Challenges in the production of sustainable fuels from pyrolysis oil - Design of efficient catalysts for gasification of char

被引:11
作者
Guell, B. Matas [1 ]
van Rossum, G. [1 ]
van Swaaij, W. P. M. [1 ]
Kersten, S. R. A. [1 ]
Lefferts, L. [1 ]
Seshan, K. [1 ]
机构
[1] Univ Twente, Fac Sci & Technol, NL-7500 AE Enschede, Netherlands
关键词
Char; Gasification; Catalyst; Ceria; Pyrolysis-oil; Activation energy; WATER-GAS SHIFT; FLUIDIZED-BED REACTOR; PT/CEO2; CATALYST; CARBON-DIOXIDE; BROWN COAL; STEAM; REACTIVITY; OXIDES; CERIA; POTASSIUM;
D O I
10.1016/j.apcatb.2010.10.033
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070305 [高分子化学与物理];
摘要
The catalytic performance of a ceria-zirconia based catalyst for (i) steam/CO2 gasification and (ii) combustion of char produced during pyrolysis oil evaporation was investigated and compared with the non-catalytic scenario in the temperature range 600-800 degrees C. Kinetic studies revealed that the presence of the ceria-zirconia catalyst enhanced char gasification rates significantly, up to one order of magnitude at 800 degrees C, for both steam and CO2 gasification. It is suggested that the red-ox properties of the ceria-zirconia catalyst play a significant role in char gasification, by allowing oxygen mobility and activation of H2O and CO2. Furthermore, XPS and SEM characterization studies showed that the catalyst also influences the nature of char formed during pyrolysis-oil evaporation to a great extent, by forming oxygenated species which are expected to be more reactive. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:587 / 597
页数:11
相关论文
共 41 条
[1]
[Anonymous], 1992, HIGH RESOLUTION XPS, DOI DOI 10.1002/ADMA.19930051035
[2]
[Anonymous], 1995, Handbook of X-ray Photoelectron Spectroscopy. A Reference Book of Standard Spectra for Identification and Interpretation of XPS Data
[3]
Changes in coal char reactivity and texture during combustion in an entrained flow reactor [J].
Arias, B. ;
Pevida, C. ;
Rubiera, F. ;
Pis, J. J. .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2007, 90 (03) :859-863
[4]
Bifunctional catalysts for single-stage water-gas shift reaction in fuel cell applications. Part 1. Effect of the support on the reaction sequence [J].
Azzam, K. G. ;
Babich, I. V. ;
Seshan, K. ;
Lefferts, L. .
JOURNAL OF CATALYSIS, 2007, 251 (01) :153-162
[5]
WATER-INSOLUBLE COMPOUNDS FORMED BY REACTION BETWEEN POTASSIUM AND MINERAL MATTER IN CATALYTIC COAL-GASIFICATION [J].
BRUNO, G ;
BURONI, M ;
CARVANI, L ;
DELPIERO, G ;
PASSONI, G .
FUEL, 1988, 67 (01) :67-72
[6]
Studies of inorganics added to low-rank coals for catalytic gasification [J].
Domazetis, G ;
Liesegang, J ;
James, BD .
FUEL PROCESSING TECHNOLOGY, 2005, 86 (05) :463-486
[7]
Active nonmetallic Au and Pt species on ceria-based water-gas shift catalysts [J].
Fu, Q ;
Saltsburg, H ;
Flytzani-Stephanopoulos, M .
SCIENCE, 2003, 301 (5635) :935-938
[8]
Design of a stable steam reforming catalyst-A promising route to sustainable hydrogen from biomass oxygenates [J].
Guell, B. Matas ;
Babich, I. ;
Nichols, K. P. ;
Gardeniers, J. G. E. ;
Lefferts, L. ;
Seshan, K. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2009, 90 (1-2) :38-44
[9]
Propan-2-ol transformation on simple metal oxides TiO2, ZrO2 and CeO2 [J].
Haffad, D ;
Chambellan, A ;
Lavalley, JC .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2001, 168 (1-2) :153-164
[10]
VARIATION OF RATE DURING POTASSIUM-CATALYZED CO2 GASIFICATION OF COAL CHAR [J].
HAMILTON, RT ;
SAMS, DA ;
SHADMAN, F .
FUEL, 1984, 63 (07) :1008-1012