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Phase equilibria of H 2S-hydrocarbons (propane, n-butane, and n-pentane) binary systems at low temperatures

Moussa Dicko 1 Christophe Coquelet 2 Pascal Théveneau 3 Pascal Mougin 4
1 LSPM - Laboratoire des Sciences des Procédés et des Matériaux
2 CEP/Fontainebleau
CEP - Centre Énergétique et Procédés
3 CEP - Centre Énergétique et Procédés
4 IFPEN - IFP Energies nouvelles
Abstract : Isothermal vapor-liquid equilibrium measurements of three binary systems, H 2S + propane, H 2S + n-butane, and H 2S + n-pentane, have been performed with a static synthetic apparatus at low temperatures. The method of Barker has been implemented to determine the corresponding nonrandom two-liquid (NRTL) parameters and to calculate the liquid mole fractions. The results have been further used along with literature data to adjust binary interaction parameters of the Peng-Robinson equation of state. Good agreement with Dechema values has been found.
Keywords : Binary interaction parameter Binary systems Isothermal vapor-liquid equilibrium Literature data Low temperatures Mole fraction n-Butane N-pentane Non random two liquids Peng-Robinson equation of state Butane Hydrocarbons Propane
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https://hal-mines-paristech.archives-ouvertes.fr/hal-00796474
Contributor : Jordane Raisin-Dadre <>
Submitted on : Monday, March 4, 2013 - 11:38:18 AM
Last modification on : Friday, April 9, 2021 - 12:02:04 PM

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IFP | ENSMP | ENSMP_CEP | PARISTECH | LSPM_P13 | UNIV-PARIS13 | INSTITUT-TELECOM | CNRS | USPC | GALILE | SORBONNE-PARIS-NORD | PSL

Citation

Moussa Dicko, Christophe Coquelet, Pascal Théveneau, Pascal Mougin. Phase equilibria of H 2S-hydrocarbons (propane, n-butane, and n-pentane) binary systems at low temperatures. Journal of Chemical and Engineering Data, American Chemical Society, 2012, 57 (5), pp.1534-1543. ⟨10.1021/je300111m⟩. ⟨hal-00796474⟩

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