Experimental measurement and thermodynamic modelling of phase equilibria of semi-clathrate hydrates of (CO2 + tetra-n-butyl-ammonium bromide) aqueous solution
- 1. Faculty of Petroleum Engineering, Petroleum University of Technology (PUT), Ahwaz (Iran, Islamic Republic of)
- 2. Department of Chemical Engineering, Iran University of Science and Technology (IUST), Tehran (Iran, Islamic Republic of)
- 3. Thermodynamics Research Unit, School of Engineering, University of KwaZulu-Natal, Howard College Campus, King George V Avenue, Durban 4041 (South Africa)
- 4. Institut de Recherche en Génie Chimique et Pétrolier (IRGCP), Paris Cedex (France)
Description
Highlights: • Hydrate phase equilibrium data are reported for the CO2 + TBAB aqueous solutions systems. • A thermodynamic model is developed to predict the dissociation conditions of the latter systems. • The properties of the aqueous phase are calculated using the AMSA-NRTL electrolyte model. • The model satisfactorily predicts the experimental data with an AARD% of approximately 13%. - Abstract: Comprehensive studies on semi-clathrate hydrates phase equilibria are still required to better understand characteristics of this type of clathrates. In this communication, new experimental data on the dissociation conditions of semi-clathrate hydrates of {carbon dioxide + tetra-n-butyl-ammonium bromide (TBAB)} aqueous solution are first reported in a wide range of TBAB concentrations and at different pressures and temperatures. A thermodynamic model is then proposed to predict the dissociation conditions of the semi-clathrate hydrates for the latter system. The (hydrate + TBAB) aqueous solution (H + Lw) phase equilibrium prediction is considered based on Gibbs free energy minimization approach. A modified van der Waals–Platteeuw solid solution theory developed based on the (H + Lw) equilibrium information is employed to predict the dissociation conditions of semi-clathrate hydrates of carbon dioxide + TBAB. The properties of the aqueous solution are estimated using the AMSA-NRTL electrolyte model (considering the association and hydration of ions). The Peng–Robinson equation of state is used for estimating the gas/vapour phase properties. Results show that the proposed model satisfactorily predicts the experimental values with an average absolute relative deviation of approximately 13%
Availability note (English)
Available from http://dx.doi.org/10.1016/j.jct.2015.03.024Additional details
Identifiers
- DOI
- 10.1016/j.jct.2015.03.024;
- PII
- S0021-9614(15)00086-5;
Publishing Information
- Journal Title
- Journal of Chemical Thermodynamics
- Journal Volume
- 87
- Journal Page Range
- p. 122-128
- ISSN
- 0021-9614
- CODEN
- JCTDAF
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 47043172
- Subject category
- S37: INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY;
- Descriptors DEI
- AMMONIUM COMPOUNDS; AQUEOUS SOLUTIONS; BROMIDES; CARBON DIOXIDE; CLATHRATES; CONCENTRATION RATIO; DISSOCIATION; ELECTROLYTES; EQUATIONS OF STATE; EQUILIBRIUM; FREE ENTHALPY; GAS HYDRATES; HYDRATION; PHASE DIAGRAMS; SOLID SOLUTIONS; VAN DER WAALS FORCES; VAPORS
- Descriptors DEC
- BROMINE COMPOUNDS; CARBON COMPOUNDS; CARBON OXIDES; CHALCOGENIDES; DIAGRAMS; DIMENSIONLESS NUMBERS; DISPERSIONS; ENERGY; EQUATIONS; FLUIDS; GASES; HALIDES; HALOGEN COMPOUNDS; HOMOGENEOUS MIXTURES; HYDRATES; INFORMATION; MIXTURES; OXIDES; OXYGEN COMPOUNDS; PHYSICAL PROPERTIES; SOLUTIONS; SOLVATION; THERMODYNAMIC PROPERTIES
Optional Information
- Copyright
- Copyright (c) 2015 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.