Last edited by Gardanos
Thursday, July 23, 2020 | History

5 edition of Liquid-Liquid Equilibrium Data Collection, Part 1 found in the catalog.

Liquid-Liquid Equilibrium Data Collection, Part 1

Binary Systems (Chemistry data series)

by J. M. Sorensen

  • 50 Want to read
  • 12 Currently reading

Published by Scholium Intl .
Written in English

    Subjects:
  • Physical Chemistry +,
  • Technology,
  • Science/Mathematics,
  • Liquid-liquid equilibrium,
  • Engineering - Chemical & Biochemical,
  • Tables

  • The Physical Object
    FormatHardcover
    Number of Pages650
    ID Numbers
    Open LibraryOL9022661M
    ISBN 103921567173
    ISBN 109783921567173

    Vapor-Liquid Equilibrium Data Collection: Aqueous-Organic Systems (Chemistry Data Series Vol. I Part 1) it was amazing avg rating — 4 ratings — published /5(15). Example Specific volume from data Introduction to Phase Equilibrium Pure Species Phase Equilibrium Gibbs Free Energy as a Criterion for Chemical Equilibrium The Chemical Potential Vapor Liquid Phase Equilibrium Example Horsepower of a compressor

    It can be seen that NRTL can correlate the liquid-liquid behavior of the mixture. From Figure 6 that shows vapor - liquid prediction for the water - isopropyl acetate - acetic acid system, it can be seen that the same set of binary parameters used in the liquid - liquid equilibrium predict quite well vapor - liquid equilibrium. This volume is a compilation of vapor–liquid equilibrium data on subcritical binary single-phase or two-phase liquid–liquid systems. All the components are well-defined pure substances, which are organic or inorganic nonelectrolytes, including low-melting ionic liquids and water. The present database contains numerical data for systems.

    Experimental (liquid + liquid) equilibrium data for the ternary system of water (1) + propanol (2) + diethyl carbonate (3) for mole fractions x at the temperature T = K Table 3 Experimental (liquid + liquid) equilibrium data for the ternary system of water (1) + diethyl carbonate (2) + benzene (3) for mole fractions x at T = K. The equilibrium state corresponds to the saturated vapor pressure curve p = p s (T), which is limited by a triple point (T tr P tr) and a critical point (T c,p c) of the substance.(In the presence of surface tension forces at the phase interface, pressures values p (1) and p (g) in coexisting phases are not equal.) The Clausius-Clapeyron equation follows from Eq.


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Liquid-Liquid Equilibrium Data Collection, Part 1 by J. M. Sorensen Download PDF EPUB FB2

Vapor-liquid Equilibrium Data Collection Pt. 3c Aldehydes and Ketones, Supplement 2 by Jurgen Gmehling, Ulfert Onken and a great selection of related books, art. Liquid-Liquid Equilibrium Data Collection, Part 1: Binary Systems (Chemistry data series) Hardcover – June 1, by J.

Sorensen (Author) See all formats and editions Hide other formats and editions. Price New from Used from Author: J. Sorensen. Liquid-Liquid Equilibrium Data Collection: Ternary and Quaternary Systems by W. Arlt (Editor), E. Macedo (Editor), P. Rasmussen (Editor), J. Sorensen (Editor) and a great selection of related books, art and collectibles available now at Liquid-Liquid Equilibrium Data Collection: Volume VI: Vapor-Liquid Equilibria for Mixtures of Low Boiling Substances To order the books of your choice, please contact Recommend Share Share Liquid-Liquid Equilibrium Data Collection.

New publications. Chemistry Data Series. Volume XV. Part 3: Organic Solutes ranging from C 6 to C 40 in mixed solventsISBN LLE – Liquid-Liquid Equilibria. The LLE data bank contains a large amount of liquid-liquid equilibrium data and liquid solubility data for binary and higher systems.

It is of great importance for extraction (distribution of a component between two liquid phases in equilibrium) and in case of other unit operations involving immiscible systems.

Liquid‐liquid equilibrium data collection, Vol. V, Part 1–3 (Binary Systems, Ternary Systems, Ternary and Quarternary Systems). Von J. Sorensen und W. Arlt. VAPOR-LIQUID EQUILIBRIUM DATA COLLECTION: AQUEOUS-ORGANIC SYSTEMS Volume 1, Part 1 of Vapor-liquid Equilibrium Data Collection: Aqueous-organic Solutions.

Organic Hydroxy Compounds: Alcohols and Phenols, J. Gmehling Chemistry data series Volume 1, Part 1 of Vapor-liquid Equilibrium Data Collection, Jürgen Gmehling: Authors: J. Gmehling, U. Liquid-Liquid Equilibrium Data Collection, Part 1 作者: Sorensen, J. 出版社: Scholium Intl 定价: 元 装帧: HRD ISBN: 豆瓣评分.

Vapor-Liquid Equilibrium Data Collection Authors: J. Gmehling, U. Onken, W. Arlt, P. Grenzheuser, U. Weidlich, B. Kolbe, J. Rarey Volume I is a comprehensive collection of vapor-liquid equilibrium data with more than isothermal or isobaric data sets for binary and multicomponent mixtures at low to moderate pressures.

Mole Fraction Component (2) I Plait point Classical coordinates Nonclassical coordinates, c~.O Nondassical coordinates, c~1 9 As for binary systems, equilibrium compositions are obtained by numerical differentiation: f A~4 X1~~T~7 A[A 1 (24) \ 12 T,P,1~2 ~L ~12J T,P,~2 Some examples of coexistence curves calculated using the simple-scaling.

Application is illustrated with the determination of activity coefficients from minimal data (single data point), like azeotropic data and activity coefficients at infinite dilution, as well as from more complete data sets of vapor–liquid, solid–liquid, and liquid–liquid equilibrium.

Recommended Liquid–Liquid Equilibrium Data. Part 4. 1-Alkanol–Water Systems. Journal of Physical and Chemical Reference Data35 (3), J. Sørensen, W. Arlt: Liquid‐Liquid Equilibrium Data Collection, in der Reihe: Dechema Chemistry Data Series, Vol.

V., Part 1: Binary Systems. Seiten, Preis. = cal/mol/deg.K to make them comparable to CHEMCAD's. Set 3 was created after regressing VLE data for acetone (1)/water (2) at a constant pressure of bar from the same source. To perform a BIP regression, select Thermophysical > Regress BIPs.

Select the components, then Regress TPxy/Pxy/Txy VLE data and enter data. The recommended liquid–liquid equilibrium (LLE) data for 32 binary n-alkane, isoalkane, and cycloalkane–water systems have been obtained after critical evaluation of all data ( data sets) reported in the open literature up to the end of The evaluation of the alkane solubility data was based on a generalized equation, which allows prediction of the alkane solubility as a.

: Vapor-liquid equilibrium data collection (Chemistry data series) Volume 1 /part 1: Jurgen Gmehling, U. Onken: BooksManufacturer: Distributed by Scholium International. Liquid–liquid equilibrium (LLE) date for the ternary systems of {water + 1-propanol + dibutyl ether (DBE)} and (water + 1-butanol + DBE) were determined at T = (,) K under atmospheric pressure.

Distribution coefficients and separation factors of 1-propanol in the mixtures were calculated and are discussed. The influence of temperature on the.

Ternary liquid-liquid equilibrium data for hexane+1-butanol+water, carbon tetrachloride +propanoic acid+water, and water+propanoic acid+hexane were measured from very low concentrations of the solute to finite concentrations at 25°C.

The measured partition coefficients showed good. The group contribution method UNIFAC has become very popular because of its large range of applicability and its reliable predictions of vapor−liquid equilibria.

With the help of new data stored in the Dortmund Data Bank (DDB), many gaps in the existing UNIFAC parameter matrix have been filled, and many new main groups have been added to the parameter table. In this paper, the. The recommended vapor–liquid equilibrium (VLE) data for 36 binary systems involving primary, secondary, and tertiary alcohols with n-alkanes and isoalkanes [with the exception of 1-alkanols–n.

DECHEMA Chemistry Data Series, Liquid-Liquid Equilibrium Data Collection. Part 2: Ternary Systems Part 3: Ternary and Quaternary Systems Vol., +3, ().Vapor-Liquid Equilibrium Data. The experimental data shown in these pages are freely available and have been published already in the DDB Explorer data represent a small sub list of all available data in the Dortmund Data more data or any further information please search the DDB or contact DDBST.

Explorer Edition Data Main Page.It provides vapor-liquid equilibrium data for State: Two-component system, single-phase liquid or two-phase liquid-liquid in equilibrium with vapor Pure component 1: C6H5Cl Chlorobenzene [