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Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach 被引量:2

Modeling of Mass Transfer in Nonideal Multicomponent Mixture with Maxwell-Stefan Approach
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摘要 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. 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.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2010年第3期362-371,共10页 中国化学工程学报(英文版)
基金 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 Center of Engineering Technology for Clean Coal Conversion (2008ZDGC-13).
关键词 rate based model equilibrium model mass transfer coefficient Murphree efficiency extractive distillation simulation 多组分 非理想 混合建模 UNIFAC 萃取精馏塔 传质 扩散方程 非平衡模型
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