New Advances in the Modeling and Verification of Experimental Information for Ester–Alkane Solutions: Application to a Batch-Distillation Case-Reference-Cited by-同舟云学术

New Advances in the Modeling and Verification of Experimental Information for Ester–Alkane Solutions: Application to a Batch-Distillation Case

Published:2020-04-05 Issue:17 Volume:59 Page:8346-8360
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Ortega Juan¹^ORCID,Fernández Luis¹,Sosa Adriel¹,Lorenzo Beatriz¹,Ríos Raúl¹,Wisniak Jaime²

Affiliation:

1. Grupo de Ingeniería Térmica e Instrumentación (IDeTIC), Parque Científico-Tecnológico, Universidad de Las Palmas de Gran Canaria, 35071 Las Palmas deGran Canaria, Canary Islands, Spain

2. Department of Chemical Engineering, Ben-Gurion University of the Negev, Beer-Sheva 84105, Israel

Funder

Ministerio de Ciencia e Innovaci?n

Agencia Canaria de Investigaci?n, Innovaci?n y Sociedad de la Informaci?n

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.0c00850

Reference52 articles.

1. Excess Properties for Propyl Propanoate + Hexane + Benzene at 298.15 K

2. Thermodynamic properties of (a propyl ester + an n-alkane) at 298.15 K I. {xC2H5CO2C3H7 + (1 − x)CnH2n+2}, (n = 6 to 10)

3. Excess Molar Enthalpies of Propyl Propanoate + Hexane + Benzene at 298.15 K and 308.15 K

4. Vapor−Liquid Equilibria for Binary Systems Composed of a Propyl Ester (Ethanoate, Propanoate, Butanoate) + an n-Alkane (C7, C9)

5. Thermodynamic properties of (a propyl ester+ann-alkane). XII. Excess molar enthalpies and excess molar volumes for {xCH3(CH2)u−1COO(CH2)2CH3+(1−x)CH3(CH2)2v+1CH3} withu=(1to 3), andv=(1to 7)

Cited by 5 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. Thermodynamic Behavior of the (Methylcyclopentane + Ethyl Acetate) Binary Liquid Mixture: Density at Several Temperatures and Vapor–Liquid Equilibrium at 25, 50, and 101.3 kPa;Journal of Chemical & Engineering Data;2024-03-19

2. Density, Excess Molar Volume and Vapor–Liquid Equilibrium Measurements at 101.3 kPa for Binary Mixtures Containing Ethyl Acetate and a Branched Alkane: Experimental Data and Modeling;Liquids;2023-04-11

3. Compressed liquid densities for cyclopentane/n-heptane mixtures from 293.15 K to 363.15 K at pressures up to 70 MPa;The Journal of Chemical Thermodynamics;2023-02

4. The precision-complexity binomial to achieve the best mathematical-thermodynamic modelling on the Gibbs-function and its effect on the separation processes design;Journal of Industrial and Engineering Chemistry;2022-04

5. Methodology Based on the Theory of Information to Describe the Representation Ability of the DMC + Alkane Behavior;Industrial & Engineering Chemistry Research;2021-01-07