Triethylene Glycol Solubility in High-Pressure Methane: New Experimental Data at 40 to 60 °C-Reference-Cited by-同舟云学术

Triethylene Glycol Solubility in High-Pressure Methane: New Experimental Data at 40 to 60 °C

Published:2024-02-06 Issue:6 Volume:63 Page:2895-2900
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Soroodan Ehsan¹²^ORCID,El-Okazy Moataz Ali²³,Macario Erwin⁴^ORCID,Kentish Sandra E.²^ORCID

Affiliation:

1. CSIRO Energy, Clayton, VIC 3168, Australia

2. Department of Chemical Engineering, The University of Melbourne, Parkville, VIC 3052, Australia

3. Chemical Engineering Department, Alexandria University, Bab Sharqi, Alexandria Governorate 5424041, Egypt

4. Worley Limited, Level 34, 385 Bourke Street, Melbourne VIC 3000, Australia

Funder

Future Fuels Co-operative Research Centre

Publisher

American Chemical Society (ACS)

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.3c04002

Reference17 articles.

1. Electrical Conductivity of Pipeline Deposits Under Pressure and Their Impacts on Sales-Gas Pipeline Cathodic Protection Systems

2. Burgass, R.; Reid, A.; Chapoy, A.; Tohidi, B. In Glycols Partitioning At High Pressures In Gas Processing Systems, 96th Annual Convention of the Gas Processors Association; GPA Midstream Association: San Antonio, TX, 2017; pp 77–92.

3. Process Design of Industrial Triethylene Glycol Processes Using the Cubic-Plus-Association (CPA) Equation of State

4. Multicomponent vapor-liquid equilibrium measurements and modeling of triethylene glycol, water, and natural gas mixtures at 6.0, 9.0 and 12.5 MPa

5. Vapor–Liquid Equilibrium Measurements and Cubic-Plus-Association Modeling of Triethylene Glycol + Water + Methane Systems at 6.0 and 12.5 MPa

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1. Vapor–Liquid Equilibrium Measurements and Cubic-Plus-Association Modeling of Triethylene Glycol Systems;Journal of Chemical & Engineering Data;2024-06-17