期刊文献+

基于ASPEN PLUS平台的生物质气化模拟 被引量:38

Simulation of biomass gasification by ASPEN PLUS
下载PDF
导出
摘要 基于ASPEN PLUS软件的Gibbs自由能最小化法,并利用RGIBBS反应器的限制平衡法修正,建立了生物质气化模型.模拟花生壳气化和木粉气化,发现模拟值和实验值符合良好.对气化两个重要影响因素(空气当量系数和床温)作了灵敏度分析,发现产气组分主要受床温影响,燃气热值和气化效率主要受空气当量系数影响.模拟分析了气化剂温度对产气组分和气化效率的影响,结果表明:基于ASPEN PLUS平台的生物质气化模型能准确地模拟实际气化过程,具有较好的可靠性和适用性. A biomass gasification model was developed by ASPEN PLUS-based Gibbs free energy minimization. The model was modified by the restricted equilibrium of the RGIBBS reactor and used to simulate a peanut shell gasifier and sawdust gasifier. It is found that the simulation results and the experiment results fit well. A sensitivity analysis with equivalence ratio and bed temperature is performed. From the analysis results, the following conclusions are derived, the gas composition is mostly influenced by the bed temperature. The syngas heating value and gasification efficiency are mostly influenced by the equivalence ratio. The effects of air temperature on gas composition and gasification efficiency are also obtained. At last, simulating the .gasification exactly, the model which is based on ASPEN PLUS is proved reliable and applicable.
出处 《华中科技大学学报(自然科学版)》 EI CAS CSCD 北大核心 2007年第9期49-52,共4页 Journal of Huazhong University of Science and Technology(Natural Science Edition)
基金 国家重点基础研究发展计划资助项目(2004CB217704)
关键词 生物质气化 模型 限制平衡 ASPEN PLUS软件 biomass gasification model restricted equilibrium ASPEN PLUS software
  • 相关文献

参考文献10

  • 1Sadaka S S, Ghaly A E, Sabbah M A. Two phase biomass air-steam gasification model for fluidized bed reactors: Part Ⅰ-model development[J]. Biomass and Bioenergy, 2002, 22(6): 439-462.
  • 2Corella J, Sanz A. Modeling circulating fluidized bed biomass gasifiers: a pseudo-rigorous model for stationary state[J]. Fuel Processing Technology, 2005, 86(9) : 1 021-1 053.
  • 3Ong' iro A, Ugursal V I, Al Taweel A M, et al. Thermodynamic simulation and evaluation of a steam CHP plant using ASPEN Plus[J]. Applied Thermal Engineering, 1996, 16(3):263-271.
  • 4Franco C, Pinto F, Gulyurtlu I, et al. The study of reactions influencing the biomass steam gasification process[J]. Fuel, 2003, 82(7): 835-842.
  • 5汪洋,代正华,于广锁,于遵宏.运用Gibbs自由能最小化方法模拟气流床煤气化炉[J].煤炭转化,2004,27(4):27-33. 被引量:86
  • 6米铁,陈汉平,高斌,刘德昌.生物质的流化床热解实验研究[J].华中科技大学学报(自然科学版),2005,33(9):71-74. 被引量:18
  • 7吴创之,吴正舜,郑舜鹏,戴先文.1MW木粉气化发电系统的运行测试研究[J].太阳能学报,2003,24(4):531-535. 被引量:12
  • 8Chen G, Spliethoff H, Andries J, et al. Bionmass gasification in a circulating fluidised bed-Part 1 : preliminary experiments and modelling development[J]. Energy Sources, 2004, 26(5): 465-498.
  • 9Li X T, Grace J R, Lim C J, et al. Biomass gasification in a circulating fluidized bed[J]. Biomass and Bioenergy, 2004, 26(2): 171-193.
  • 10Mathieu P, Dubuisson R. Performance analysis of a biomass gasifier[J]. Energy Conversion and Management, 2002, 43(9-12): 1 291-1 299.

二级参考文献16

  • 1Beenackeeeers A A C M. Solar Energy R&D in the European Community Series E: Advanced gasification[ M]. D.Reidel publishing Company. 1986.
  • 2Reed T B. Biomass gasification principle and technology[ M]. United States, 1981.
  • 3Palz W,Chartier P,Hall D O. Energy from biomass[ M].London: Applied Science Publishers Ltd, 1981.
  • 4Wu C, Yin X,Zheng S,et al. A Demonstration Project for Biomass Gasification and Power Generation in China[A].Symposium on Biomass Thermo-chemical conversion[C],Tyrol, Austria, Sep, 18-25,2000.
  • 5Varhegyi G, Jakab E, Antal M J. Is the broido-shafizadeh model for cellulose pyrolysis true[J].Energy and Fuels, 1994, 8:1345-1355.
  • 6Corella J, Orio A, Toledo J M. Biomass gasification with air in fluidized:reforming of the gas composition with commerical steam catalyst[J].Ind Eng Chen Res, 1998, 37(12):4617-4626.
  • 7Azbar M, Caballero M, Gil J, et al. Commercial steam reforming catalysts to improve biomass gasification with steam-oxygen mixtures[J].Ind Eng Chen Res, 1998, 37(7):2668-2680.
  • 8Scott D S, Piskorz J. The continuous.ash pyrolysis of biomass[J].Can J Chem Eng, 1984, 62:404-412.
  • 9Sjostrom K, Chen G, Yu Q, et al. Promoted reactivity of char in co-gasification of biomass and coal:Synergies in the thermo-chemical process[J].Fuel, 1999, 78:1189-1194.
  • 10Watkinson A P, Lucas J P, Lim C J. A Prediction of Performance of Commercial Coal Gasifiers. Fuel, 1991, 70:519-527

共引文献113

同被引文献257

引证文献38

二级引证文献153

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