Unconverted chars obtained during biomass gasification on a pilot-scale gasifier as a source of activated carbon production

被引:30
作者
García-García, A [1 ]
Gregório, A [1 ]
Franco, C [1 ]
Pinto, F [1 ]
Boavida, D [1 ]
Gulyurtlu, I [1 ]
机构
[1] Inst Nacl Engn & Tecnol Ind, Dept Engn Energet & Controle Ambiental, P-1649038 Lisbon, Portugal
关键词
pine wastes; biomass gasification; pilot gasifier; unconverted char; activated carbon; microporosity;
D O I
10.1016/S0960-8524(02)00266-3
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Biomass gasification was used to produce activated carbon on a pilot-scale fluidised-bed gasifier. The feedstock included both biomass alone and biomass mixed with coal and coal/granulated plastic wastes. This paper reports the results obtained from four different runs undertaken under various conditions of fuel supply, different ratios of steam/air for the gasification and temperature. These conditions were selected because they led to a significant amount of unconverted chars produced during gasification (from 0.72 to 1.4 kg) which then served as raw material for the production of activated carbon whilst the amount of gas obtained was also high enough for its potential use for different end-use applications. From the analysis of the results obtained, it can be concluded that a reasonable porosity development (mainly in the area of narrow micropores) was obtained by gasifying unblended pine wastes with steam for 4 h, producing about 1.4 kg of good-quality activated carbon (micropore volume of 0.263 cm(3)/g). In other runs, chars with a reduced microporosity development (i.e. 0.180 cm(3)/g) were obtained, however, they could be used as a proper starting material for the chemically activated carbon production. (C) 2002 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:27 / 32
页数:6
相关论文
共 9 条
[1]  
Bansal R.C., 1988, ACTIVE CARBON
[2]   Novel activation process for preparing highly microporous and mesoporous activated carbons [J].
Hu, ZH ;
Srinivasan, MP ;
Ni, YM .
CARBON, 2001, 39 (06) :877-886
[3]  
JONES JL, 1980, ACS SYM SER, V130, P237
[4]   Preparation of activated carbons from Spanish anthracite I.: Activation by KOH [J].
Lozano-Castelló, D ;
Lillo-Ródenas, MA ;
Cazorla-Amorós, D ;
Linares-Solano, A .
CARBON, 2001, 39 (05) :741-749
[5]   Fluidized-bed co-gasification of residual biomass/poor coal blends for fuel gas production [J].
Pan, YG ;
Velo, E ;
Roca, X ;
Manyà, JJ ;
Puigjaner, L .
FUEL, 2000, 79 (11) :1317-1326
[6]  
ROWELL RM, 1984, ADV CHEM SER, V207, P487
[7]  
SMITH WH, 1986, BIOMASS ENERGY DEV, P321
[8]  
SOFER SS, 1981, BIOMASS CONVERSION P, P145
[9]   Biomass gasification in a laboratory-scale AFBG:: influence of the location of the feeding point on the fuel-N conversion [J].
Vriesman, P ;
Heginuz, E ;
Sjöström, K .
FUEL, 2000, 79 (11) :1371-1378