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Measurements and Correlations of the Isobaric Vapor–Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa

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What this work says

Outgoing claims: the papers this work cites, builds on, or argues with.

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A generalized thermodynamic correlation based on three‐parameter corresponding states

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Second virial coefficients of water pollutants

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Measurements and Analysis of Excess Enthalpies of Ester + n‐Alkane Using the UNIFAC Model

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Volumetric study of (an aliphatic methyl ester + heptane or nonane) at the temperature 298.15 K

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Thermodynamic properties of (an ethyl ester + and -alkane). IX.mEandmEfor { CH3(CH2)uCOOCH2CH3+ (1− )CH3(CH2)2v + 1CH3} with = 0 to 5, and = 1 to 7

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Organic solvents: Physical properties and methods of purification

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Excess molar volumes of (methyl butanoate + n-heptane + n-decane) and of (butyl butanoate + n-heptane + n-decane) at 298.15 K

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Excess molar enthalpies of methyl alkanoates + n-nonane at 298.15 k

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Vapor-liquid equilibria using UNIFAC. A group contribution method

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Vapour pressures of some ethyl and propyl esters of fatty acids

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Excess properties and isobaric vapor–liquid equilibria for four binary systems of alkyl (methyl to butyl) methanoates with decane

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Thermodynamic properties of (an ester + an alkane). XVI. Experimental HmE and VmE values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K

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Thermodynamic properties of (an ester + an alkane). XVIII. Experimental HmEandVmE values for (an alkyl butanoate + an alkane) at T= 318.15 K

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Thermodynamic properties of (an ethyl ester+a branched alkane). XV. HmE and VmE values for (an ester+an alkane)

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Volumetric properties and viscosities of the methyl butanoate + n-heptane + n-octane ternary system and its binary constituents in the temperature range from 283.15 to 313.15 K

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A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties

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A New Correlation Method for Vapor−Liquid Equilibria and Excess Enthalpies for Nonideal Solutions Using a Genetic Algorithm. Application to Ethanol + an n-Alkane Mixtures

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New Parametric Model to Correlate the Gibbs Excess Function and Other Thermodynamic Properties of Multicomponent Systems. Application to Binary Systems

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The Volumetric and Thermodynamic Properties of Fluids. I. Theoretical Basis and Virial Coefficients 1

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Excess Molar Volumes of Binary Mixtures Containing a Methyl Ester (Ethanoate to Tetradecanoate) with Odd n-Alkanes at 298.15 K

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Isobaric vapor-liquid equilibria of ethyl acetate + ethanol mixtures at 760 .+-. 0.5 mmHg

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Isobaric vapor-liquid equilibrium of methyl butanoate with ethanol and 1-propanol binary systems

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Isobaric Vapor−Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane

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Isobaric Vapor−Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane

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Measurements of the Excess Properties and Vapor−Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)

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Isothermal vapor-liquid equilibrium data for the system heptane-ethyl butyrate at 74.7 and 100.deg.

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Improved equation for prediction of saturated liquid density

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saturated liquid molar volumes. Rackett equation

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Vapor−Liquid Equilibria and Densities for Ethyl Esters (Ethanoate to Butanoate) and Alkan-2-ol (C3−C4) at 101.32 kPa

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Densities, Relative Permittivities, Excess Volumes, and Excess Molar Polarizations for Alkyl Ester (Methyl Propanoate, Methyl Butanoate, Ethyl Propanoate, and Ethyl Butanoate) + Hydrocarbons (n-Heptane, Benzene, Chlorobenzene, and 1,1,2,2-Tetrachloroethane) at 308.15 K and 318.15 K

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Physical Properties of Molecular Crystals, Liquids and Glasses

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What points at this work

Incoming claims: where this work appears in other papers’ reference lists and arguments.

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Experimental Determination and Theoretical Modelling of Isobaric Vapor-Liquid Equilibria, Liquid Mass Density, Surface Tension and Dynamic Viscosity for Methyl Butyrate and Tert -Butanol Binary Mixture

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