inert materials as bed materials in low throughput fluidized bed gasification systems
    Asadullah, M
    Miyazawa, T
    Ito, S
    Kunimori, K
    Koyama, S
    Tomishige, K
    [J]. BIOMASS & BIOENERGY, 2004, 26 (03) : 269 - 279
  • [2] Synthetic olivine supported nickel catalysts for gasification of glycerol
    Atong, Duangduen
    Pechyen, Chiravoot
    Aht-Ong, Duangdao
    Sricharoenchaikul, Viboon
    [J]. APPLIED CLAY SCIENCE, 2011, 53 (02) : 244 - 253
  • [3] Synthesis, characterization and photocatalytic activity of TiO2 supported natural palygorskite microfibers
    Bouna, L.
    Rhouta, B.
    Amjoud, M.
    Maury, F.
    Lafont, M. -C.
    Jada, A.
    Senocq, F.
    Daoudi, L.
    [J]. APPLIED CLAY SCIENCE, 2011, 52 (03) : 301 - 311
  • [4] Improving the modeling of the kinetics of the catalytic tar elimination in biomass gasification
    Corella, J
    Toledo, JM
    Aznar, MP
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (14) : 3351 - 3356
  • [5] Performance of CaO and MgO for the hot gas clean up in gasification of a chlorine-containing (RDF) feedstock
    Corella, Jose
    Toledo, Jose M.
    Molina, Gregorio
    [J]. BIORESOURCE TECHNOLOGY, 2008, 99 (16) : 7539 - 7544
  • [6] Biomass gasification with steam in fluidized bed: Effectiveness of CaO, MgO, and CaO-MgO for hot raw gas cleaning
    Delgado, J
    Aznar, MP
    Corella, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) : 1535 - 1543
  • [7] Olivine as tar removal catalyst for biomass gasifiers:: Catalyst characterization
    Devi, L
    Craje, M
    Thüne, P
    Ptasinski, KJ
    Janssen, FJJG
    [J]. APPLIED CATALYSIS A-GENERAL, 2005, 294 (01) : 68 - 79
  • [8] Pretreated olivine as tar removal catalyst for biomass gasifiers: investigation using naphthalene as model biomass tar
    Devi, L
    Ptasinski, KJ
    Janssen, FJJG
    [J]. FUEL PROCESSING TECHNOLOGY, 2005, 86 (06) : 707 - 730
  • [9] 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
  • [10] Adsorption of Pb(II) on palygorskite from aqueous solution: Effects of pH, ionic strength and temperature
    Fan, Qiaohui
    Li, Zhan
    Zhao, Haogui
    Jia, Zehong
    Xu, Junzheng
    Wu, Wangsuo
    [J]. APPLIED CLAY SCIENCE, 2009, 45 (03) : 111 - 116