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生物质快速热裂解主要参数对产物产率及其分布的影响(英文) 被引量:20

Effects of biomass fast pyrolysis key parameters on yields and distributions of products
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摘要 在生物质喂入率为 0 .8~ 2 .0 kg· h- 1的流化床上以木屑为原料进行了快速热裂解试验 ,系统研究了木屑热裂解过程中的流化床反应器温度、生物质粒径和气相滞留期三个主要参数对热裂解产物产率的影响。结果表明 ,当反应器温度在45 0~ 6 0 0℃之间变化时 ,在 5 0 0℃条件下 ,生物油产率最高 ,其值为 5 3.33%,而木炭及不可冷凝气体产率分别为 8.97%和37.70 %。当温度为 5 0 0℃ ,木屑粒径在 0 .90 mm以下时 ,粒径在 0 .45~ 0 .6 0 mm范围内的生物油产率最大 ,达到 5 8.2 3%,这时木炭产率为 8.2 3%。对粒径小于 0 .2 0 m m的木屑在温度 5 0 0℃ ,气相滞留期 0 .80 ,1.2 0 ,1.5 0 s三个量级上的热裂解表明 ,气相滞留期为 0 .80 s时 ,生物油产率达到最大值为 6 2 .6 0 %。但是 ,当气相滞留期较长时 (1.5 0 s) ,生物油产率稍有下降。生物油是极性有机物与水的可溶混合物。因此 ,木屑快速热裂解生产液体燃料具有较大的潜力。 Sawdust fast pyrolysis experiments were conducted in a fluidized bed reactor at a biomass feed rate of 0.80~2.00 kg·h -1. The effects of process conditions, like fluidized bed reactor temperature, feed size and vapor residence time on the product yields were studied. When reactor temperatures were varied from 450℃ to 600℃, a maximum bio-oil yield of 53.33%wt was achieved at 500℃ with a char and gaseous yields of 8.97 %wt and 37.70%wt respectively. The particle size of sawdust varied in the range of 0~0.90 mm. The yield of bio-oil was maximum (58.23%wt of biomass feed) for the particle size of 0.45~0.60 mm with a char yield of 8.23%wt. Vapor residence times were ranged from 0.80 to 1.50 s at temperature of 500℃ with a particle size less than 0.20 mm. A maximum bio-oil yield of 62.60%wt was achieved at 500℃ when the vapor residence time was held constant at 0.80 s. However, at the longer residence time(1.50 s), bio-oil yield was slightly lower. Bio-oil is a miscible mixture of polar organics with water. The results showed the potential of sawdust fast pyrolysis for liquid hydrocarbon fuels production.
出处 《农业工程学报》 EI CAS CSCD 北大核心 2003年第5期204-208,共5页 Transactions of the Chinese Society of Agricultural Engineering
基金 National Natural Science Foundation of China(50 2 760 39) Natural Science Foundation Liaoning Province(0 0 2 0 4 6)
关键词 生物质 热裂解 生物油 流化床反应器 biomass pyrolysis bio-oil fluidized bed reactor
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  • 1Zabaniotou A A, Roussos A I, Koroneos C J. A laboratory study of cotton gin waste pyrolysis[J]. Journal of Analytical and Applied Pyrolysis, 2000, 56:47-59.
  • 2Dai Lin, Li Jingming, Ralph Overand. Biomass energy conversion technologies in China. development and evaluation[M]. Beijing: Chinese Environmental Science Press, 1998.
  • 3Bain R L. Electricity from biomass in the United States:Status and future direction[J]. Bioresource Technology,1993,46(1-2) :86-93.
  • 4Bridgwater A V, Meier D, Radlein D. An overview of fast pyrolysis [J]. Organic Geochemistry 1999, 30 (12) :1479-1493.
  • 5Bridgwater A V, Peacocke G V C. Fast pyrolysis process for biomass [J]. Renewable and Sustainable Energy Reviews, 2000,4 ( 1 ) : 1 - 73.
  • 6Scoltes E J. Of biomass pyrolysis, and liquid the refrom[A]. In: Scoltes E J. Pyrolysis oils from biomass,producing, analyzing, and upgrading [ C]. American Chemical Society. 1988. 1-7.
  • 7Niu Weisheng. Design and experimental research of small fluidized bed reactor for biomass pyrolysis[D]. Shenyang:College of Agricultural Engineering, Shenyang Agricultural University, 2000.
  • 8Scott D S, Piskorz J. The continuous flash pyrolysis of biomass[J]. Can J Chem Eng, 1984,62:404-412.
  • 9Yu Xiaofang. Experimental research of biomass pyrolysis for liquid production in a small fluidized bed reactor[D].Shenyang: College of Agricultural Engineering, Shenyang Agricultural University, 2002.
  • 10Li Tianshu. Analysis of main factors and experimental research for biomass pyrolysis[D]. Shenyang: College of Agricultural Engineering, Shenyang Agricultural University, 2003.

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