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稻草水热法液化的实验研究 被引量:10

Experimental research on the thermochemical liquefaction of straw
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摘要 以农业废物稻草为研究对象,利用非等温技术,考察了农业废物在亚临界水(温度350℃,压力约20MPa)及超临界水(温度380℃,压力约30MPa)中的液化行为,并对反应获得的固体残渣和生物油进行了分析。实验结果表明,固体残渣的结构遭到较严重的破坏,质地变得松散,有利于进行生物发酵。实验获得的生物油成分主要为酮类和酚类的衍生物,其能量密度比原料提高将近一倍,但是黏度较大,酸性较强。在超临界状态下,固体残渣得率较低,液化效率高,获得的生物油的组分相对简单,酸性较弱,故稻草在超临界水中的液化优于其在亚临界水中的液化。 Agricultural refuse (straw) liquefaction in suberitieal water (T = 350℃ ,P = 20MPa) and supereritieal water ( T = 380℃ , P = 30MPa) with a non-isothermal technique was studied, and the analysis of residue and bio-oil was carried out. The structure of solid residue has been destroyed and the texture got looser, which can be fermented more easily. The bio-oil obtained in liquefaction has dowbled the energy density of straw. But the viscidity and acidity of bio-oil was high. Ketone and phenol derivates are the main components. The yield of solid residue is lower in supereritieal water than in suberitieal water and the component of the bio-oil obtained in supereritieal water is simpler, moreover, the acidity is weaker. The liquefaction in supereritieal water is superior to that in suberitieal water.
出处 《能源工程》 2006年第2期34-38,共5页 Energy Engineering
基金 国家863高技术资助项目(2004AA649370)
关键词 稻草 热化学液化 亚临界水 超临界水 生物油 straw thermochemical liquefaction subcritical water supercritical water bio-oil
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参考文献16

  • 1A V Bridgwater,G V C Peacocke.Fast pyrolysis processes for biomass[J].Renewable ﹠ Sustainable Energy Reviews,2000,(4):1-73.
  • 2A Demirbs.Mechanisms of liquefaction and pyrolysis reactions of biomass.Energy Conversion﹠Management[J].2000,41:633-646.
  • 3王树荣,骆仲泱,董良杰,洪军,谷月玲,廖艳芬,方梦祥,倪明江,岑可法.生物质闪速热裂解制取生物油的试验研究[J].太阳能学报,2002,23(1):4-10. 被引量:72
  • 4王树荣,骆仲泱,谭洪,洪军,董良杰,方梦祥,岑可法.生物质热裂解生物油特性的分析研究[J].工程热物理学报,2004,25(6):1049-1052. 被引量:77
  • 5赵明,吴文权,卢玫,魏晓阳.稻草热裂解动力学研究[J].农业工程学报,2002,18(1):107-110. 被引量:32
  • 6廖艳芬,王树荣,洪军,谷月玲,骆仲泱,岑可法.生物质热裂解制取液体燃料的实验研究[J].能源工程,2002,22(3):1-3. 被引量:26
  • 7H F Gercel.The production and evaluation of biooils from the pyrolysis of sunflower oil cake[J].Biomass﹠Bioenergy,2002,23:301-314.
  • 8A Kruse,A Gawlik.Biomass conversion in water at 330-410℃and 30-50MPa:identification of key compounds for indicating different chemical receation pathways[J].Ind Eng Chem Res,2003,42:267-279.
  • 9Z Fang,T Minowa.Liquefaction and gasification of cellulose with Na2CO3 and Ni in subcritical water at 350℃[J].Ind Eng Chem Res,2004,43:2454-2463.
  • 10朱自强.超临界流体技术--原理和应用[M].北京:化学工业出版社,2003.

二级参考文献25

  • 1丁素珍,王孟杰.生物质能的开发与利用[J].农业工程学报,1993,9(4):51-57. 被引量:18
  • 2董良杰.生物质热裂解技术及其反应动力学[M].沈阳:沈阳农业大学,1997..
  • 3王树荣 廖艳芬 等.生物质热裂解制油的动力学及技术研究.高等学校工程热物理研究会第八届全国学术会议[M].,2000.350-356.
  • 4[3]Demirbas A . Mechanisms of liquefaction and pyrolysis reactions of biomass [J]. Energy Conversion & Management 2000,41:633~646.
  • 5[5]Hu H Q,Zhang J,Guo S C,et al. Extraction of Huadian oil shale with water in sub-and supercritical states[J]. Fuel, 1999, 78(6): 645~651. .
  • 6[6]Missal P, Hu H Q, Guo S C. Vergleich der extraction von Kohle mit Toluol und mit Zusatz des H-donors Tetralin[J]. Erdoel Erdgas und Kohle, 1992, 108(6): 279~283.
  • 7[1]Bridgwater A V, Peacocke G V C. Fast Pyrolysis Processing for Biomass. Renewable and Sustainable Energy Reviews, 2000, 4:1-73
  • 8[2]Peacocke G V C, Russell P A, Jenkins J D, et al. Physical Properties of Flash Pyrolysis Liquids. Biomass and Energy, 1994, 7(1-6): 169-177
  • 9[3]Rick F, Vix U. Product Standards for Pyrolysis Products for Use as Fuel in Industrial Firing Plant. In: Biomass Pyrolysis Liquids Upgrading and Utilization, ed. Bridgwater A V, Grassi G. London: Elsevier Applied Science,1991. 177-218
  • 10[5]Bridgwater A V, Cottam M L. Opportunities for Biomass Pyrolysis LiquidsProduction and Upgrading. Energy and Fuels, 1992, 6(2): 113-120

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