Skip to Main content Skip to Navigation
Journal articles

Phase Equilibrium Measurements and Modeling of 1-propanethiol + 1-butanethiol + CH4 in Methane + Water Ternary Systems at 303, 336, and 365 K and Pressure Up to 9 MPa

Abstract : New vapor-liquid equilibrium (VLE) data for 1-propanethiol + 1-butanethiol + CH4 ternary system is reported. Measurements were performed at three different temperatures (303, 336 and 368 K), while the pressure was ranged from1 to 9 MPa. The total system pressure was maintained by CH4. The inlet mole fraction of 1-propanethiol (x = 5.43  10-1) and 1n-butanethiol (x = 4.56  10-1) in the liquid phase were same in all experiments. A static analytic method was used for performing phase equilibrium measurements. The new VLE data have been modeled successfully with Cubic-Plus-Association (CPA) EoS.
Document type :
Journal articles
Complete list of metadata

Cited literature [4 references]  Display  Hide  Download

https://hal-mines-paristech.archives-ouvertes.fr/hal-01258498
Contributor : Marie-Claude Watroba <>
Submitted on : Tuesday, January 19, 2016 - 10:58:35 AM
Last modification on : Friday, April 9, 2021 - 12:02:04 PM
Long-term archiving on: : Wednesday, April 20, 2016 - 11:11:28 AM

File

Manuscript-je-2016-001342-12-1...
Files produced by the author(s)

Identifiers

Collections

Citation

Javeed A. Awan, Christophe Coquelet, Ioannis Tsivintzelis, Georgios M. Kontogeorgis. Phase Equilibrium Measurements and Modeling of 1-propanethiol + 1-butanethiol + CH4 in Methane + Water Ternary Systems at 303, 336, and 365 K and Pressure Up to 9 MPa. Journal of Chemical and Engineering Data, American Chemical Society, 2016, 61, pp.41-44. ⟨10.1021/acs.jced.5b00134⟩. ⟨hal-01258498⟩

Share

Metrics

Record views

339

Files downloads

312