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Methane and Water Phase Equilibria in the Presence of Single and Mixed Electrolyte Solutions Using the Cubic-Plus-Association Equation of State

Oil & gas science and technology, 2009-03, Vol.64 (2), p.141-154

2009

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Measurement and Modeling of Gas Solubility and Literature Review of the Properties for the Carbon Dioxide−Water System

Industrial & engineering chemistry research, 2004-03, Vol.43 (7), p.1794-1802

2004

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Predicting the Hydrate Stability Zones of Natural Gases Using Artificial Neural Networks

Oil & gas science and technology, 2007-09, Vol.62 (5), p.701-706

2007

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Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa

Fluid phase equilibria, 2003-11, Vol.214 (1), p.101-117

2003

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Development of a New Alpha Function for the Peng–Robinson Equation of State: Comparative Study of Alpha Function Models for Pure Gases (Natural Gas Components) and Water-Gas Systems

International journal of thermophysics, 2004-01, Vol.25 (1)

2004

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Vapor–liquid equilibrium data for the carbon dioxide (CO 2) + difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa

Fluid phase equilibria, 2004-04, Vol.218 (1), p.95-101

2004

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Enhancement of CO2 capture through hydrate formation: the effect of tetrahydrofuran (THF) and tertiary amine solutions

International journal of environmental science and technology (Tehran), 2022-02, Vol.19 (2), p.691-704

2022

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Vapour–liquid equilibria in the carbon dioxide–water system, measurement and modelling from 278.2 to 318.2K

Fluid phase equilibria, 2004-12, Vol.226 (Complete), p.333-344

2004

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A Wet Cold-Flow Technology for Tackling Offshore Flow-Assurance Problems

SPE projects, facilities & construction, 2010-06, Vol.5 (2), p.58-64

2010

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Gas solubility measurement and modeling for methane–water and methane–ethane–n-butane–water systems at low temperature conditions

Fluid phase equilibria, 2004-06, Vol.220 (1), p.113-121

2004

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Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12K and pressures up to 34.5MPa

Fluid phase equilibria, 2003-11, Vol.214 (1), p.101-117

2003

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Mutualiser les pratiques documentaires : Bibliothéques en réseau

Jérôme Pouchol

2016

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Experimental Measurement and Thermodynamic Modeling of Water Content in Methane and Ethane Systems

Industrial & engineering chemistry research, 2004-10, Vol.43 (22), p.7148-7162

2004

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Establishing the Maximum Carbon Number for Reliable Quantitative Gas Chromatographic Analysis of Heavy Ends Hydrocarbons. Part 1: Low-Conversion Thermal Cracking Modeling

Energy & fuels, 2012-05, Vol.26 (5), p.2600-2610

2012

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Measurements and Thermodynamic Modeling of Vapor−Liquid Equilibria in Ethane−Water Systems from 274.26 to 343.08 K

Industrial & engineering chemistry research, 2004-08, Vol.43 (17), p.5418-5424

2004

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Solubility measurement and modeling for the system propane–water from 277.62 to 368.16 K

Fluid phase equilibria, 2004-12, Vol.226, p.213-220

2004

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Experimental Measurement and Phase Behavior Modeling of Hydrogen Sulfide−Water Binary System

Industrial & engineering chemistry research, 2005-09, Vol.44 (19), p.7567-7574

2005

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Phase Equilibrium Properties Aspects of CO2 and Acid Gases Transportation

Cutting‐Edge Technology for Carbon Capture, Utilization, and Storage, 2018, p.147-167

2018

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Speed of Sound Measurements for a CO2 Rich Mixture

Cutting‐Edge Technology for Carbon Capture, Utilization, and Storage, 2018, p.181-185

2018

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Estimation of Water Content for Methane + Water and Methane + Ethane + n-Butane + Water Systems Using a New Sampling Device

Journal of chemical and engineering data, 2005-07, Vol.50 (4), p.1157-1161

2005

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A Semiempirical Approach for Estimating the Water Content of Natural Gases

Industrial & engineering chemistry research, 2004-10, Vol.43 (22), p.7137-7147

2004

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Measurement of the Water Solubility in the Gas Phase of the Ethane + Water Binary System near Hydrate Forming Conditions

Journal of chemical and engineering data, 2003-07, Vol.48 (4), p.957-966

2003

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Experimental Measurement and Phase Behavior Modeling of Hydrogen Sulfide−Water Binary System

Industrial & engineering chemistry research, 2005-12, Vol.44 (26), p.10021-10021

2005

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Developing a Hydrate-Monitoring System

SPE projects, facilities & construction, 2009-03, Vol.4 (1), p.1-6

2009

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Corrigendum to “Revised solubility data and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa” : [Fluid Phase Equilibria 214 (2003) 101–117]

Fluid phase equilibria, 2005, Vol.230 (1), p.210-214

2005

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Methane and Water Phase Equilibria in the Presence of Single and Mixed Electrolyte Solutions Using the Cubic-Plus-Association Equation of State

Measurement and Modeling of Gas Solubility and Literature Review of the Properties for the Carbon Dioxide−Water System

Predicting the Hydrate Stability Zones of Natural Gases Using Artificial Neural Networks

Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa

Development of a New Alpha Function for the Peng–Robinson Equation of State: Comparative Study of Alpha Function Models for Pure Gases (Natural Gas Components) and Water-Gas Systems

Vapor–liquid equilibrium data for the carbon dioxide (CO 2) + difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa

Enhancement of CO2 capture through hydrate formation: the effect of tetrahydrofuran (THF) and tertiary amine solutions

Vapour–liquid equilibria in the carbon dioxide–water system, measurement and modelling from 278.2 to 318.2K

A Wet Cold-Flow Technology for Tackling Offshore Flow-Assurance Problems

Gas solubility measurement and modeling for methane–water and methane–ethane–n-butane–water systems at low temperature conditions

Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12K and pressures up to 34.5MPa

Mutualiser les pratiques documentaires : Bibliothéques en réseau

Experimental Measurement and Thermodynamic Modeling of Water Content in Methane and Ethane Systems

Establishing the Maximum Carbon Number for Reliable Quantitative Gas Chromatographic Analysis of Heavy Ends Hydrocarbons. Part 1: Low-Conversion Thermal Cracking Modeling

Measurements and Thermodynamic Modeling of Vapor−Liquid Equilibria in Ethane−Water Systems from 274.26 to 343.08 K

Solubility measurement and modeling for the system propane–water from 277.62 to 368.16 K

Experimental Measurement and Phase Behavior Modeling of Hydrogen Sulfide−Water Binary System

Phase Equilibrium Properties Aspects of CO2 and Acid Gases Transportation

Speed of Sound Measurements for a CO2 Rich Mixture

Estimation of Water Content for Methane + Water and Methane + Ethane + n-Butane + Water Systems Using a New Sampling Device

A Semiempirical Approach for Estimating the Water Content of Natural Gases

Measurement of the Water Solubility in the Gas Phase of the Ethane + Water Binary System near Hydrate Forming Conditions

Experimental Measurement and Phase Behavior Modeling of Hydrogen Sulfide−Water Binary System

Developing a Hydrate-Monitoring System

Corrigendum to “Revised solubility data and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa” : [Fluid Phase Equilibria 214 (2003) 101–117]

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