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Crystallization risk of aromatic compounds in LNG production. Part II: The solubility of p-xylene in methane-rich mixtures down to cryogenic temperatures
Experimental Measurements and Modeling of Vapor–Liquid Equilibria for Eight Mixtures Containing trans-1-Chloro-3,3,3-trifluoropropene (R1233zd(E)) and 2-Chloro-3,3,3-trifluoropropene (R1233xf)
Jamal El Abbadi, Julien Brocus, Alain Valtz, Christophe Coquelet and Céline Houriez Journal of Chemical & Engineering Data 68(9) 2316 (2023) https://doi.org/10.1021/acs.jced.3c00296
Separation of Xenon from Noble Gas Mixtures of Argon, Krypton, and Xenon Using Gas Hydrate Technology
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Phase behavior of carbon dioxide + 2,4-dimethylpentane binary system at high pressures
Mihaela Ioniţă, Sergiu Sima, Adrian Crişciu, Catinca Secuianu and Dan Vladimir Nichita The Journal of Supercritical Fluids 199 105941 (2023) https://doi.org/10.1016/j.supflu.2023.105941
Phase Behavior of Carbon Dioxide + Isobutanol and Carbon Dioxide + tert-Butanol Binary Systems
Methane + neo-pentane system: VLE measurements, modeling of the phase diagram including solid phases
Marco Campestrini, Alain Valtz, Salem Hoceini and Paolo Stringari The Journal of Chemical Thermodynamics 166 106687 (2022) https://doi.org/10.1016/j.jct.2021.106687
New Experimental Vapor-Liquid Equilibria Data and Thermodynamic Modelling for R1234yf/propane/R32 as low-GWP Mixtures in Heat Pump Applications
Experimental study of impurity freeze-out in ternary methane + ethane + benzene mixtures with applications to LNG production
Arman Siahvashi, Saif Z.S. Al Ghafri, Brendan F. Graham and Eric F. May Journal of Natural Gas Science and Engineering 90 103918 (2021) https://doi.org/10.1016/j.jngse.2021.103918
Vapor–Liquid Equilibria for Carbon Dioxide + 3,3,3-Trifluoropropene Binary Mixtures at Temperatures between (288 and 348) K
Mirhadi S. Sadaghiani, Arash Arami-Niya, Benjamin Marsh, Saif Z.S. Al Ghafri and Eric F. May Journal of Chemical & Engineering Data 66(11) 4044 (2021) https://doi.org/10.1021/acs.jced.1c00297
Evolving LSSVM and ELM models to predict solubility of non-hydrocarbon gases in aqueous electrolyte systems
Measurement and Modeling of the Solubility of Tetrafluoromethane in Either Perfluoroheptane or Perfluorodecalin
Rasoul Hassanalizadeh, Wayne Michael Nelson, Paramespri Naidoo and Deresh Ramjugernath Journal of Chemical & Engineering Data 65(10) 4862 (2020) https://doi.org/10.1021/acs.jced.0c00461
Measurement and modelling of the thermodynamic properties of carbon dioxide mixtures with HFO-1234yf, HFC-125, HFC-134a, and HFC-32: vapour-liquid equilibrium, density, and heat capacity
High-pressure experimental vapour-liquid-liquid equilibrium measurements and modelling for natural gas processing: Equipment validation, and the system CH4+nC6H14+H2O
Modeling of Trifluoromethane (R-23) or Hexafluoroethane (R-116) and Alkane Binary Mixtures using the Group-Contribution with Association Equation of State
Mark D. Williams-Wynn, Francisco Adrián Sánchez, Paramespri Naidoo, Selva Pereda and Deresh Ramjugernath Industrial & Engineering Chemistry Research 57(31) 10640 (2018) https://doi.org/10.1021/acs.iecr.8b01933
Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K
Karima Djebaili, Elise El Ahmar, Alain Valtz, Abdeslam Hassen Meniai and Christophe Coquelet Journal of Chemical & Engineering Data (2018) https://doi.org/10.1021/acs.jced.8b00683
Gas solubilities of carbon dioxide in methanol, acetone, mixtures of methanol and water, and mixtures of methanol and acetone
Isothermal Vapor–Liquid Equilibrium Data for the Hexafluoroethane (R116) + n-Butane System at Temperatures from 273 to 323 K
Deresh Ramjugernath, Alain Valtz, Dominique Richon, Mark D. Williams-Wynn and Christophe Coquelet Journal of Chemical & Engineering Data 62(10) 3483 (2017) https://doi.org/10.1021/acs.jced.7b00485
Solubility of carbon monoxide in bio-oil compounds
Muhammad Saad Qureshi, Tom Le Nedelec, Hernando Guerrero-Amaya, et al. The Journal of Chemical Thermodynamics 105 296 (2017) https://doi.org/10.1016/j.jct.2016.10.030
Vapor–liquid equilibrium data for the carbon dioxide and nitrogen (CO 2 + N 2 ) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPa
Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Phase Equilibria for Perfluoroethane + (n-Perfluorohexane or n-Perfluorooctane) Binary Systems: Measurement and Modeling
Piniel Nyasha Bengesai, Wayne Michael Nelson, Paramespri Naidoo and Deresh Ramjugernath Journal of Chemical & Engineering Data 61(9) 3363 (2016) https://doi.org/10.1021/acs.jced.6b00409
Densities and derived thermophysical properties of the 0.9505 CO2+ 0.0495 H2S mixture from 273 K to 353 K and pressures up to 41 MPa
Design of Equilibrium Cells for Phase Equilibria and PVT Measurements in Large Ranges of Temperatures and Pressures. I. Vapor–Liquid–Liquid Equilibria
Petri Uusi-Kyyny, Simona Ionita, Muhammad Saad Qureshi, Ville Alopaeus and Dominique Richon Journal of Chemical & Engineering Data 61(8) 2700 (2016) https://doi.org/10.1021/acs.jced.6b00126
High-pressure phase equilibria data for mixtures involving ethene and perfluoro-n-octane from 293 to 353 K
Wayne Michael Nelson, Zoubir Tebbal, Paramespri Naidoo, Latifa Negadi and Deresh Ramjugernath Fluid Phase Equilibria 408 33 (2016) https://doi.org/10.1016/j.fluid.2015.07.054
An improved static–analytic apparatus for vapor–liquid equilibrium ( PTxy ) measurement using modified in-situ samplers
Vapor-liquid equilibrium data for the carbon dioxide and oxygen (CO2 + O2) system at the temperatures 218, 233, 253, 273, 288 and 298 K and pressures up to 14 MPa
Isothermal Vapor–Liquid Equilibrium Data for the 1,1,2,3,3,3-Hexafluoroprop-1-ene +1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (292 to 352) K and Pressures up to 2.6 MPa
Francois J. Conradie, Philippus L. Crouse, Xavier Courtial, et al. Journal of Chemical & Engineering Data 60(3) 966 (2015) https://doi.org/10.1021/je501047e
Isothermal phase (vapour+liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318)K
Shalendra Clinton Subramoney, Wayne Michael Nelson, Xavier Courtial, et al. The Journal of Chemical Thermodynamics 90 100 (2015) https://doi.org/10.1016/j.jct.2015.06.017
Measurement of vapor–liquid–liquid phase equilibrium—Equipment and results
Isothermal vapor–liquid equilibrium data for the ethene+2,2,3-trifluoro-3-(trifluoromethyl)oxirane binary system between 258 and 308K at pressures up to 4.5MPa
Design and test of a new high pressure phase equilibrium apparatus for highly corrosive mixtures of importance for natural gas
Maria T. Mota-Martinez, Sabbir Samdani, Abdallah S. Berrouk, et al. Journal of Natural Gas Science and Engineering 27 661 (2015) https://doi.org/10.1016/j.jngse.2015.09.008
Isothermal Vapor–Liquid Equilibrium (VLE) and Vapor–Liquid–Liquid Equilibrium (VLLE) Data for Two Binary Systems Containing Perfluorohexane with Carbon Monoxide or Hydrogen Sulfide at (293, 313, and 333) K
Mulamba Marc Tshibangu, Alain Valtz, Caleb Narasigadu, Christophe Coquelet and Deresh Ramjugernath Journal of Chemical & Engineering Data 60(8) 2461 (2015) https://doi.org/10.1021/acs.jced.5b00318
High-pressure (vapour+liquid) equilibria for ternary systems composed by {(E)-2-hexenal or hexanal+carbon dioxide+water}: Partition coefficient measurement
Arturo Bejarano, Pablo I. López, José M. del Valle and Juan C. de la Fuente The Journal of Chemical Thermodynamics 89 79 (2015) https://doi.org/10.1016/j.jct.2015.05.003
Isothermal Vapor–Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
Wayne Michael Nelson, Mark Williams-Wynn, Shalendra Clinton Subramoney and Deresh Ramjugernath Journal of Chemical & Engineering Data 60(3) 568 (2015) https://doi.org/10.1021/je5006938
High Pressure Fluid Technology for Green Food Processing
José M. S. Fonseca, Ralf Dohrn and Stephanie Peper Food Engineering Series, High Pressure Fluid Technology for Green Food Processing 3 (2015) https://doi.org/10.1007/978-3-319-10611-3_1
Vapor–Liquid Equilibrium of Methane with Water and Methanol. Measurements and Modeling
Michael Frost, Eirini Karakatsani, Nicolas von Solms, Dominique Richon and Georgios M. Kontogeorgis Journal of Chemical & Engineering Data 59(4) 961 (2014) https://doi.org/10.1021/je400684k
Isothermal Vapor–Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
Francois J. Conradie, Philippus L. Crouse, Xavier Courtial, et al. Journal of Chemical & Engineering Data 59(1) 82 (2014) https://doi.org/10.1021/je400828j
Phase Equilibria of Clathrate Hydrates of Ethyne + Propane
Kaniki Tumba, Saeedeh Babaee, Paramespri Naidoo, Amir H. Mohammadi and Deresh Ramjugernath Journal of Chemical & Engineering Data 59(9) 2914 (2014) https://doi.org/10.1021/je500598j
Isothermal Vapor–Liquid Equilibrium Data and Thermodynamic Modeling for Binary Systems of Perfluorobutane (R610) + (Methane or Hydrogen Sulfide) at (293, 313, and 333) K
Mulamba Marc Tshibangu, Alain Valtz, Caleb Narasigadu, Christophe Coquelet and Deresh Ramjugernath Journal of Chemical & Engineering Data 59(9) 2865 (2014) https://doi.org/10.1021/je500496y
Phase equilibrium data for the hydrogen sulphide + methane system at temperatures from 186 to 313 K and pressures up to about 14 MPa
Vapor–Liquid Equilibrium (VLE) Data and Thermodynamic Modeling for Binary Systems Containing Perfluorobutane (R610) with Carbon Monoxide or Nitric Oxide at (293, 313, and 333) K
Mulamba M. Tshibangu, Alain Valtz, Caleb Narasigadu, Christophe Coquelet and Deresh Ramjugernath Journal of Chemical & Engineering Data 59(2) 346 (2014) https://doi.org/10.1021/je400822m
New high-pressures vapor-liquid equilibrium data for the carbon dioxide + 2-methyl-2-propanol binary system
Isothermal Vapor–Liquid Equilibrium Data and Modeling for the Ethane (R170) + Perfluoropropane (R218) System at Temperatures from (264 to 308) K
Mulamba Marc Tshibangu, Xavier Courtial, Christophe Coquelet, Paramespri Naidoo and Deresh Ramjugernath Journal of Chemical & Engineering Data 58(5) 1316 (2013) https://doi.org/10.1021/je4000857
Accurate Measurements of CO2 Rich Mixture Phase Equilibria Relevant for CCS Transport and Conditioning
Experimental vapour–liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Shalendra Clinton Subramoney, Alain Valtz, Christophe Coquelet, et al. The Journal of Chemical Thermodynamics 61 18 (2013) https://doi.org/10.1016/j.jct.2013.01.017
Vapor–liquid equilibrium for the ternary carbon dioxide–ethanol–nonane and decane systems
Miguel G. Arenas-Quevedo, Luis A. Galicia-Luna, Octavio Elizalde-Solis and José A. Pérez-Pimienta Fluid Phase Equilibria 338 30 (2013) https://doi.org/10.1016/j.fluid.2012.10.012
Isothermal vapor–liquid equilibrium of R170+n-perfluorooctane at 308–338K: Measurement, equation of state modelling, and molecular simulation
Isothermal vapor–liquid equilibrium data for the ethylene+1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308K at pressures up to 4.56MPa
Vapor–liquid equilibrium data for the dimethyl ether (RE170)+decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83K and pressures up to 4.9MPa
Vapor–liquid equilibria of ethylene (C2H4)+decafluorobutane (C4F10) at 268–298K from experiment, molecular simulation and the Peng–Robinson equation of state
Experimental Vapor–Liquid Equilibrium for the Quaternary Carbon Dioxide + Ethanol + Thiophene + Pentane/Nonane Systems
Verónica Serrano-Cocoletzi, Luis A. Galicia-Luna and Octavio Elizalde-Solis Journal of Chemical & Engineering Data 57(10) 2896 (2012) https://doi.org/10.1021/je300831t
Compositional analysis of the gas phase for the CO2+N2+tetra-n-butylammonium bromide aqueous solution systems under hydrate stability conditions
Isothermal Vapor–Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (248 to 283) K
Francois J. Conradie, Philippus L. Crouse, Xavier Courtial, Izak J. van der Walt and Deresh Ramjugernath Journal of Chemical & Engineering Data 57(7) 1978 (2012) https://doi.org/10.1021/je300217x
Vapor–Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
Shalendra C. Subramoney, Alain Valtz, Christophe Coquelet, et al. Journal of Chemical & Engineering Data 57(11) 2947 (2012) https://doi.org/10.1021/je300431n
Sampling from fluid mixtures under high pressure: Review, case study and evaluation
Phase equilibria of CO2+N2 and CO2+CH4 clathrate hydrates: Experimental measurements and thermodynamic modelling
Imen Ben Attouche Sfaxi, Veronica Belandria, Amir H. Mohammadi, Rafael Lugo and Dominique Richon Chemical Engineering Science 84 602 (2012) https://doi.org/10.1016/j.ces.2012.08.041
Experimental Methods for Phase Equilibria at High Pressures
Study of Gas Hydrate Formation in the Carbon Dioxide + Hydrogen + Water Systems: Compositional Analysis of the Gas Phase
Veronica Belandria, Ali Eslamimanesh, Amir H. Mohammadi and Dominique Richon Industrial & Engineering Chemistry Research 50(10) 6455 (2011) https://doi.org/10.1021/ie102335v
Gas Hydrate Formation in Carbon Dioxide + Nitrogen + Water System: Compositional Analysis of Equilibrium Phases
Veronica Belandria, Ali Eslamimanesh, Amir H. Mohammadi and Dominique Richon Industrial & Engineering Chemistry Research 50(8) 4722 (2011) https://doi.org/10.1021/ie101635k
Vapor–Liquid Equilibria of Binary and Ternary Systems Containing Carbon Dioxide, Alkane, and Benzothiophene
Luis E. Camacho-Camacho, Luis A. Galicia-Luna and Octavio Elizalde-Solis Journal of Chemical & Engineering Data 56(11) 4109 (2011) https://doi.org/10.1021/je200586g
New High Pressure Vapor–Liquid Equilibrium and Density Predictions for the Carbon Dioxide + Ethanol System
Sergiu Sima, Viorel Feroiu and Dan Geană Journal of Chemical & Engineering Data 56(12) 5052 (2011) https://doi.org/10.1021/je2008186
Vapor−Liquid Equilibrium Data for Binary Systems Consisting of Either Hexafluoropropene (HFP) or 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane (HFPO) with Carbon Dioxide (R-744) or 2,2-Dichloro-1,1,1-trifluoroethane (R-123)
W. M. Nelson, S. C. Subramoney, A. Valtz, et al. Journal of Chemical & Engineering Data 56(1) 74 (2011) https://doi.org/10.1021/je100841y
Compositional Analysis and Hydrate Dissociation Conditions Measurements for Carbon Dioxide + Methane + Water System
Veronica Belandria, Ali Eslamimanesh, Amir H. Mohammadi, et al. Industrial & Engineering Chemistry Research 50(9) 5783 (2011) https://doi.org/10.1021/ie101959t
Vapor−Liquid Equilibrium Data for the Nitrogen + Dodecane System at Temperatures from (344 to 593) K and at Pressures up to 60 MPa
Tomás García-Córdova, Daimler N. Justo-García, Blanca E. García-Flores and Fernando García-Sánchez Journal of Chemical & Engineering Data 56(4) 1555 (2011) https://doi.org/10.1021/je1012372
Vapor–Liquid Equilibrium Measurements for the Ternary Systems of CO2+n-Hexane +n-Decane and CO2+n-Octane +n-Decane
Carmen Sánchez-García, Karla E. Vázquez-Hernández, Luis A. Galicia-Luna and Octavio Elizalde-Solis Industrial & Engineering Chemistry Research 50(21) 12254 (2011) https://doi.org/10.1021/ie201516g
Isothermal vapor–liquid equilibrium data for the carbon dioxide (R744)+decafluorobutane (R610) system at temperatures from 263 to 353K
Alain Valtz, Xavier Courtial, Erik Johansson, Christophe Coquelet and Deresh Ramjugernath Fluid Phase Equilibria 304(1-2) 44 (2011) https://doi.org/10.1016/j.fluid.2011.01.017
Thermodynamic study of binary systems containing sulphur dioxide: Measurements and molecular modelling