期刊文献+

单颗粒脱硫反应模型分析 被引量:3

THE MODEL ANALYSIS OF SINGLE-PARTICLE DESULFURIZATION
下载PDF
导出
摘要 本文在单颗粒脱硫缩核模型的基础上分析了晶粒模型,并指出了原有晶粒模型中的不足之处,分析了晶粒初始孔隙率非均匀的原因,建立了一个初始孔隙率沿半径变化的改进晶粒模型。改进后的非均匀模型考虑到颗粒内部初始孔隙率的非均匀性,分析了非均匀初始孔隙率对脱硫效率和脱硫剂利用率的影响,并给出了初始非均匀孔隙率模型的完整的数学描述。 In this paper we analyze the grain model based on shrinking core model, and point out the defect of original grain model. Prom analyzing the reason of original uneven porosity of the grain, we build a modified grain model whose original porosity varies according to the radius of grain. The modified model considers the original uneven porosity of the grain, and analyzes the effect of original uneven porosity on the efficiency of desulfurization and utilization ratio of CaO, then proposes the complete mathematical description of the original uneven porosity model.
作者 陈兵 张学学
出处 《工程热物理学报》 EI CAS CSCD 北大核心 2003年第5期852-854,共3页 Journal of Engineering Thermophysics
基金 国家重点基础研究专项经费资助项目(No.G1999022208-2-7)
关键词 干法脱硫 晶粒模型 孔隙率 数学模型 dry method for desulfurization grain model porosity mathematical model
  • 相关文献

参考文献4

  • 1Yagi S, Kunii D. Fluidized-Solids Reactors with Continuous Solids Feed-I Residence Time of Particles in Fluidized Beds. Chem. Eng. Sci., 1961, 16:364.
  • 2Wen C Y. Noncatalatic heterogeneous solid fluid reaction models. Industrial and Eng. Chem., 1968, 60(9): 34-53.
  • 3Szekely J, Evans J W. A Structural model for gas-solid reactions with a moving boundary: II. The effect of grain size, porosity and temperature on the reaction of porous pellets. Chem. Eng. Sci., 1970, 25:1091-1107.
  • 4Hartman M, Coughlin R W. Heaction of sulfur dioxide with limestone and the grain model. AIChE J., 1976, 22:490-498.

同被引文献23

  • 1王世昌,徐旭常,姚强.水蒸汽对CaO颗粒脱硫反应催化作用的实验研究[J].中国电机工程学报,2004,24(9):252-256. 被引量:10
  • 2王文龙,崔琳,马春元,董勇,徐夕仁.干法半干法脱硫灰的特性与综合利用研究[J].电站系统工程,2005,21(5):27-29. 被引量:37
  • 3Mmldelbrot B B. Fractal: Form, Chance and Dimension [M]. San Francisco: Freeman, 1977.
  • 4王乾,段钰锋.半干法烟气脱硫技术[J].能源研究与利用,2007(4):1-4. 被引量:14
  • 5Yagi S, Kunii D. Fluidized-solids reactors with continuous solids feed-i residence time of particles in fiuidized beds[J]. Chem. Eng. Sci., 1961,16: 364.
  • 6Braun A, Bartsch M, Schnyder B et al. A model for the film growth in samples with two moving reaction frontiers - an application and extension of the unreacted-core model[J]. Chem. Eng. Sci., 2000, 55(22): 5273-5282.
  • 7Szekely J, Evans J W. A Structural model for gas-solid reactions with a moving boundary: II. The effect of grain size, porosity and temperature on the reaction of porous pellets[J]. Chem. Eng. Sci.,1970, 25: 1091-1107.
  • 8Simons G A, Garman A R. Small pore closure and the deactivation of the limestone sulfation reaction[J]. AIChE J., 1986, 32(9): 1491 - 1499.
  • 9Simons G A, Garman A R, Bomi AA. The kinetic rate of SO2 sorption by CaO[J]. AIChE J., 1987, 33(2): 211-217.
  • 10Li X T, Luo Z Y et al. Modeling Sulfur retention in circulating fluidized bed combustors[J]. Chem. Eng. Sci., 1995, 50(14):2235-2242.

引证文献3

二级引证文献24

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