A FILM MODEL-BASED APPROACH FOR SIMULATION OF MULTICOMPONENT REACTIVE SEPARATION

被引:46
作者
KENIG, E [1 ]
GORAK, A [1 ]
机构
[1] RUSSIAN ACAD SCI, INST NEW CHEM PROBLEMS, CHERNOGOLOVKA 142432, RUSSIA
关键词
FILM MODEL; SIMULATION; MULTICOMPONENT REACTIVE SEPARATION; MAXWELL-STEFAN APPROACH;
D O I
10.1016/0255-2701(94)03004-9
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A general approach to the design of multicomponent mass transfer accompanied by chemical reactions is presented. Both homogeneous and heterogeneous reactions in liquid phase, as well as their combination, have been studied and incorporated into the film model. Because of the multicomponent nature of reactive separation, the mass transfer equations in the fluid phases are based on the Maxwell-Stefan approach. These equations are coupled by diffusional interactions in the gas (vapour) phase and by both diffusional and homogeneous chemical interactions in the liquid phase. Heterogeneous reaction mechanism has been accounted for by mass balance relationships. The solution obtained allows the determination of concentration profiles of the components along the contacting apparatus.
引用
收藏
页码:97 / 103
页数:7
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