Kinetic azeotropy and design of reactive distillation columns

被引:5
|
作者
Mahajani, SM [1 ]
机构
[1] Monash Univ, Dept Chem Engn, Clayton, Vic 3168, Australia
关键词
D O I
10.1021/ie9802663
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The reactive fixed points in the distillation maps of a reactive distillation column (RDC) with kinetically controlled reactions are identified and their role in deciding the design feasibility has been elucidated. The fixed points at which both reaction and distillation vectors have zero magnitudes correspond to the equilibrium fixed point. It is known that the relative positions of these points for the rectifying and stripping sections determine the value of the minimum reflux ratio. However, apart from these fixed points, there are certain fixed points in the distillation map at which, though the reaction and distillation vectors have nonzero magnitudes, they nullify the effects of each other. These points correspond to the kinetic fixed points and have a special significance. Their positions have direct influence on the feasible product composition. A simple example of an ideal ternary system undergoing a reaction 2B double left right arrow A + C has been illustrated to show the importance of kinetic azeotropy in the design aspects of RDC.
引用
收藏
页码:177 / 186
页数:10
相关论文
共 50 条
  • [21] Design of heterogeneous distillation columns for separation of azeotropic non-reactive and reactive mixtures
    Wasylkiewicz, SK
    COMPUTERS & CHEMICAL ENGINEERING, 1999, 23 : S125 - S128
  • [22] NEW TOOLS FOR THE DESIGN OF KINETICALLY CONTROLLED REACTIVE DISTILLATION-COLUMNS
    DOHERTY, MF
    BUZAD, G
    COMPUTERS & CHEMICAL ENGINEERING, 1994, 18 : S1 - S13
  • [23] CHARACTERISTIC DESIGN FEATURES OF REACTIVE DISTILLATION COLUMNS FOR ETHYLENE GLYCOL PRODUCTION
    Samoilov, N. A.
    Mnushkin, I. A.
    Mnushkina, O. A.
    CHEMICAL AND PETROLEUM ENGINEERING, 2006, 42 (5-6) : 248 - 254
  • [24] Conceptual design of reactive distillation columns using stage composition lines
    Groemping, M
    Dragomir, RM
    Jobson, M
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (03) : 369 - 382
  • [25] Conceptual design of single-feed hybrid reactive distillation columns
    Dragomir, RM
    Jobson, M
    CHEMICAL ENGINEERING SCIENCE, 2005, 60 (16) : 4377 - 4395
  • [26] Analysis of finishing reactive distillation columns
    Espinosa, J
    Aguirre, P
    Frey, T
    Stichlmair, J
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (01) : 187 - 196
  • [27] Analysis of finishing reactive distillation columns
    Espinosa, José
    Aguirre, Pio
    Frey, Thomas
    Stichlmair, Johann
    Industrial and Engineering Chemistry Research, 1999, 38 (01): : 187 - 196
  • [28] Controllability of reactive batch distillation columns
    Biller, NCT
    Sorensen, E
    EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING - 12, 2002, 10 : 445 - 450
  • [29] Optimization-based design of reactive distillation columns using a memetic algorithm
    Urselmann, M.
    Barkmann, S.
    Sand, G.
    Engell, S.
    COMPUTERS & CHEMICAL ENGINEERING, 2011, 35 (05) : 787 - 805
  • [30] Conceptual design of single-feed kinetically controlled reactive distillation columns
    Dragomir, RM
    Jobson, M
    CHEMICAL ENGINEERING SCIENCE, 2005, 60 (18) : 5049 - 5068