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渣油催化裂化生焦反应集总动力学模型的研究 被引量:3

INVESTIGATION OF THE LUMPED KINETIC MODEL OF COKING REACTION FOR RESIDUE OIL CATALYTIC CRACKING
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摘要 在柴油馏分和重馏分油催化裂化生焦反应集总动力学模型研究的基础上,通过生焦反应试验和动力学参数估计,建立渣油催化裂化生焦反应十集总动力学模型。结果表明,反应系统气相和液相均符合催化生焦机理的动力学模型,具有较好的拟合试验数据能力和良好的外推性,并符合催化裂化生焦反应规律。 The purpose of this paper is to develop the coking kinetic model of residue oil catalytic cracking.Firstly,based on investigation of the coking lumped kinetic model of diesel oil and vacuum gas oil reaction systems,two kinds of coking physical models of residue catalytic cracking reaction system,thermal coking mechanism and catalytic coking mechanism,were determined.Furthermore,over a wide range of reaction conditions,five kinds of feedstocks were cracked on the commercial equilibrium zeolite catalyst in a fix fluidized bed reactor.Based on experiment data, model parameters and activity energy were determined by use of a parameter estimation method.This work pointed out that the coking lumped kinetic model for the catalytic coking mechanism of gas phase and liquid phase cauld simulate experiment data well.It also predicted well the coke yields of the feedstock whose composition is quite different from the compositions of feedstocks used to develop the coking kinetic model and fitted well with the feature of coking reaction for RFCC reaction system.
作者 任杰
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 1997年第3期58-64,共7页 Acta Petrolei Sinica(Petroleum Processing Section)
关键词 催化裂化 生焦 动力学模型 渣油 catalytic cracking,coking,lump,kinetic model,residue oil
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同被引文献11

  • 1杨小明,罗京娥.蒸汽失活裂化催化剂沸石活性组元的再活化研究[J].燃料化学学报,2001,29(z1):225-229. 被引量:1
  • 2邓铭波,任杰.催化裂化装置中催化剂平衡活性的数学模拟[J].石油学报(石油加工),2005,21(5):12-18. 被引量:3
  • 3Chester A W,Stover W A. Steam deactivation kinetics of zeolitic cracking catalysts[J]. Ind Eng Chem Prod Res Dev,1977, 16(4): 285-290.
  • 4Chen N Y, Burgess W P, Daniels R H. An automated microcatalytic system for gas oil cracking[J]. Ind Eng Chem Prod Res Dev, 1977, 16(3): 242-243.
  • 5Chen N Y, Mitchell T O, Olson D H, et al. Irreversible deactivation of zeolite fluid cracking catalyst 1 X-Ray and catalytic studies of catalyst aged in an automated microcatalytic system for gas oil cracking[J]. Ind Eng Chem Prod Res Dev, 1977, 16(3): 244-247.
  • 6Chen N Y, Mitchell T O, Olson D H, et al. Irreversible deactivation of zeolite fluid cracking catalyst 2 Hydrothermal stability of catalysts containing NH4Y and rare earth Y[J]. Ind Eng Chem Prod Res Dev, 1977, 16(3) : 247-252.
  • 7Chester A W,Stover W A.Steam deactivation kinetics of zeolitic cracking catalysts[J].Ind Eng Chem Prod Res Dev,1977,16(4):285-290.
  • 8Chen N Y,Burgess W P,Daniels R H.An automated microcatalytic system for gas oil cracking[J].Ind Eng Chem Prod Res Dev,1977,16(3):242-243.
  • 9Chen N Y,Mitchell T O,Olson D H,et al.Irreversible deactivation of zeolite fluid cracking catalyst 1 X-Ray and catalytic studies of catalyst aged in an automated microcatalytic system for gas oil cracking[J].Ind Eng Chem Prod Res Dev,1977,16(3):244-247.
  • 10Chen N Y,Mitchell T O,Olson D H,et al.Irreversible deactivation of zeolite fluid cracking catalyst 2 Hydrothermal stability of catalysts containing NH4 Y and rare earth Y[J].Ind Eng Chem Prod Res Dev,1977,16(3):247-252.

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