Effect of Fe-olivine on the tar content during biomass gasification in a dual fluidized bed

被引:168
作者
Virginie, M. [1 ]
Adanez, J. [2 ]
Courson, C. [1 ]
de Diego, L. F. [2 ]
Garcia-Labiano, F. [2 ]
Niznansky, D. [3 ]
Kiennemann, A. [1 ]
Gayan, P. [2 ]
Abad, A. [2 ]
机构
[1] Surfaces & Procedes Catalyse UMR 7515, Lab Mat, F-67087 Strasbourg, France
[2] Inst Carboquim ICB CSIC, Environm & Energy Dept, Zaragoza 50018, Spain
[3] Charles Univ Prague, Dept Inorgan Chem, Fac Nat Sci, Prague 12843 2, Czech Republic
关键词
Fe/olivine catalyst; Biomass gasification; Tar removal; Dual fluidized bed; BREAKDOWN CATALYST; STEAM-GASIFICATION; IRON; GAS; MOSSBAUER; REDUCTION; CRACKING; GASIFIERS; HYDROGEN;
D O I
10.1016/j.apcatb.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
The Fe/olivine catalyst effectiveness regarding tar primary reduction during biomass gasification in dual fluidized beds has been investigated. The use of Fe/olivine instead olivine leads to an important decrease in the amount of produced tar, which was reduced by up to 65% at 850 degrees C, naphthalene being the most stable molecule. It has been found that Fe/olivine materials have a double effect on tar destruction. On the one hand, they act as a catalyst for tar and hydrocarbon reforming. On the other hand, they can act as an oxygen carrier that transfers oxygen from the combustor to the gasifier, and part of the oxygen is used to burn volatile compounds. The catalyst was fairly stable because the result was confirmed during 48 h of continuous operation. The Fe/olivine material characterization (X-ray diffraction, Mossbauer spectroscopy, temperature programmed reduction and oxidation, etc.) revealed that the catalyst structure was maintained despite the large number of oxidizing-reducing cycles. The carbon that formed on the catalyst surface was low and easily oxidized in the combustion zone. Therefore, the inexpensive and non-toxic Fe/olivine catalyst is a material suitable for use as primary catalyst in a fluidized bed gasification of biomass. (c) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:214 / 222
页数:9
相关论文
共 46 条
[1]   Progress in Chemical-Looping Combustion and Reforming technologies [J].
Adanez, Juan ;
Abad, Alberto ;
Garcia-Labiano, Francisco ;
Gayan, Pilar ;
de Diego, Luis F. .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2012, 38 (02) :215-282
[2]   Tar reduction in biomass producer gas via mechanical, catalytic and thermal methods: A review [J].
Anis, Samsudin ;
Zainal, Z. A. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2011, 15 (05) :2355-2377
[3]   Mossbauer study of transformation mechanism of Fe cations in olivine after thermal treatments in air [J].
Barcova, K ;
Mashlan, M ;
Zboril, R ;
Martinec, P .
JOURNAL OF RADIOANALYTICAL AND NUCLEAR CHEMISTRY, 2003, 255 (03) :529-533
[4]   NUCLEATION AND GROWTH OF IRON OXIDES IN OLIVINES, (MG,FE)2SIO4 [J].
CHAMPNESS, PE .
MINERALOGICAL MAGAZINE, 1970, 37 (291) :790-+
[5]   Olivine as tar removal catalyst for biomass gasifiers:: Catalyst characterization [J].
Devi, L ;
Craje, M ;
Thüne, P ;
Ptasinski, KJ ;
Janssen, FJJG .
APPLIED CATALYSIS A-GENERAL, 2005, 294 (01) :68-79
[6]   Biomass Gasification with Catalytic Tar Reforming: A Model Study into Activity Enhancement of Calcium- and Magnesium-Oxide-Based Catalytic Materials by Incorporation of Iron [J].
Di Felice, L. ;
Courson, C. ;
Niznansky, D. ;
Foscolo, P. U. ;
Kiennemann, A. .
ENERGY & FUELS, 2010, 24 (07) :4034-4045
[7]   Iron and nickel doped alkaline-earth catalysts for biomass gasification with simultaneous tar reformation and CO2 capture [J].
Di Felice, Luca ;
Courson, Claire ;
Foscolo, Pier Ugo ;
Kiennemann, Alain .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (09) :5296-5310
[8]   SURFACE AND INTERFACE PROPERTIES OF EPITAXIAL FE3O4 FILMS STUDIED BY MOSSBAUER-SPECTROSCOPY [J].
FUJII, T ;
TAKANO, M ;
KATANO, R ;
ISOZUMI, Y ;
BANDO, Y .
JOURNAL OF MAGNETISM AND MAGNETIC MATERIALS, 1994, 130 (1-3) :267-274
[9]   RESIDUAL OIL CRACKING WITH GENERATION OF HYDROGEN - DEACTIVATION OF IRON-OXIDE CATALYST IN THE STEAM IRON REACTION [J].
FUKASE, S ;
SUZUKA, T .
APPLIED CATALYSIS A-GENERAL, 1993, 100 (01) :1-17
[10]   Modeling of biomass gasification in fluidized bed [J].
Gomez-Barea, A. ;
Leckner, B. .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2010, 36 (04) :444-509