Biomass gasification with oxygen and steam in a fluidized bed gasifier
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摘要: 在小型流化床气化装置上进行了氧气-水蒸气气化实验,考察了原料、当量比、水蒸气配比、温度、二次风和床料对气化特性的影响。结果表明,原料中C和H含量越高,气化气中H2和CO含量越高,焦油含量越低;当量比为0.27和水蒸气配比为0.6时,H2含量达到最大值;温度的升高可提高H2含量,在840 ℃以上,可提高CO含量;二次风从进料口偏上且二次风比率为15%通入,气体组分变化较明显,二次风通入点位置越高,焦油含量降低幅度越大;白云石和石灰石裂解焦油和提高H2含量的活性高于橄榄石,但同时明显提高了气体中的灰分含量。Abstract: The characteristics of biomass gasification with oxygen-steam mixtures in a fluidized bed are studied in this paper. The effects of feedstock, equivalence ratio (ER), steam to biomass ratio (S/B), gasification temperature, secondary oxygen supply and bed materials on gasification performance were investigated. The results showed that higher C and H content of feedstock was more favorable for higher H2 and CO content and lower tar content of fuel gas. The H2 content increased with gasification temperature and reached its maximum at ER=0.27 and S/B=0.6. Higher gasification temperature (>840 ℃) also contributed to higher CO content. The introduction of secondary flow upper the feedstock inlet with a second flow ratio of 15% improved the gas quality significantly, and more tar was reduced as the secondary flow inlet move upward the gasifier. Dolomite and limestone performed better than olivine on cracking tar and increasing H2 content, but resulted in higher ash content.
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Key words:
- biomass /
- fluidized bed /
- gasification /
- oxygen-steam
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吴创之, 阴秀丽, 徐冰燕, 罗曾凡, 刘平. 生物质富氧气化特性的研究[J]. 太阳能学报, 1997, 18(3): 237-242. (WU Chuang-zhi, YIN Xiu-li, XU Bing-yan, LUO Zeng-fan, LIU Ping. The performance study of biomass gasification with oxygen-rich air[J]. Acta Energiae Solaris Sinica, 1997, 18(3): 237-242.) BASU P. Biomass gasification and pyrolysis: Practical design and theory[M]. Burlington: Academic Press, 2010. GILA J, CORELLA J, AZNAR M P, CABALLEROA M A. Biomass gasification in atmospheric and bubbling fluidized bed: Effect of the type of gasifying agent on the product distribution[J]. Biomass Bioenergy, 1999, 17(5): 389-403. BAKER E, MUDGE L, MITCHELL D. Oxygen/steam gasification of wood in a fixed-bed gasifier[J]. Ind Eng Chem Process Des Dev, 1984, 23(4): 725-728. GIL J, AZNAR M, CABALLERO M, FRANCÉS M, CORELLA1 J. Biomass gasification in fluidized bed at pilot scale with steam-oxygen mixtures. Product distribution for very different operating conditions[J]. Energy Fuels, 1997, 11(6): 1109-1118. FRANCIS S. The hawaiian project[J]. Biomass Bioenergy, 1998, 15(3): 233-238. NARVÁEZ I, ORÍO A, AZNAR M, CORELLA1 J. Biomass gasification with air in an atmospheric bubbling fluidized bed. Effect of six operational variables on the quality of produced raw gas[J]. Ind Eng Chem Res, 1996, 35(7): 2110-2120. DRIFT A V, DOORNA J V, VERMEULENB J W. Ten residual biomass fuels for circulating fluidized-bed gasification[J]. Biomass Bioenergy, 2001, 20(1): 45-56. FRANCO C, PINTO F, GULYURTLU I, CABRITA I. The study of reactions influencing the biomass steam gasification process[J]. Fuel, 2003, 82(7): 835-842. PAASEN S, KIEL J, NEEFT J, KNOEF H, BUFFINGA G, ZIELKE U, SJÖSTRÖM K, BRAGE C, HASLER P, SIMELL P, SUOMALAINEN M, DORRINGTON M, THOMAS L. Guideline for sampling and analysis of tar and particles in biomass producer gases . Petten: ECN, 2002. CORELLA J, TOLEDO J M, PADILLA R. Olivine or dolomite as in-bed additive in biomass gasification with air in a fluidized bed: Which is better?[J]. Energy Fuels, 2004, 18(3): 713-720. XU G W, MURAKAMI T, SUDA T, KUSAMA S, FUJIMORI T. Distinctive effects of CaO additive on atmospheric gasification of biomass at different temperatures[J]. Ind Eng Chem Res, 2005, 44(15): 5864-5868. CHANG C S. Thermal reactions of freshly generated coal tar over calcium oxide. Cambridge: Massachusetts Institute of Technology, 1986. DELGADO J, AZNAR M. Biomass gasification with steam in fluidized bed: Effectiveness of CaO, MgO, and CaO-MgO for hot raw gas cleaning[J]. Ind Eng Chem Res, 1997, 36(5): 1535 -1543. SWIERCZYHSKI D, COURSON C, BEDEL L, KIENNEMANN A, VILMINOT S. Oxidation reduction behavior of iron-rearing olivines (Fe Mg1-x)2SiO4 used as catalysts for biomass gasification[J]. Chem Mater, 2006, 18(4): 897-905. 陈汉平, 杨海平, 李斌, 杨国来, 王贤华, 张世红. 生物质流化床气化焦油析出特性的研究[J]. 燃料化学学报, 2009,37(4): 433-437. (CHEN Han-ping, YANG Hai-ping, LI Bin, YANG Guo-lai, WANG Xian-hua, ZHANG Shi-hong. Evolving characteristics of tar during biomass fluidized bed gasification[J]. Journal of Fuel Chemistry and Technology, 2009, 37(4): 433-437.)
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