P–T–x Measurement and Modeling of Methane or Carbon Dioxide + Methanol +2,2′-[Ethane-1,2-diylbis(oxy)] di(ethan-1-ol) Systems from T = 298 to 323 K
Author:
Affiliation:
1. Thermodynamics Research Unit, School of Engineering, University of KwaZulu-Natal, Howard College Campus, Durban, 4041, South Africa
2. Department of Process Engineering, Stellenbosch University, Banhoekweg, Stellenbosch, 7600, South Africa
Funder
National Research Foundation
SARChI (South African Research Chairs Initiative) Program
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.2c00061
Reference39 articles.
1. Measurement of vapor–liquid–liquid phase equilibrium—Equipment and results
2. Carbon dioxide solubility in Triethylene Glycol and aqueous solutions
3. Phase Behavior in Natural Gas + Glycol Systems, Part 1: Tri(ethylene glycol) (TEG) and Its Aqueous Solutions
4. Measurement of the triethylene glycol solubility in supercritical methane at pressures up to 9MPa
5. Vapor liquid equilibria for acid gases and lower alkanes in triethylene glycol
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2. P-T-x measurement and modelling of (methane + propane + methanol + water + TEG) and (methane + propane + carbon dioxide + methanol + water + TEG) systems;The Journal of Supercritical Fluids;2023-12
3. P-T-x Measurement and Modeling of Methane + Propane + Methanol or 2,2′-[Ethane-1,2-diylbis(oxy)] Di(ethan-1-ol) and Methane + Propane + Methanol + 2,2′-[Ethane-1,2-diylbis(oxy)] Di(ethan-1-ol) Systems;Journal of Chemical & Engineering Data;2023-03-08
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