Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
Author:
Affiliation:
1. Escuela de Ingenierías Industriales y Civiles, Universidad de Las Palmas de Gran Canaria, 35017 Las Palmas de Gran Canaria, Canary Islands, Spain
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.9b00668
Reference41 articles.
1. Gmehling, J.; Onken, U. In Vapor–Liquid Equilibrium Data Collection; Vol. 1; Dechema: Frankfurt, 2002, part 5b, pp. 76, 259–264.
2. Isobaric Vapor−Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
3. Measurements of the Excess Properties and Vapor−Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
4. Gmehling, J.; Menke, J.; Krafczyk, J.; Fischer, K. In Azeotropic Data, 2nd ed. Wiley–VCH Verlag: Weinheim: Germany, 2004, part 1, pp. 399–501.
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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. 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
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