期刊文献+

二段式干煤粉气流床气化技术的模拟研究与分析 被引量:83

SIMULATION AND ANALYSIS ON GASIFICATION TECHNOLOGY OF A TWO-STAGE DRY FEED ENTRAINED FLOW BED
下载PDF
导出
摘要 提出了将煤的热解模型、气固间非均相反应模型和气相间均相反应模型与ASPEN PLUS图形建模法相结合的二段式干煤粉气流床气化工艺的模拟计算方法,并对其性能进行了模拟研究与分析.模拟研究表明,二段式干煤粉气流床气化工艺可以降低出口煤气的温度,为简化工艺过程,降低煤气冷却器的几何尺寸提供了可能.采用该气化方式可以提高气化炉的冷煤气效率2~6个百分点. Based on ASPEN PLUS, a simulating method of two-stage dry feed entrained flow bed gasification technology is presented, in which a thermal decomposition model, a gas-solid heterogeneous reaction model and a gas-gas homogeneous reaction model are integrated for action. A simulating on the performance of proposed technology is proceeded resulting in reduction of outlet temperature of gas, that allows to reduce geometry size of syngas cooler and to simplify the technology process, and of the all the cold gas efficiency will be promoted 2~6 percent points.
出处 《中国电机工程学报》 EI CSCD 北大核心 2003年第10期186-190,共5页 Proceedings of the CSEE
基金 国家高技术研究发展计划(863计划)(2003AA522030)~~
关键词 二段式干煤粉气流床 煤气化 气化炉 煤气效率 气化工艺 Gasification Two-stage gasification techno-logy Gasifier Dry feed entrained flow bed
  • 相关文献

参考文献9

  • 1徐越,吴一宁,危师让.基于ASPEN PLUS平台的干煤粉加压气流床气化性能模拟[J].西安交通大学学报,2003,37(7):692-694. 被引量:41
  • 2国家电力公司热工研究院.两段式干煤粉气化炉[P].专利号01240407.1(No.01240407.1)..
  • 3徐越.干煤粉加压气化技术报告之六[R].西安:热工研究院,TPRI/T8-RA-006-2002,2002.6.
  • 4壳牌国际石油产品公司 电力工业部华北电力设计院 电力工业部热工研究院.中国IGCC电站项目初步可行性研究报告[R].北京:华北电力设计院,1997.12.
  • 5高正阳,阎维平,刘忠.煤颗粒在快速升温过程中非傅立叶导热效应的计算研究[J].中国电机工程学报,2002,22(9):141-145. 被引量:11
  • 6Merrick D. Mathematical models of the thermal decomposition of coal[J]. FUEL, 1983, 62(5): 534-539.
  • 7Norman J. Modelling the formation and emission of environmentally unfriendly coal species in some gasification processes[J]. FUEL, 1997,76: 1201-1216.
  • 8Vamvuka D, Woodbum E T. Senior, Modeling of an entrained flow coal gasifier, 1.Development of the model and general predicition[J]. FUEL,1995, 74: 1452-1465.
  • 9朱彤,马喜辰,董鹏,秦裕琨.切向燃烧炉膛中网格划分方法对数值模拟的影响[J].哈尔滨工业大学学报,1997,29(5):59-61. 被引量:24

二级参考文献18

  • 1项友谦.煤气化过程热力学平衡过程的理论计算[J].煤气与热力,1986,(1):4-9.
  • 2[1]Alonso M J G., Borrego A G., Alvarez D, et al.Pyrolysis behaviour of pulverized coals at different temperature[J].Fuel, 1999,78(13):1501-1513.
  • 3[2]Donskio E, Mcelwain D L S .Approximate modeling of coal pyrolysis[J]. Fuel, 1999,78(7):825-835.
  • 4[3]Monazam, E R, Maloney D J , Lawson L O. Measurment of heat capacity, temperatures, and absorptivities of single particles in an electrodynamic balance[J]. Rev. Sci. Instrum,1989,60(11):3460-3465.
  • 5[4]Richardson, M J. The specific heats of coals, cokes and their ashes[J].Fuel, 1993, 72(7):1047-1054.
  • 6[5]Merrick D, Mathematical models of the thermal decomposition of coal[J]. Fuel, 1983, 62(4):540-546.
  • 7[6]Maloney D J, Monazam E R, Woodruff S W,et al. Measurements and analysis of temperatures histories and size changes for single carbon and coal particles during the early stages of heating and devolatilization[J].Combust and Flame, 1991, 84(5/6):210-220.
  • 8[7]Fletcher T H. Time-resolved temperature measurements of individual coal particles during devolatilization[J]. Combust. Sci. and Tech., 1989, 63(1):89-105.
  • 9[8]Manoley D J, Ramanayhan Sampath, Zondlo W J. Heat capacity and thermal conductivity considerations for coal particles during the early stages of rapid heating [J]. Combust and Flame, 1999, 116(1/2):94-104.
  • 10[9]Fournier D, Boccara A C. Heterogeneous media and rough surface:a fractal approach for heat diffusion studies[J]. Physica A, 1989 157(3):587-592.

共引文献71

同被引文献703

引证文献83

二级引证文献642

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