Synthesis of cylohexanol by three-phase reactive distillation: influence of kinetics on phase equilibria

被引:41
|
作者
Steyer, F
Qi, ZW
Sundmacher, K
机构
[1] Otto Von Guericke Univ, Inst Verfahrenstech, Proc Syst Engn, D-39106 Magdeburg, Germany
[2] Max Planck Inst Dynam Complex Tech Syst, D-39106 Magdeburg, Germany
关键词
reactive distillation; residue curve maps; multiphase reactors; phase equilibria; reactive separation;
D O I
10.1016/S0009-2509(02)00023-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A reactive distillation process is being suggested for the production of the commercially interesting intermediate cyclohexanol from cyclohexene and water, which avoids some of the drawbacks of the conventional liquid-phase cyclohexane oxidation process, especially with respect to operational safety. This reactive distillation process has its own intricate challenges due to the fact that reaction, distillative separation and liquid-phase splitting occur simultaneously. The interaction of these three phenomena is studied using residue curve maps for both, model simulations and experimental data. Based on the fixed point analysis of the residue curves, a novel process is proposed for the reactive separation of cyclohexene/cyclohexane mixtures which is difficult to be carried out by conventional distillation due to very close boiling temperatures. (C) 2002 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:1511 / 1520
页数:10
相关论文
共 50 条
  • [1] Kinetics and phase equilibria of competing aldolization and elimination in a three-phase reactor
    Serra-Holm, V
    Salmi, T
    Kangas, M
    Mäki-Arvela, P
    Lindfors, LP
    CATALYSIS TODAY, 2001, 66 (2-4) : 419 - 426
  • [2] Performance of a three-phase fluidized bed as a reactive distillation device
    Liang, WG
    Wang, ZW
    Jin, Y
    Ya, ZQ
    Yang, S
    CHEMICAL ENGINEERING & TECHNOLOGY, 1996, 19 (05) : 456 - 461
  • [3] Performance of a three-phase fluidized bed as a reactive distillation device
    Dept. of Chem./Biochem. Engineering, University of Western Ontario, London, Ont. N6A 5B9, Canada
    不详
    Chem Eng Technol, 5 (456-461):
  • [4] Three-phase fluidized distillation
    Ravagnani, TMK
    Pereira, JAFR
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2001, 79 (06): : 881 - 890
  • [5] Three-phase fluidized distillation
    DESQ/Faculdade de Engenharia Quimica, Universidade Estadual de Campinas, 13083-970 Campinas, São Paulo, Brazil
    Canadian Journal of Chemical Engineering, 2002, 79 (06): : 881 - 890
  • [6] A method for modeling two- and three-phase reactive distillation columns
    Khaledi, Rahman
    Bishnoi, P. R.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (17) : 6007 - 6020
  • [7] Robust dynamic simulation of three-phase reactive batch distillation columns
    Brüggemann, S
    Oldenburg, J
    Zhang, P
    Marquardt, W
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (14) : 3672 - 3684
  • [8] Nonequilibrium modeling of three-phase distillation
    Higler, A
    Chande, R
    Taylor, R
    Baur, R
    Krishna, R
    COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (10) : 2021 - 2036
  • [9] A three-phase nonequilibrium model for catalytic distillation
    Kotora, Marcel
    Svandova, Zuzana
    Markos, Jozef
    CHEMICAL PAPERS, 2009, 63 (02): : 197 - 204
  • [10] A three-phase nonequilibrium model for catalytic distillation
    Marcel Kotora
    Zuzana Švandová
    Jozef Markoš
    Chemical Papers, 2009, 63 : 197 - 204