Reactive absorption:: Optimal process design via optimal modelling

被引:61
作者
Kenig, EY [1 ]
Schneider, R
Górak, A
机构
[1] Univ Dortmund, Dept Chem Engn, D-44221 Dortmund, Germany
[2] Essen Univ, Dept Mech Engn, D-45141 Essen, Germany
关键词
D O I
10.1016/S0009-2509(00)00234-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Optimal design of complex reactive separations is inconceivable unless reliable process models are available. Such models have to be both rigorous enough in order to reflect the process complexity and simple enough in order to ensure feasibility of process simulations. In this respect, an optimal model should represent a kind of a consensus between the rigour and simplicity, and its development requires a comparison of both detailed and simplified process models with experimental data. From this viewpoint, reactive absorption operations with their pronounced kinetic character and complex non-ideal behaviour provide one of the best objects for studying. This work gives a detailed analysis of the problem supplemented by the examples of industrial importance. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:343 / 350
页数:8
相关论文
共 25 条
[1]  
Astarita G., 1991, KINETIC THERMODYNAMI
[2]   MULTICOMPONENT FILM-PENETRATION THEORY WITH LINEARIZED KINETICS .1. LINEARIZATION THEORY AND FLUX EXPRESSIONS [J].
DELANCEY, GB .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (12) :2315-2323
[3]  
Doraiswamy LK., 1984, EXAMPLES REACTOR DES, V2
[4]   VAPOR-LIQUID-EQUILIBRIA IN MULTICOMPONENT AQUEOUS-SOLUTIONS OF VOLATILE WEAK ELECTROLYTES [J].
EDWARDS, TJ ;
MAURER, G ;
NEWMAN, J ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1978, 24 (06) :966-976
[5]  
GORAK A, 1994, PROZESSSIMULATION
[6]  
Hikita H., 1964, INT CHEM ENG, V4, P332
[7]   A FILM MODEL-BASED APPROACH FOR SIMULATION OF MULTICOMPONENT REACTIVE SEPARATION [J].
KENIG, E ;
GORAK, A .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1995, 34 (02) :97-103
[8]  
Kenig E. Y., 1994, THEOR FOUND CHEM ENG, V28, P305
[9]   Comparison of numerical and analytical solutions of a multicomponent reaction-mass-transfer problem in terms of the film model [J].
Kenig, EY ;
Butzmann, F ;
Kucka, L ;
Górak, A .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (08) :1483-1496
[10]  
KENIG EY, 1994, THEOR FOUND CHEM ENG, V28, P199