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催化裂化提升管反应器建模研究 被引量:1

Studies on Model of Fccu Reactor
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摘要 根据提升管反应器的动态机理,考虑反应对压力的影响,结合物料平衡、能量平衡方程,建立了馏分油5集总催化裂化反应动力学模型。使用Nelder-Mead最优化法进行了参数的拟合,并用MATLAB对模型进行了仿真。通过对工业装置数据的计算比较表明,该模型能较好的预测催化裂化产品产率,可用于实际催化裂化过程。 Baseing on the equations of mass, energy, composition balance, the five lumping dynamic mechanism models of the Fluidized Catalytic Cracking Unit (FCCU) reactor were developed. Nelder- Mead minimization algorithm was adopted to model parameters and used MATLAB to describe model. The results of the simulation showed that this simple model was capable of sensible predictions of the dynamic responses of each lupmings.
出处 《化工时刊》 CAS 2007年第8期7-9,15,共4页 Chemical Industry Times
关键词 催化裂化 机理模型 反应器 catalyting cracking mechanism model reactor
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参考文献10

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二级参考文献17

  • 1邓先梁,沙颖逊,王龙延,王国良,孟繁东.渣油催化裂化反应动力学模型的研究[J].石油炼制与化工,1994,25(9):35-39. 被引量:27
  • 2翁惠新,马军,欧阳福生.重油催化裂化反应集总动力学模型(Ⅱ)——模型的工业验证[J].化工学报,1995,46(6):669-674. 被引量:10
  • 3沙颖逊.催化裂化集总动力学模型的研究I.物理模型的确立[J].石油学报:石油加工,1985,1(1):3-15.
  • 4Wei James, Prater Charles D. A new approach to first-order chemical reaction systems [J]. AIChE J, 1962, 9(1): 77-81.
  • 5Weekman V M. A model of catalytic cracking conversion in fixed, moving and fluid-bed reactors [J]. Ind Eng Chem Prod Res Dev. 1968, 7: 90-95.
  • 6Lee L S, Chen Y W, Huang T N, Pan W Y. Four lump kinetic model for FCC process [J]. Can J Chem Eng. 1989, 67: 615-619.
  • 7Corella J, Frances E. Analysis of the riser reactor of a fluid cracking unit. Fluid Catalytic Cracking II [J]. ACS Symp Ser, 1991, 452: 165-182.
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共引文献53

同被引文献4

  • 1WEEKMAN J V W. A model of catalytic cracking conversion in fixed, moving and fluid-bed reactors[J]. Ind Eng Chem Process Des Dev, 1968, 7(1): 90-95.
  • 2郑远扬 高少立 袁璞.催化裂化装置的动态模型Ⅰ提升管反应器的动态模型和动力学参数估计.石油炼制,1986,27(2):23-30.
  • 3郑远扬 高少立.催化裂化装置的动态模型Ⅲ两段再生器的动态模型和动力学参数估计.石油炼制,1986,27(5):45-49.
  • 4罗雄麟,袁璞,林世雄.催化裂化装置动态机理模型 Ⅰ.反应器部分[J].石油学报(石油加工),1998,14(1):34-34. 被引量:26

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