Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach

宋一鸣; 宋金荣; 龚明; 曹彬; 杨燕红; 马晓迅

doi:10.1016/S1004-9541(10)60232-7

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Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach

Updated：2026-01-06

- Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach
- Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach
- 中国化学工程学报（英文版） 2010年18卷第3期页码：362-371
- Affiliations：
  
  1. School of Chemical Engineering, Northwest University,Xi'an,China,710069
  2. Chemical Engineering Research Center of the Ministry of Education for Advanced Use Technology of Shanbei Energy,Xi'an,China,710069
- Author bio：
- Funds：
  
  Supported by the National Natural Science Foundation of China(20776118);Science&Technology Bureau of Xi'an[CXY09019(1)];Innovation Foundation for Graduated Student of Northwest University(08YJC21);Shaanxi Research Centerof Engineering Technology for Clean Coal Conversion(2008ZDGC-13)
- DOI：10.1016/S1004-9541(10)60232-7
  中图分类号：
- 纸质出版：2010
- Accepted：
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宋一鸣, 宋金荣, 龚明, 等. Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach[J]. 中国化学工程学报（英文版）, 2010,18(3):362-371.

SONG Yiming, SONG Jinrong, GONG Ming, CAO Bin, YANG Yanhong, MA Xiaoxun. Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach[J]. , 2010, 18(3): 362-371.
宋一鸣, 宋金荣, 龚明, 等. Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach[J]. 中国化学工程学报（英文版）, 2010,18(3):362-371. DOI： 10.1016/S1004-9541(10)60232-7.

SONG Yiming, SONG Jinrong, GONG Ming, CAO Bin, YANG Yanhong, MA Xiaoxun. Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach[J]. , 2010, 18(3): 362-371. DOI： 10.1016/S1004-9541(10)60232-7.

摘要

Abstract

The Intalox metal tower packing was used to simulate an industrial relevant extractive distillation column for purifying azeotropic multicomponent mixture.In order to explain the inconsistencies in the modeling of transfer process in nonideal multicomponent distillation column

a method was developed with equilibrium stage models(EQ)and non-equilibrium model(NEQ)incorporated with Maxwell-Stefan diffusion equations in the framework of AspenONE simulator.Dortmund Modified UNIFAC(UNIFAC-DMD)thermodynamic model was employed to estimate activity coefficients.In addition

to understand the reason for the diffusion against driving force and the different results by EQ and NEQ models

explicit investigations were made on diffusion coefficients

component Murphree efficiency and mass transfer coefficients.The results provide valuable information for basic design and applications associated with extractive distillation.

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