Author : American Petroleum Institute. Division of Refining
Publisher :
Page : 72 pages
File Size : 20,94 MB
Release : 1963
Category : Distillation
ISBN :
Author : Gerd Brunner
Publisher : Springer Science & Business Media
Page : 396 pages
File Size : 40,26 MB
Release : 2013-06-29
Category : Science
ISBN : 3662073803
Application of compressed gases as solvents has found widespread interest within the scientific community. Its processes have industrial applications. Gas Extraction deals with the possibilities of supercritical gases as solvents for separation processes. The volume combines physico-chemical aspects with chemical engineering methods. The text generalizes as far as possible, and treats examples in detail. Gas Extraction covers, for the first time, the subject in textbook form. Most of the examples provide new results that will be helpful for practicing scientists, engineers, and students who want to make use of the techniques.
Author : Jürgen Gmehling
Publisher :
Page : 570 pages
File Size : 16,97 MB
Release : 2004
Category : Chemistry, Organic
ISBN :
Author : J. A. Muckleroy
Publisher :
Page : 114 pages
File Size : 46,79 MB
Release : 1962
Category : Hydrocarbons
ISBN :
Author : Ivan Wichterle
Publisher : Elsevier Science & Technology
Page : 304 pages
File Size : 43,98 MB
Release : 1976
Category : Science
ISBN :
Author : Natural Gas Processors Suppliers Association
Publisher :
Page : 314 pages
File Size : 13,20 MB
Release : 1967
Category : Gasoline
ISBN :
Author : A.L. Horvath
Publisher : CRC Press
Page : 921 pages
File Size : 32,45 MB
Release : 2020-11-26
Category : Science
ISBN : 1000146073
This book promotes a basic understanding of the concept of solubility and miscibility between halogenated hydrocarbons and water. It points out the regularities existing between solubility and physical properties of solute and solvent. The book is valuable to chemists and chemical engineers.
Author : Thomas J. Bruno
Publisher : CRC Press
Page : 606 pages
File Size : 11,54 MB
Release : 2017-11-22
Category : Science
ISBN : 1351357514
In this volume, we have collected a series of reviews that cover both experimental and theoretical work geared toward the more exact requirements of current SFE applications. While we have artificially divided the volume into experimental and theoretical sections, natural overlaps will be apparent. Many of the papers on experimental and theoretical sections, natural overlaps will be apparent. Many of the papers on experimental technique contain discussions on equation of state correlations. Indeed, a good deal of the experimental work is intimately tied to a mathematical description of fluid mixtures. The theoretical section presents reviews that cover the modern theory of critical phenomena, methods to correlate near critical experimental results and approaches to understanding the behavior of near critical fluids from microscopic theory. It is hoped that the scope of these reviews will provide the reader with the basis to further develop our understanding of the behavior of supercritical fluids.
Author : Andrzej Mączyński
Publisher :
Page : 234 pages
File Size : 27,91 MB
Release : 1979
Category : Hydrocarbons
ISBN :
Author : Aage Fredenslund
Publisher : Elsevier
Page : 393 pages
File Size : 17,35 MB
Release : 2012-12-02
Category : Technology & Engineering
ISBN : 0444601503
Vapor-Liquid Equilibria Using UNIFAC: A Group-Contribution Method focuses on the UNIFAC group-contribution method used in predicting quantitative information on the phase equilibria during separation by estimating activity coefficients. Drawing on tested vapor-liquid equilibrium data on which UNIFAC is based, it demonstrates through examples how the method may be used in practical engineering design calculations. Divided into nine chapters, this volume begins with a discussion of vapor and liquid phase nonidealities and how they are calculated in terms of fugacity and activity coefficients, respectively. It then introduces the reader to the UNIFAC method and how it works, the procedure used in establishing the parameters needed for the model, prediction of binary and multicomponent vapor-liquid equilibria for a large number of systems, the potential of UNIFAC for predicting liquid-liquid equilibria, and how UNIFAC can be used to solve practical distillation design problems. This book will benefit process design engineers who want to reliably predict phase equilibria for designing distillation columns and other separation processes.
