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Thermodynamic study of the CO2 – H2O – NaCl system: Measurements of CO2 solubility and modeling of phase equilibria using Soreide and Whitson, electrolyte CPA and SIT models

International journal of greenhouse gas control, 2019-12, Vol.91, p.102825, Article 102825

2019

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Excess Molar Volumes and Enthalpies of Binary Mixtures Containing Furan and Toluene, 1-Octanol or n-Hexane at Temperatures Up to 383.15 K and Pressure Up to 1.6 MPa

Journal of solution chemistry, 2024, Vol.53 (1), p.60-79

2024

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Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air

Journal of chemical and engineering data, 2018-04, Vol.63 (4), p.1021-1026

2018

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Vapor–liquid equilibrium and molecular simulation data for carbon dioxide (CO2) + trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02 K and pressures up to 7.6 MPa

International journal of refrigeration, 2019-02, Vol.98, p.362-371

2019

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Thermodynamic study of binary systems containing sulphur dioxide and nitric oxide: Measurements and modelling

Fluid phase equilibria, 2018-04, Vol.461, p.84-100

2018

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Apparent Henry’s law constants of furan in different n -alkanes and alcohols at temperatures from 293 to 323 K

Journal of environmental chemical engineering, 2017-02, Vol.5 (1), p.1205-1209

2017

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Isothermal Vapor−Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K

Journal of chemical and engineering data, 2011-05, Vol.56 (5), p.1918-1924

2011

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Thermodynamic Study of Mixtures of Compounds Present During the Carbon Dioxide Capture, Transport and Storage

Energy procedia, 2013, Vol.36, p.702-706

2013

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Alkane solubilities in aqueous alkanolamine solutions with CPA EoS

Fluid phase equilibria, 2017-02, Vol.434, p.93-101

2017

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Improvement of the PR-CPA equation of state for modelling of acid gases solubilities in aqueous alkanolamine solutions

Fluid phase equilibria, 2018-09, Vol.471, p.74-87

2018

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CO2 Heat of Absorption in Aqueous Solutions of MDEA and MDEA/Piperazine

Journal of chemical and engineering data, 2020-08, Vol.65 (8), p.3784-3793

2020

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Upcycling cellulose waste textile into aerogel beads via prilling technique

Cellulose (London), 2024-01, Vol.31 (2), p.823-839

2024

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CO 2 Heat of Absorption in Aqueous Solutions of MDEA and MDEA/Piperazine

Journal of chemical and engineering data, 2020-08, Vol.65 (8), p.3784-3793

2020

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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

Journal of chemical and engineering data, 2018-12, Vol.63 (12), p.4626-4631, Article acs.jced.8b00683

2018

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Impact of impurities on CO 2 storage in saline aquifers: Modelling of gases solubility in water

International journal of greenhouse gas control, 2018-01, Vol.68, p.247-255

2018

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Upcycling of textile waste into high added value cellulose porous materials, aerogels and cryogels

RSC sustainability, 2023-03, Vol.1 (2), p.335-345

2023

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Thermodynamic study of the CO 2 -H 2 O -NaCl system: Measurements of CO 2 solubility and modeling of phase equilibria using Soreide and Whitson, electrolyte CPA and SIT models

International journal of greenhouse gas control, 2019-12, Vol.91

2019

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Corrigendum and Comments to “Vapor-liquid equilibrium and molecular simulation data for carbon dioxide (CO2) + trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02 K and pressures up to 7.6 MPa” [Int. J. Refrig. 98 (2019) 362–371]

International journal of refrigeration, 2019-08, Vol.104, p.386-389

2019

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Corrigendum to “Improvement of the PR-CPA equation of state for modelling of acid gases solubilities in aqueous alkanolamine solutions” [Fluid Phase Equilibria, vol. 471, 2018, 74–87]

Fluid phase equilibria, 2019-04, Vol.485, p.126-127

2019

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Corrigendum to "Vapor-liquid equilibrium and molecular simulation data for carbon dioxide (CO 2 ) + trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02 K and pressures up to 7.6MPa"

International journal of refrigeration, 2018-11, Vol.98

2018

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Apparent Henry’s law constants of furan in different n-alkanes and alcohols at temperatures from 293 to 323K

Journal of environmental chemical engineering, 2017-02, Vol.5 (1), p.1205-1209

2017

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An improved static–analytic apparatus for vapor–liquid equilibrium (PTxy) measurement using modified in-situ samplers

Fluid phase equilibria, 2016-02, Vol.409, p.425-433

2016

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Vapour–liquid equilibrium of binary systems containing pentafluorochemicals from 363 to 413 K: Measurement and modelling with Peng–Robinson and three SAFT-like equations of states

International journal of refrigeration, 2012-12, Vol.35 (8), p.2297-2310

2012

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Thermodynamic study of the CO2 – H2O – NaCl system: Measurements of CO2 solubility and modeling of phase equilibria using Soreide and Whitson, electrolyte CPA and SIT models

Excess Molar Volumes and Enthalpies of Binary Mixtures Containing Furan and Toluene, 1-Octanol or n-Hexane at Temperatures Up to 383.15 K and Pressure Up to 1.6 MPa

Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air

Vapor–liquid equilibrium and molecular simulation data for carbon dioxide (CO2) + trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02 K and pressures up to 7.6 MPa

Thermodynamic study of binary systems containing sulphur dioxide and nitric oxide: Measurements and modelling

Apparent Henry’s law constants of furan in different n -alkanes and alcohols at temperatures from 293 to 323 K

Isothermal Vapor−Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K

Thermodynamic Study of Mixtures of Compounds Present During the Carbon Dioxide Capture, Transport and Storage

Simulations of the Impact of Co-injected Gases on CO2 Storage, the SIGARRR Project: Processes and Geochemical Approaches for Gas-water-Salt Interactions Modeling

Role of Impurities on CO2 Injection: Experimental and Numerical Simulations of Thermodynamic Properties of Water-salt-gas Mixtures (CO2 + Co-injected Gases) Under Geological Storage Conditions

Alkane solubilities in aqueous alkanolamine solutions with CPA EoS

Improvement of the PR-CPA equation of state for modelling of acid gases solubilities in aqueous alkanolamine solutions

CO2 Heat of Absorption in Aqueous Solutions of MDEA and MDEA/Piperazine

Upcycling cellulose waste textile into aerogel beads via prilling technique

CO 2 Heat of Absorption in Aqueous Solutions of MDEA and MDEA/Piperazine

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

Impact of impurities on CO 2 storage in saline aquifers: Modelling of gases solubility in water

Upcycling of textile waste into high added value cellulose porous materials, aerogels and cryogels

Thermodynamic study of the CO 2 -H 2 O -NaCl system: Measurements of CO 2 solubility and modeling of phase equilibria using Soreide and Whitson, electrolyte CPA and SIT models

Corrigendum and Comments to “Vapor-liquid equilibrium and molecular simulation data for carbon dioxide (CO2) + trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02 K and pressures up to 7.6 MPa” [Int. J. Refrig. 98 (2019) 362–371]

Corrigendum to “Improvement of the PR-CPA equation of state for modelling of acid gases solubilities in aqueous alkanolamine solutions” [Fluid Phase Equilibria, vol. 471, 2018, 74–87]

Corrigendum to "Vapor-liquid equilibrium and molecular simulation data for carbon dioxide (CO 2 ) + trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02 K and pressures up to 7.6MPa"

Apparent Henry’s law constants of furan in different n-alkanes and alcohols at temperatures from 293 to 323K

An improved static–analytic apparatus for vapor–liquid equilibrium (PTxy) measurement using modified in-situ samplers

Vapour–liquid equilibrium of binary systems containing pentafluorochemicals from 363 to 413 K: Measurement and modelling with Peng–Robinson and three SAFT-like equations of states

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