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湿生物质催化气化固体产物的微观结构分析

Microstructure Analysis of Solid Products of Wet Biomass Catalytic Gasification with CO_2 Absorption
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摘要 为深入地认识一种伴随有CO2吸收的湿生物质催化气化技术,对该过程中有代表性的固相:如,半焦、吸收剂、催化气化固体残留物进行微观结构分析.结果表明:湿生物质半焦具有更加丰富的微孔结构,其比表面积和孔容积相对于干物质半焦分别增加了17%和19%;Ca(OH)2以及水合Ca(OH)2的高温分解能提高比表面积和孔容积,且产物CaO的孔径分布随水合Ca(OH)2中水分含量的增加而上升.温度对湿生物质催化气化固体残留物的微观结构有较大的影响,随着温度的升高,其比表面积曲线呈S型,孔容积曲线则先略微降低后迅速升高. To investigate the catalytic gasification of wet biomass with CO2 absorption, the microstructure of several representative solids, such as biomass semicoke, absorbents, and solid residues of catalytic gasification of biomass, was determined with N2 adsorption. The results show that the semicoke of wet biomass has more plentiful micropores than that of dry biomass, and its specific surface area(ABET) and total pore volume(Vp) is increased by 17% and 19%, respectively. Both ABET and Vp of CaO are much higher than that of its precursors (Ca(OH)2 and hydrated Ca(OH)2). The PSD of CaO increases as the ratio of water to Ca(OH)2 increases. Furthermore, with the increase of reactor temperature, the trend of ABET curve presents 'S' type, and Vp curve decreases slightly, and then fast increases.
作者 黄浩 胡国新
出处 《上海交通大学学报》 EI CAS CSCD 北大核心 2009年第2期247-250,共4页 Journal of Shanghai Jiaotong University
基金 国家级星火计划资助项目(2006EA105033)
关键词 湿生物质 催化气化 比表面积 孔容积 孔径分布 wet biomass catalytic gasification specific surface area total pore volume pore size distribution
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参考文献8

  • 1李俊峰,王仲颖,梁志鹏,时景丽.我国未来可再生能源开发利用的战略思考[J].中国能源,2004,26(3):4-10. 被引量:55
  • 2Demirbas A. Biomass resource facilities and biomass conversion process for fuel and chemicals[J]. Energy Conversion and Management, 2001, 42 ( 11 ) : 1357- 1371.
  • 3吕鹏梅,常杰,熊祖鸿,吴创之,陈勇.生物质在流化床中的空气-水蒸气气化研究[J].燃料化学学报,2003,31(4):305-310. 被引量:52
  • 4Delgado J, Aznar M P,Corella J. 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.
  • 5Aznar M P, Caballero M A, Gil J. Commercial steam reforming catalysts to improve biomass gasification with steam-oxygen mixtures. 2. Vatalytic tar removal [J]. Ind Eng Chem Res, 1998. 37(7), 2668-2680.
  • 6黄浩,胡国新.Ca(OH)_2对生物质水蒸气气化制氢的影响[J].上海交通大学学报,2007,41(12):1930-1933. 被引量:8
  • 7Hanaokaa T, Yoshidaa Y, Fuiimotoa S J, et al. Hydrogen production from woody biomass by steam gasi- fication using a CO2 sorbent[J]. Biomass and Bioenergy, 2005,28(1) :63-68.
  • 8Gregg S J, Sing K S W. Adsorption, surface area and porosity [M]. London: Academic Press, 1982.

二级参考文献23

  • 1刘江华,方新湘,周华.我国氢能源开发与生物制氢研究现状[J].新疆农业科学,2004,41(F08):85-87. 被引量:9
  • 2吴创之,徐冰嬿,罗曾凡,阴秀丽.生物质中热值气化技术的分析及探讨[J].煤气与热力,1995,15(2):8-14. 被引量:23
  • 3Delgado J, Aznar M P. 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.
  • 4Rapagnà S, Jand N, Kiennemann A, et al . Steam-gasification of biomass in a fluidized-bed of olivine particles[J]. Biomass Bioenergy, 2000, 19(3): 187-197.
  • 5Schuster G, L ffler G, Weigl K, et al . Biomass steam gasification-an extensive parametric modeling study[J]. Bioresour Technol,2001, 77(1): 71-79.
  • 6Pan Y G, Velo E, Roca X, et al . Fluidized-bed co-gasification of residual biomass/poor coal blends for fuel gas production[J].Fuel, 2000, 79(11): 1317-1326.
  • 7Turn S, Kinoshita C, zhang Z, et al . An experimental investigation of hydrogen production from biomass gasification[J]. Int J Hydrogen Energy, 1998, 23(8): 641-648.
  • 8Colomba Di Blasi. Kinetic and heat transfer control in the slow and flash pyrolysis of solids[J]. Ind Eng Chem Res, 1996, 36(1):37-46.
  • 9Delgado J. Maria P A. Josc C. 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.
  • 10Ximena A G, Nelson A A, Gordon A L. Steam gasi fication of tars using a CaO catalyst [J]. Fuel Processing Technology, 1999. 58: 83-102.

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