Experimental Determination of Densities and Isobaric Vapor−Liquid Equilibria of Binary Mixtures Formed by a Propyl Alkanoate (Methanoate to Butanoate) + An Alkan-2-ol (C3, C4)-Reference-Cited by-同舟云学术

Experimental Determination of Densities and Isobaric Vapor−Liquid Equilibria of Binary Mixtures Formed by a Propyl Alkanoate (Methanoate to Butanoate) + An Alkan-2-ol (C3, C4)

Published:1999-06-15 Issue:4 Volume:44 Page:772-783
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

González Carmelo¹,Ortega Juan¹,Hernández Pablo¹,Galván Salvador¹

Affiliation:

1. Laboratorio de Termodinámica y Fisicoquímica, Universidad Las Palmas de Gran Canaria, C/. Rabadán núm. 33, 35003-Las Palmas de Gran Canaria, Islas Canarias, Spain

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/je980304p

Reference28 articles.

1. Densities and Vapor−Liquid Equilibria in Binary Mixtures Formed by Propyl Methanoate + Ethanol, +Propan-1-ol, and +Butan-1-ol at 160.0 kPa

2. Vapour pressures of some ethyl and propyl esters of fatty acids

3. Fredenslund, Aa.; Gmehling, J.; Rasmussen, P.Vapor−LiquidEquilibriaUsingUNIFAC.AGroupContributionModel; Elsevier: Amsterdam, 1977; pp 27−64.

Cited by 34 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. Accounting for cross-association in nonself-associating species using SAFT-VR Mie: Application to mixtures with esters;Fluid Phase Equilibria;2023-06

2. Ebulliometric determination of vapour liquid equilibria for 1-propanol – n-propyl acetate system;Chemical Data Collections;2023-04

3. PC–SAFT modeling of the high pressure VLE data for 2,2,4–Trimethylpentane with Ethanol, 1–Propanol, 2–Propanol and 1–Butanol. Experimental equipment and binary systems at 1.5 MPa;The Journal of Chemical Thermodynamics;2022-09

4. High Pressure Vapor–Liquid Equilibria of n-Heptane with Ethanol, 1-Propanol, 2-Propanol, and 1-Butanol at 1.5 MPa: Experimental Data of Binary Systems and Perturbed Chain–Statistical Associating Fluid Theory Model Predictions;Journal of Chemical & Engineering Data;2022-05-04

5. Isobaric Vapor–Liquid Equilibrium Data for the Isopropanol–Water System;Journal of Chemical & Engineering Data;2021-10-15