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循环流化床烟气脱硫数学模型参数的确定 被引量:6

Determination of Parameters of a Flue Gas Desulfurization's Mathematical Model for Circulating Fluidized Beds
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摘要 给出了循环流化床烟气脱硫数学模型中的各个参数或相应的计算公式。采用微机编程软件VB对脱硫效率进行了计算,介绍了计算程序。经验证:模型计算结果与实际数据较为吻合,表明这种模拟计算方法是有效的。 Values of parameters, or relevant formulae, for determining lhe parameters of the mathematical desulfurization model for circulating fluidized bed boilers, are here presented. Desulfurization efficiency is being calculated by using programming software VB for personal computers. The calculation procedure is explained. Verification shows that calculation results meet actual operational data relatively well. This simulation calculation method is therefore acceptable. Figs 2,table 1 and refs 12.
作者 马双忱 赵毅
出处 《动力工程》 CSCD 北大核心 2006年第5期716-719,737,共5页 Power Engineering
关键词 环境工程学 循环流化床 烟气脱硫 数学模型 参数 确定 environmental engineering circulating fluidized bed flue gas desulfurization mathematical model parameter determination
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参考文献11

  • 1马双忱,赵毅,华伟.烟气循环流化床脱硫数学模型及应用[J].中国电机工程学报,2004,24(10):228-232. 被引量:12
  • 2何大阔,王福利,李振中.循环流化床烟气脱硫效率的研究[J].动力工程,2005,25(4):582-586. 被引量:16
  • 3James K Neathery.Model for Flue Gas Desulfurization in A Circulating Dry Scrubber[J].AIChE.Journal,1996,42(1):259 ~ 268.
  • 4David M J.Puchyr,Anil K.Mehrotra,Leo A.Behie.Modeling A Circulating Fluidized Bed Riser Reactor with Gas-Solids Downflow at the Wall[J].The Canadian Journal Of Chemical Engineering,1997,75:317 ~ 326.
  • 5Werther,J.Fluid Mechanics of Large-Scale Units[C].in Circulating Fluidized Bed Technology Ⅳ,New York,1994,1 ~14.
  • 6王建龙译.环境工程导论[M].北京:清华大学出版社,2002.778~783.
  • 7潘永康,王喜忠等编.现代干燥技术[M].北京:化学工业出版社,1982.1~16.
  • 8Newton G H,Kramlich J,Payne R.Modeling the SO2-Slurry Droplet Reaction[J].ACIhE J,1990 (36):1865 ~1872.
  • 9Rabe A E,Harris J E.Vapor Liquid Equilibrium Data for the Binary System.Sulfur dioxide and Water[J].J.of Chem.Eng.Data,1963(8):133 ~ 136.
  • 10Perry R H.PERRY化学工程手册.第3篇,物理和化学数据[M],北京:化学工业出版社,1993.131~132.

二级参考文献22

  • 1魏飞,杨国强,金涌,俞芷青.高密度循环流化床中气固两相流动结构的一维成像分析[J].化工学报,1994,45(5):523-530. 被引量:5
  • 2Contractor R M, Patience G S, Garnertt D Let al. A new process for N-butane oxidation to maletic anhydride using a circulating fluidized bed reactor[A]. Circulating Fluidized Bed Technology Ⅳ, New York[C].1994: 387-389.
  • 3Patience G S, Chaouki J. Gas phase hydrodynamics in the riser of a circulating fluidized bed[J]. Chem..Eng. Sci. 1993, 48: 3195-3205.
  • 4Patience G S, Chaouki J. Solids hydrodynamics in the fully developed region of CFB risers[A]. Fluidization Ⅷ Preprints,France [C]. 1995,3-40.
  • 5Yan Yan, Peng Xiaofeng. Analysis of flue gas desulfurization in a circulating fluidized bed[J]. Int. Comm. of Heat and Mass Transfer.2003,30(1): 71-82.
  • 6Rhodes M J. Modeling the flow structure of upward flowing gas-solid suspensions[J]. Powder Technology, 1990,60: 27-38.
  • 7Harris B J, Davidson J F. A core/annulus deposition model for circulating fluidized beds[A]. Circulating Fluidized Bed Technology Ⅳ[C]. Hidden Vaey, A A Avidan eds, 1994, AIChE,New York, 103.
  • 8David M, Puchyr J, Antl K, et al. Modeling a circulating fluidized bed riser reactor with gas-solids downflow at the wall[J]. The Canadian Journal of Chemical Engineering,1997,75: 317-326.
  • 9James K Neathery. Model for flue gas desulfurization in a circulating dry scrubber[J]. AIChE Journal. 1996,42(1): 259-268.
  • 10Shuangchen Ma, Yi Zhao, Jianjun Huang et al. Experimental study on flue gas desulfurization by circulating fuidized bed[A]. Proceedings of the 4th Asia-Pacific Conference on Combustion[C]. Nanjing, China, 2003,220-224.

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