Vapor–Liquid Equilibrium Measurements and Cubic-Plus-Association Modeling of Triethylene Glycol + Water + Methane Systems at 6.0 and 12.5 MPa
Author:
Affiliation:
1. Center for Energy Resources Engineering (CERE), Department of Chemical and Biochemical Engineering, Technical University of Denmark (DTU), DK-2800Kgs Lyngby, Denmark
2. Research and Development Center, Equinor, N-7005Trondheim, Norway
Funder
Danmarks Tekniske Universitet
Equinor
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.2c00597
Reference26 articles.
1. Natural Gas Processing
2. Natural Gas Dehydration and Mercaptans Removal
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4. Advanced equation of state method for modeling TEG–water for glycol gas dehydration
5. Terms and Conditions for Transportation of Gas in the GASSLED, 2015, https://www.gassco.no/globalassets/terms-and-conditions-for-transportation-of-gas-in-gassled-01.10.2015.pdf (Accessed May 12, 2022).
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1. Solubility measurement of methane in triethylene glycol aqueous solutions (90,95,98 wt.% triethylene glycol) from 298 to 323 K and 0.17 to 2.5 MPa;Fluid Phase Equilibria;2024-08
2. Vapor–Liquid Equilibrium Measurements and Cubic-Plus-Association Modeling of Triethylene Glycol Systems;Journal of Chemical & Engineering Data;2024-06-17
3. Triethylene Glycol Solubility in High-Pressure Methane: New Experimental Data at 40 to 60 °C;Industrial & Engineering Chemistry Research;2024-02-06
4. Solubility Measurement of Methane in Triethylene Glycol Aqueous Solutions (90,95,98 Wt.% Triethylene Glycol) from 298 to 323 K and 0.17 to 2.5 Mpa;2023
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