期刊文献+

Energetic analysis of gasification of biomass by partial oxidation in supercritical water 被引量:1

生物质超临界水部分氧化气化的能量过程分析(英文)
下载PDF
导出
摘要 Partial oxidation gasification in supercritical water could produce fuel gases(such as H2, CO and CH4) and significantly reduce the energy consumption. In this work, an energetic model was developed to analyze the partial oxidative gasification of biomass(glucose and lignin) in supercritical water and the related key factors on which gasification under autothermal condition depended upon. The results indicated that the oxidant equivalent ratio(ER) should be over 0.3 as the concern about energy balance but less than 0.6 as the concern about fuel gas production. Feedstocks such as glucose and lignin also had different energy recovery efficiency. For materials which can be efficiently gasified, the partial oxidation might be a way for energy based on the combustion of fuel gases. Aromatic materials such as lignin and coal are more potential since partial oxidation could produce similar amount of fuel gases as direct gasification and offer additional energy. Energy recovered pays a key role to achieve an autothermal process. Keeping heat exchanger efficiency above 80% and heat transfer coefficient below15 k J·s-1is necessary to maintain the autothermal status. The results also indicated that the biomass loading should be above 15% but under 20% for an autothermal gasification, since the increase of biomass loading could improve the energy supplied but decrease the efficiency of gasification and gaseous yields. In general,some specific conditions exist among different materials. Partial oxidation gasification in supercritical water could produce fuel gases(such as H2, CO and CH4) and significantly reduce the energy consumption. In this work, an energetic model was developed to analyze the partial oxidative gasification of biomass(glucose and lignin) in supercritical water and the related key factors on which gasification under autothermal condition depended upon. The results indicated that the oxidant equivalent ratio(ER) should be over 0.3 as the concern about energy balance but less than 0.6 as the concern about fuel gas production. Feedstocks such as glucose and lignin also had different energy recovery efficiency. For materials which can be efficiently gasified, the partial oxidation might be a way for energy based on the combustion of fuel gases. Aromatic materials such as lignin and coal are more potential since partial oxidation could produce similar amount of fuel gases as direct gasification and offer additional energy. Energy recovered pays a key role to achieve an autothermal process. Keeping heat exchanger efficiency above 80% and heat transfer coefficient below15 k J·s-1is necessary to maintain the autothermal status. The results also indicated that the biomass loading should be above 15% but under 20% for an autothermal gasification, since the increase of biomass loading could improve the energy supplied but decrease the efficiency of gasification and gaseous yields. In general,some specific conditions exist among different materials.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2015年第1期205-212,共8页 中国化学工程学报(英文版)
基金 Supported by the National Natural Science Foundation of China(21037001,21076091,21307049) the National Key Project for Basic Research of China(2008BAC32B06-1) Yunnan Province High-tech Talent Introduction Project(2010CI110) the Important Yunnan Province's Science&Technology Specific Project(2012ZB002) the Yunnan Science Foundation(2013FZ032,14118583)
关键词 AUTOTHERMAL GASIFICATION Supercritical water BIOMASS Energetic model 部分氧化反应 生物质气化 能量分析 超临界水 可燃气体 燃料气体 气化原料 木质素
  • 相关文献

参考文献3

二级参考文献32

  • 1苏东海,孙君社,刘萍,吕燕萍.Effects of Different Pretreatment Modes on the Enzymatic Digestibility of Corn Leaf and Corn Stalk[J].Chinese Journal of Chemical Engineering,2006,14(6):796-801. 被引量:8
  • 2吴学华,苏磊,刘秀茹,陈丽英,陈克宇,洪时明.超临界水中过氧化苯甲酰对聚乙烯降解的促进作用[J].高分子材料科学与工程,2006,22(1):135-137. 被引量:1
  • 3Serio, M.A., Kroo, E., Wojtowicz, M.A., "Biomass pyrolysis for distributed energy generation", Prepr. Pap.-Am. Chem. Soc., Div. Fuel Chem., 48, 584-589 (2003).
  • 4Chen, Y.G., Charpeny, S., Jensen, A., Wojtowicz, M.A., Serio, M.A., "Modelling of biomass pyrolysis kinetics", Symposium (Interna- tional) on Combustion, 27 (1), 1327-1334 (1998).
  • 5Eckhoff, R.K., Dust Explosion in the Process Industries, Butterworth Heinemann, Oxford (1997).
  • 6Lee, D.H., Kwon, S., "Heat transfer and quenching analysis of combustion in a micro combustion vessel", J. Micromech. Microeng. 12, 670-676 (2002).
  • 7Lee, D.H., Park, D.E., Yoon, E., Kwon, S., "A MEMS pis- ton-cylinder device actuated by combustion", ASME J. Heat Transf, 125, 487-493 (2003).
  • 8Daou, J., Matalon, M., "Influence of conductive heat-losses on the propagation of premixed flames in channels", Combust. Flame, 128, 321-339 (2002).
  • 9Vican, J., Gajdeczko, B.F., Dryer, EL., Milius, D.L., Aksay, I.A., Yetter, R.A., "Development of a microreactor as a thermal source for micro-electro-mechanical systems power generation", Proc. Corn- bust. Inst., 29, 909-916 (2002).
  • 10Hua, J., Wu, M., Kumar, K., "Numerical simulation of the com- bustion of hydrogen-air mixture in micro-scaled chambers. Part I: Fundamental study", Chem. Eng. Sci., 60, 3497-3506 (2005).

共引文献11

同被引文献2

引证文献1

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部