The gasification of wet biomass using Ca(OH)2 as CO2 absorbent: The microstructure of char and absorbent

被引:15
作者
Hu Guoxin [1 ]
Huang Hao [1 ]
Li Yanhong [1 ]
机构
[1] Shanghai Jiao Tong Univ, Sch Mech & Power Engn, Shanghai 200240, Peoples R China
关键词
Microstructure; Surface area; Total pore volume; Pore size distribution; Wet biomass;
D O I
10.1016/j.ijhydene.2008.06.064
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 [物理化学]; 081704 [应用化学];
摘要
Aimed at the hydrogen production by gasification of wet biomass coupled CO2 absorption, the microstructures of chars produced from gasification of wet/pre-dried biomass and several possible stages of absorbent were studied with N-2 adsorption, XRD and SEM. The results show that all the chars examined have essentially microporous structures of pore size less than 2 nm, and the char obtained from gasification of wet biomass at 923 K exhibits larger surface area (A(BET)) of 430.87 m(2) g(-1) and total pore volume (V-pore) Of 0.188 m(3) g(-1) than those (368.15 m(2) g(-1) and 0.157 m(3) g(-1)) from pre-dried biomass at the same temperature. The great change of microstructures in the absorbents was observed in the gasification process. The CaO generated from the dehydration of Ca(OH)(2) has larger A(BET) and V-pore, than its former Ca(OH)(2), and the increase of pore mainly belongs to mesopores ranges (pore size between 2 nm and SO nm). However, the generated CaO suffers from a jam of mesopores with the formation of CaCO3 which will cause incomplete utilization. Although the burning of SR sample can realize CaO generation, the regenerated CaO with a totally deteriorated pore networks suggests poor reactivity. With the increase of temperature the CO2 absorption by CaO is weakened gradually except in low temperature range of less than 973 K, meaning that the maximum temperature of the process should not exceed the decomposition temperature of CaCO3. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:5422 / 5429
页数:8
相关论文
共 24 条
[1]
CATALYSIS IN THERMAL BIOMASS CONVERSION [J].
BRIDGWATER, AV .
APPLIED CATALYSIS A-GENERAL, 1994, 116 (1-2) :5-47
[2]
Adsorption of gases in multimolecular layers [J].
Brunauer, S ;
Emmett, PH ;
Teller, E .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1938, 60 :309-319
[3]
Biomass gasification in fluidized bed: Where to locate the dolomite to improve gasification? [J].
Corella, J ;
Aznar, MP ;
Gil, J ;
Caballero, MA .
ENERGY & FUELS, 1999, 13 (06) :1122-1127
[4]
Hydrogen production from biomass gasification on nickel catalysts - Tests for dry reforming of methane [J].
Courson, C ;
Udron, L ;
Swierczynski, D ;
Petit, C ;
Kiennemann, A .
CATALYSIS TODAY, 2002, 76 (01) :75-86
[5]
Hydrogen production from the fermentation of corn stover biomass pretreated with a steam-explosion process [J].
Datar, Rohit ;
Huang, Jie ;
Maness, Pin-Ching ;
Mohagheghi, Ali ;
Czemik, Stefan ;
Chornet, Esteban .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (08) :932-939
[6]
Biomass gasification with steam in fluidized bed: Effectiveness of CaO, MgO, and CaO-MgO for hot raw gas cleaning [J].
Delgado, J ;
Aznar, MP ;
Corella, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) :1535-1543
[7]
Gaseous products from biomass by pyrolysis and gasification: effects of catalyst on hydrogen yield [J].
Demirbas, A .
ENERGY CONVERSION AND MANAGEMENT, 2002, 43 (07) :897-909
[8]
Hydrogen production from biomass coupled with carbon dioxide capture: The implications of thermodynamic equilibrium [J].
Florin, Nicholas H. ;
Harris, Andrew T. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (17) :4119-4134
[9]
Steam gasification of tars using a CaO catalyst [J].
García, XA ;
Alarcón, NA ;
Gordon, AL .
FUEL PROCESSING TECHNOLOGY, 1999, 58 (2-3) :83-102
[10]
Gregg S. J., 1982, ABSORPTION SURFACE A