Phase equilibrium in mixtures /
Phase Equilibrium in Mixtures.
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Main Authors: | |
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Corporate Authors: | |
Published: |
Pergamon Press,
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Publisher Address: | Oxford ; New York : |
Publication Dates: | [1969] |
Literature type: | eBook |
Language: | English |
Edition: | [1st ed.]. |
Series: |
International series of monographs in chemical engineering ;
v. 9 |
Subjects: | |
Online Access: |
http://www.sciencedirect.com/science/book/9780080123011 |
Summary: |
Phase Equilibrium in Mixtures. |
Carrier Form: | 1 online resource (xviii, 585 pages) : illustrations. |
Bibliography: | Includes bibliographical references. |
ISBN: |
9781483152417 1483152413 |
Index Number: | QD501 |
CLC: | O642.1 |
Contents: |
Front Cover; Phase Equilibrium in Mixtures; Copyright Page; Table of Contents; Preface; Nomenclature and units used; List of symbols; CHAPTER 1. INTRODUCTION AND SOME THERMODYNAMIC CONSIDERATIONS; SCOPE OF THE BOOK; THE ROLE OF THERMODYNAMICS AND THE CRITERIA FOR EQUILIBRIUM BETWEEN PHASES; THE CHEMICAL POTENTIAL; PROPERTIES OF PARTIAL MOLAR QUANTITIES; DEPENDENCE OF THE THERMODYNAMIC FUNCTIONS OF PURE SUBSTANCES ON PRESSURE. REFERENCE VALUES FOR THESE FUNCTIONS. THE FUGACITY OF A PURE SUBSTANCE; DEPENDENCE OF THE THERMODYNAMIC FUNCTIONS OF MIXTURES ON PRESSURE AND COMPOSITION; THE FUGACITY. Ideal solutionsnon-ideal solutions; the phase rule for non-reacting components; chemically reacting systems; chapter 2. descriptive account of phase equilibria; introduction, phase behaviour of pure substances; vapour-liquid equilibria for systems which are completely miscible in the liquid phase; phase equilibrium diagrams for mixtures of substances which are not completely miscible in the liquid phase; gas hydrates; chapter 3. latent heats and vapour pressures; latent heats; vapour pressure equations for pure substances. Temperature dependence of the dew- and bubble-point pressures of mixturesaccurate representation of vapour pressure and other phase boundary data using residual plots; extension of vapour pressure data using reference substance plots; chapter 4. dilute solutions; henry's law; liquid-liquid equilibrium; the solubility of non-polar substancesin water and in aqueous solutions of electrolytes; chapter 5. ideal and near-ideal solutions; chapter 6. non-ideal solutions at normalpressures: uses of the activity coefficient; introduction. Analytical representation of activity coefficients as functions of composition at constant temperature.correlation of isothermal vapour-liquid equilibrium datathe activity coefficient as a function of temperature; correlation of activity coefficients derived from isobaric vapour-liquid equilibrium data; partial pressures and activity coefficients in systems where a specific reaction occurs; prediction of activity coefficients for binary systems from the properties of the pure components. Prediction of liquid-liquid equilibria in a ternary system when two of the components are virtually immiscibleprediction of vapour-liquid equilibrium data for a binary system with immiscible liquid phases, from mutual solubility data for the two liquids; prediction of activity coefficients for ternary systems from phase equilibrium data for the corresponding binary systems; prediction of activity coefficients for quaternary and multicomponent systems from data for the appropriate binary systems; azeotropes; chapter 7. consistency tests. |