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Book Vapour   Liquid Equilibrium

Download or read book Vapour Liquid Equilibrium written by Eduard Hála and published by Elsevier. This book was released on 2013-10-22 with total page 624 pages. Available in PDF, EPUB and Kindle. Book excerpt: Vapor-Liquid Equilibrium, Second Edition covers the theoretical principles and methods of calculation of equilibrium conditions from various experimental data and the elements of measuring technique, as well as the instruments for the direct determination of the equilibrium compositions of the liquid and vapor phases of the system. The book discusses the relations necessary for the thermodynamic treatment of the equilibrium between the liquid and vapor phase of a system; the concept of an ideal solution and auxiliary thermodynamic functions; and the activity and the activity coefficient. The text also describes vapor-liquid equilibrium in real systems (electrolytes and non-electrolytes) and in systems whose components (i.e. temperature, pressure, and composition of phases) mutually react according to several stoichiometric equations. The criteria of purity of substances and the methods of measuring temperature; low, medium, and high pressures; the pressures of the saturated vapors at given temperatures; and the boiling points at given pressures used in laboratory work in the field of vapor-liquid equilibrium are considered. The book also tackles the methods for the direct determination of equilibrium data (distillation, circulation, static, dew and bubble point, and flow methods). The text concludes with a review of the literature on the systems whose vapor-liquid equilibrium data had been measured and reported to the beginning of 1954. Workers in the chemical industry who deal with problems of distillation and rectification will find the book useful.

Book Vapor liquid Equilibrium

Download or read book Vapor liquid Equilibrium written by James C. K. Ho and published by . This book was released on 1962 with total page 0 pages. Available in PDF, EPUB and Kindle. Book excerpt: This thesis comprises of two parts. The first part is the determination of vapor-liquid equilibrium data at atmospheric pressure and 55°C for the ternary system n-hexane-ethyl alcohol-benzene and for the three possible binary systems n-hexane-ethyl alcohol, n-hexane-benzene and ethyl alcohol-benzene which constituted the ternary system. A modified Gillespie equilibrium still is employed to conduct the investigation. The equilibrium data for the three binary systems and the ternary system appear to be consistent as shown from the thermodynamic consistency tests. The experimental results indicate that two binary systems, namely, n-hexane-ethyl alcohol and ethyl alcohol-benzene form azeotrope at 760 nm. Hg. and 55°C. The ternary system deviates considerably from ideal liquid phase behavior. However, no ternary azeotrope is found from the experiment. The second part presents a method for predicting binary vapor-liquid equilibrium data at various conditions if the equilibrium data for the system concerned are available over the complete concentration range at any one isothermal or isobaric condition. The proposed method is limited to nonazeotropic solutions.

Book Vapor liquid Equilibrium Data

Download or read book Vapor liquid Equilibrium Data written by Shuzo Ohe and published by . This book was released on 1989 with total page 742 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Book Measurement  Evaluation  and Prediction of Phase Equilibria

Download or read book Measurement Evaluation and Prediction of Phase Equilibria written by Henry V. Kehiaian and published by Elsevier Publishing Company. This book was released on 1986 with total page 524 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Book The Experimental Determination of Solubilities

Download or read book The Experimental Determination of Solubilities written by G. T. Hefter and published by John Wiley & Sons. This book was released on 2003-11-14 with total page 658 pages. Available in PDF, EPUB and Kindle. Book excerpt: * Guidelines are provided on the reliability of various methods, as well as information for selecting the appropriate technique. * Unique coverage of the whole range of solubility measurements. * Very useful for investigators interested in embarking upon solubility measurements.

Book A Study of Predicting Vapor liquid equilibrium of a Binary from Two Conjugated Binaries of a Ternary by Using the Wilson Equation

Download or read book A Study of Predicting Vapor liquid equilibrium of a Binary from Two Conjugated Binaries of a Ternary by Using the Wilson Equation written by William J. Lambert and published by . This book was released on 1981 with total page 238 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Book Prediction of Vapor liquid Equilibria for Ternary Systems Under Atmospheric Pressure

Download or read book Prediction of Vapor liquid Equilibria for Ternary Systems Under Atmospheric Pressure written by Gregory Frank Vinci and published by . This book was released on 1950 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt:

Book Vapor Liquid Equilibria Using Unifac

Download or read book Vapor Liquid Equilibria Using Unifac written by Aage Fredenslund and published by Elsevier. This book was released on 2012-12-02 with total page 393 pages. Available in PDF, EPUB and Kindle. Book excerpt: 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.

Book Vapor liquid Equilibrium at Low Pressures

Download or read book Vapor liquid Equilibrium at Low Pressures written by Norman I. Silverman and published by . This book was released on 1977 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt:

Book Phase Equilibria

    Book Details:
  • Author : Andreas L. Muhlbauer
  • Publisher : Taylor & Francis
  • Release : 2023-02-03
  • ISBN : 1351425064
  • Pages : 486 pages

Download or read book Phase Equilibria written by Andreas L. Muhlbauer and published by Taylor & Francis. This book was released on 2023-02-03 with total page 486 pages. Available in PDF, EPUB and Kindle. Book excerpt: This work provides coverage of experimental and theoretical procedures for vapour-liquid equilibria (VLE). A survey of the different models and approaches in recent literature enables the reader to choose the appropriate action.

Book Phase Equilibrium Methods for Binary and Ternary Mixtures  applications to the Nitrogen oxygen argon System

Download or read book Phase Equilibrium Methods for Binary and Ternary Mixtures applications to the Nitrogen oxygen argon System written by William Paul Clarke and published by . This book was released on 1988 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt: Three models are used to predict vapor-liquid-equilibrium (VLE) properties of binary and ternary mixtures of nitrogen, argon, and oxygen. These models predict mixture properties using accurate wide-range equations of state for the pure-fluid components of the mixture. One model uses extended corresponding states principles to predict mixture properties. The other tow models combine coefficients of terms from the equations of state for the components in the mixture to obtain coefficients for a single equation which calculates mixture propertied directly. Iteration methods to solve the VLE constraint equations for different input combinations are presented. Equilibrium pressures and vapor phase compositions predicted by the three models are compared to experimental values from P-T-x-y data measured over a wide range of equilibrium states. The computer programs for the calculations reported in this work are listed in the appendices.