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Petroleum Science and Technology Volume 36, 2018 - Issue 3
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Original Articles

The solubility of acid gases in the ionic liquid [C8mim][PF6]

Alireza AfsharpourYoung Researchers and Elite Club, Qazvin Branch, Islamic Azad University, Qazvin, IranCorrespondence[email protected]
&
Alireza KheiriDepartment of technical unit, Kalleh dairy co, Amol, Iran
Pages 232-238 | Published online: 29 Dec 2017

References

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  • Afsharpour, A., and A. Haghtalab 2017. Modeling of CO2 solubility in aqueous N-methyldiethanolamine solution using electrolyte modified HKM plus association equation of state. Fluid Phase Equilib. 433:149–158.
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  • Georgios Kontogeorgis, M., and G. K. Folas. 2010. Thermodynamic Models for Industrial Applications. Chichester, United Kingdom: John Wiley & Sons Ltd.
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  • Macías-Salinas, R., J. A. Chávez-Velasco, M. Aquino-Olivos, J. Mendoza de la Cruz, and J. C. Sánchez-Ochoa. 2013. Accurate Modeling of CO2 Solubility in Ionic Liquids Using a Cubic EoS. Ind. Eng. Chem. Res. 52 (22):7593–601.
  • Safavi, M., C. Ghotbi, V. Taghikhani, A. H. Jalili, and A. Mehdizadeh. 2013. Study of the solubility of CO2, H2S and their mixture in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate: Experimental and modelling. J. Chem. Thermodynamics 65:220–32.
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  • Tomida, D., A. Kumagai, S. Kenmochi, K. Qiao, and C. Yokoyama. 2007. Viscosity of 1-hexyl-3 methylimidazolium hexafluorophosphate and 1-Octyl-3-methylimidazolium hexafluorophosphate at high pressure. J. Chem. Eng. Data 52:577–9.
  • Tsivintzelis, I., G. M. Kontogeorgis, M. L. Michelsen, and E. H. Stenby. 2010. Modeling phase equilibria for acid gas mixtures using the CPA equation of state. I. Mixtures with H2S. AIChE Journal 56:2965–82.
  • Voutsas, E., C. Perakis, G. Pappa, and D. Tassios. 2007. An evaluation of the performance of the Cubic-Plus-Association equation of state in mixtures of non-polar, polar and associating compounds: Towards a single model for non-polymeric systems. Fluid Phase Equilibria 261:343–50.

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