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Reseña del editor Addresses the use of rigorous multicomponent mass transfer models for the simulation and design of process equipment. Deals with the basic equations of diffusion in multicomponent systems. Describes various models and estimations of rates of mass and energy transfer. Covers applications of multicomponent mass transfer models to process design. Includes appendices providing necessary mathematical background. Contains a large number of numerical examples worked out in detail. Contraportada Divided into three parts, Part I of Multicomponent Mass Transfer offers a detailed overview of the basic equations of diffusion in multicomponent systems. Chapters cover continuing relations for mass, momentum, and energy; mass transfer fluxes and reference velocity frames; Maxwell-Stefan relations; diffusion in electrolyte systems; Fick's law for binary mixtures and multicomponent systems; irreversible thermodynamics; procedures for estimating diffusion coefficients in multicomponent mixtures; and methods for solution of multicomponent diffusion programs. Part II describes known models of mass and energy transfer. Multicomponent mass transfer coefficients are defined and the multicomponent film model developed. The unsteady state of diffusion models is examined as are models based on turbulent eddy diffusion. Finally, the book tackles the additional complication of simultaneous mass and energy transfer. In Part III the authors cover the various applications of multicomponent mass transfer models to process design. Readers examine models of mass transfer on distillation trays and use the information to develop procedures for the estimation of point and tray efficiencies in multicomponent distillation and in the simulation and design of distillation of absorption columns. The final chapters in Part III considers the design of mixed vapor condensers. Biografía del autor Ross Taylor and R. Krishna are the authors of Multicomponent Mass Transfer, published by Wiley.


Modeling multicomponent organic chemical transport in a twodimensional finiteelement model was developed to predict coupled transient flow and multicomponent transport of organic chemicals which can partition between nonaqueous phase liquid water gas and solid phases in porous media under the assumption of local chemical equilibrium gasphase pressure gradients are assumed negligible and liquid flow equations are solved simultaneously using

Some features of isothermal multicomponent mass transfer isothermal multicomponent diffusion in the h2 arn2 and ch4 arn2 threecomponent gas mixtures has been experimentally studied at various pressures and certain concentrations of components in binary mixtures it has been shown that in systems where diffusion coefficients differ significantly from each other convective instability occurs with increasing pressure which significantly

88197028 catalogolibrosdeespecialidad 1 0 ingles37 diffusional mass transfer fotocopia ahp skelland 1 0 ingles38 operaciones de separación por etapas de equilibrio en ingqmcfotoc ejhenley 1 0 español39 problemas de ingenieria quimica tomo i ocon tojo 2 1 español40 problemas de ingenieria quimica tomo ii ocon tojo 2 1 español41 chemical engineering practica herbert cremer 1 0 ingles42 mass transfer operations treybal

A general analysis of multicomponent mass transfer with chemical engineering science 1969 vol 24 pp 553569 pergamon press printed in great britain a general analysis of mutticomponent mass transfer with simultaneous reversible chemical reactions in multiphase systems lawrence l tavlaridest and benjamin galor chemical and petroleum engineering department university of pittsburgh pittsburgh pennsylvania 15213 usa

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