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Phase equilibrium in mixtures /
Phase Equilibrium in Mixtures.
| Clasificación: | Libro Electrónico |
|---|---|
| Autor principal: | |
| Formato: | Electrónico eBook |
| Idioma: | Inglés |
| Publicado: |
Oxford ; New York :
Pergamon Press,
[1969]
|
| Edición: | [1st ed.]. |
| Colección: | International series of monographs on chemical engineering ;
v. 9. |
| Temas: | |
| Acceso en línea: | Texto completo |
MARC
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| 100 | 1 | |a King, M. B. | |
| 245 | 1 | 0 | |a Phase equilibrium in mixtures / |c M.B. King. |
| 250 | |a [1st ed.]. | ||
| 260 | |a Oxford ; |a New York : |b Pergamon Press, |c [1969] | ||
| 300 | |a 1 online resource (xviii, 585 pages) : |b illustrations | ||
| 336 | |a text |b txt |2 rdacontent | ||
| 337 | |a computer |b c |2 rdamedia | ||
| 338 | |a online resource |b cr |2 rdacarrier | ||
| 490 | 1 | |a International series of monographs in chemical engineering ; |v v. 9 | |
| 504 | |a Includes bibliographical references. | ||
| 506 | |3 Use copy |f Restrictions unspecified |2 star |5 MiAaHDL | ||
| 533 | |a Electronic reproduction. |b [Place of publication not identified] : |c HathiTrust Digital Library, |d 2010. |5 MiAaHDL | ||
| 538 | |a Master and use copy. Digital master created according to Benchmark for Faithful Digital Reproductions of Monographs and Serials, Version 1. Digital Library Federation, December 2002. |u http://purl.oclc.org/DLF/benchrepro0212 |5 MiAaHDL | ||
| 583 | 1 | |a digitized |c 2010 |h HathiTrust Digital Library |l committed to preserve |2 pda |5 MiAaHDL | |
| 588 | 0 | |a Print version record. | |
| 505 | 0 | |a 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. | |
| 505 | 8 | |a 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. | |
| 505 | 8 | |a 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. | |
| 505 | 8 | |a 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. | |
| 505 | 8 | |a 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. | |
| 520 | |a Phase Equilibrium in Mixtures. | ||
| 546 | |a English. | ||
| 650 | 0 | |a Phase rule and equilibrium. | |
| 650 | 0 | |a Mixtures. | |
| 650 | 6 | |a Loi des phases et �equilibre. |0 (CaQQLa)201-0020005 | |
| 650 | 6 | |a M�elanges (Chimie) |0 (CaQQLa)201-0017115 | |
| 650 | 7 | |a SCIENCE |x Chemistry |x Industrial & Technical. |2 bisacsh | |
| 650 | 7 | |a TECHNOLOGY & ENGINEERING |x Chemical & Biochemical. |2 bisacsh | |
| 650 | 7 | |a Mixtures |2 fast |0 (OCoLC)fst01024157 | |
| 650 | 7 | |a Phase rule and equilibrium |2 fast |0 (OCoLC)fst01060399 | |
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| 650 | 7 | |a Phasengleichgewicht |2 gnd |0 (DE-588)4132145-5 | |
| 650 | 7 | |a Thermodynamik |2 gnd |0 (DE-588)4059827-5 | |
| 650 | 7 | |a Zustandsgleichung |2 gnd |0 (DE-588)4068158-0 | |
| 650 | 1 | 7 | |a Fase-evenwichten. |2 gtt |
| 650 | 1 | 7 | |a Mengsels. |2 gtt |
| 650 | 1 | 7 | |a Thermodynamica. |2 gtt |
| 776 | 0 | 8 | |i Print version: |a King, M.B. |t Phase equilibrium in mixtures. |b [1st ed.]. |d Oxford, New York, Pergamon Press [1969] |w (DLC) 67027484 |w (OCoLC)260 |
| 830 | 0 | |a International series of monographs on chemical engineering ; |v v. 9. | |
| 856 | 4 | 0 | |u https://sciencedirect.uam.elogim.com/science/book/9780080123011 |z Texto completo |