(Vapor+liquid) equilibrium data for (carbon dioxide+1,1-difluoroethane) system at temperatures from (258 to 343)K and pressures up to about 8MPa

A Mathematical Model Based on Artificial Neural Network Technique for Estimating Liquid Water−Hydrate Equilibrium of Water−Hydrocarbon System

article

A Semiempirical Approach for Estimating the Water Content of Natural Gases

article

A fundamental equation of state for the (R134a + triethylene glycol dimethyl ether) mixture

A monodisperse thermodynamic model for estimating asphaltene precipitation

article

A novel method for evaluation of asphaltene precipitation titration data

A novel static analytical apparatus for phase equilibrium measurements

A statistical method for evaluation of the experimental phase equilibrium data of simple clathrate hydrates

A “non-linear” quantitative structure–property relationship for the prediction of electrical conductivity of ionic liquids

scholarly article by Farhad Gharagheizi et al published September 2013 in Chemical Engineering Science

Acid gases partial pressures above a 50wt% aqueous methyldiethanolamine solution: Experimental work and modeling

An improved Clapeyron model for predicting liquid water–hydrate–liquid hydrate former phase equilibria

Application of gas hydrate formation in separation processes: A review of experimental studies

article

Artificial Neural Network Modeling of Solubilities of 21 Commonly Used Industrial Solid Compounds in Supercritical Carbon Dioxide

scholarly article by Farhad Gharagheizi et al published 5 January 2011 in Industrial & Engineering Chemistry Research

Artificial Neural Network modeling of solubility of supercritical carbon dioxide in 24 commonly used ionic liquids

scholarly article by Ali Eslamimanesh et al published July 2011 in Chemical Engineering Science

Assessment of clathrate hydrate phase equilibrium data for CO2+CH4/N2+water system

Assessment test for glycol loss in gaseous system

Assessment test of sulfur content of gases

CLATHRATE HYDRATE PHASE EQUILIBRIA FOR CARBONYL SULFIDE, HYDROGEN SULFIDE, ETHYLENE, OR PROPANE + WATER SYSTEM BELOW WATER FREEZING POINT

article by Amir H. Mohammadi & Dominique Richon published 2 December 2013 in Chemical Engineering Communications

Calculation of ir band profiles of diatomic molecules dissolved in liquids

Can Toluene or Xylene Form Clathrate Hydrates?

Chlorofluorohydrocarbon—alcohol mixtures: bubble pressures and saturated liquid molar volumes (experimental data and modeling)

Chrastil-Type Approach for Representation of Glycol Loss in Gaseous System

Clarification of the volumetric properties of the (tetrahydrofuran+water) systems [J. Chem. Thermodyn. 41 (2009) 1382–1386]: Author’s statement

Clathrate Hydrates of Cyclohexane + Hydrogen Sulfide and Cyclohexane + Methane: Experimental Measurements of Dissociation Conditions

Clathrate hydrate dissociation conditions for the methane+cycloheptane/cyclooctane+water and carbon dioxide+cycloheptane/cyclooctane+water systems

article published in 2010

Comment on “Data and prediction of water content of high pressure nitrogen, methane and natural gas” by G.K. Folas, E.W. Froyna, J. Lovland, G.M. Kontogeorgis, E. Solbraa, Fluid Phase Equilib. 252 (2007) 162–174

Comments on “Experimental Measurement of Vapor Pressures and Densities at Saturation of Pure Hexafluoropropylene Oxide: Modeling Using a Crossover Equation of State”

Compositional Analysis and Hydrate Dissociation Conditions Measurements for Carbon Dioxide + Methane + Water System

article

Compositional analysis of the gas phase for the CO2+N2+tetra-n-butylammonium bromide aqueous solution systems under hydrate stability conditions

article

Compressed and Saturated Liquid Densities for the 2-Propanol + Water System

Correction to Corresponding States Method for Determination of the Viscosity of Gases at Atmospheric Pressure

scholarly article published in Industrial & Engineering Chemistry Research

Corresponding States Method for Determination of the Viscosity of Gases at Atmospheric Pressure

Corresponding States Method for Evaluation of the Solubility Parameters of Chemical Compounds

Corrigendum to “Thermodynamic modeling of phase equilibria of semi-clathrate hydrates of CO2, CH4, or N2+tetra-n-butylammonium bromide aqueous solution” [Chem. Eng. Sci. 81 (2012) 319–328]

scholarly article published in Chemical Engineering Science

Corrigendum to “Volumetric properties of the isopropanolamine–water mixture at atmospheric pressure from 283.15 to 353.15 K” [Thermochim. Acta 440 (2006) 122–128]

scholarly article published in Thermochimica Acta

Densities of Water + Diethanolamine + Methanol and Water +N-Methyldiethanolamine + Methanol at Temperatures Ranging from (283.15 to 353.15) K

Design of Equilibrium Cells for Phase Equilibria and PVT Measurements in Large Ranges of Temperatures and Pressures. I. Vapor–Liquid–Liquid Equilibria

Determination of Critical Properties and Acentric Factors of Petroleum Fractions Using Artificial Neural Networks

scholarly article by Amir H. Mohammadi et al published May 2008 in Industrial & Engineering Chemistry Research

Determination of Critical Properties and Acentric Factors of Pure Compounds Using the Artificial Neural Network Group Contribution Algorithm

scholarly article by Farhad Gharagheizi et al published 12 May 2011 in Journal of Chemical & Engineering Data

Determination of Gas Hydrate Safety Margin Using Specific Gravity Data of Salt or Organic Inhibitor Aqueous Solution

article

Determination of Parachor of Various Compounds Using an Artificial Neural Network−Group Contribution Method

scholarly article by Farhad Gharagheizi et al published 4 May 2011 in Industrial & Engineering Chemistry Research

Determination of Sulfur Content of Various Gases Using Chrastil-Type Equations

Determination of Vapor Pressure of Chemical Compounds: A Group Contribution Model for an Extremely Large Database

article

Determination of critical properties of pure and multi-component mixtures using a “dynamic–synthetic” apparatus

Determination of hydrate stability zone using electrical conductivity data of salt aqueous solution

Determination of the normal boiling point of chemical compounds using a quantitative structure–property relationship strategy: Application to a very large dataset

Determining phase diagrams of tetrahydrofuran+methane, carbon dioxide or nitrogen clathrate hydrates using an artificial neural network algorithm

scholarly article by Amir H. Mohammadi et al published November 2010 in Chemical Engineering Science

Development of Predictive Techniques for Estimating Liquid Water-Hydrate Equilibrium of Water-Hydrocarbon System

Development of a LSSVM-GC model for estimating the electrical conductivity of ionic liquids

Development of a general model for determination of thermal conductivity of liquid chemical compounds at atmospheric pressure

Development of a group contribution method for determination of viscosity of ionic liquids at atmospheric pressure

article

Development of a group contribution method for estimating the thermal decomposition temperature of ionic liquids

Development of a quantitative structure–liquid thermal conductivity relationship for pure chemical compounds

article

Development of corresponding states model for estimation of the surface tension of chemical compounds

article

Diagnosis of asphaltene stability in crude oil through “two parameters” SVM model

article

Effect of acid gases on the solubility of n-propylmercaptan in 50wt% methyl-diethanolamine aqueous solution

Effect of solvent molecular structure on vibration—rotation spectra of DCl and CO solutes in cycloalkanes

article

Empirical Method for Representing the Flash-Point Temperature of Pure Compounds

Empirical method for estimation of Henry’s law constant of non-electrolyte organic compounds in water

article

Equilibrium Data for the Oxygen + Propane Binary System at Temperatures of (110.22, 120.13, 130.58, and 139.95) K†

Equilibrium Data of Carbonyl Sulfide and Hydrogen Sulfide Clathrate Hydrates

Equilibrium Data of Methyl Cyclohexane + Hydrogen Sulfide and Methyl Cyclohexane + Methane Clathrate Hydrates

Equilibrium Data of Neohexane + Hydrogen Sulfide and Neohexane + Methane Clathrate Hydrates

article published in 2011

Equilibrium Data of Nitrous Oxide and Carbon Dioxide Clathrate Hydrates†

Equilibrium Data of Sulfur Dioxide and Methyl Mercaptan Clathrate Hydrates

Equilibrium data of (tetrahydropyran+hydrogen sulphide) and (tetrahydropyran+methane) clathrate hydrates

Erratum to “Vapor–liquid equilibrium data for the (hexafluoroethane+1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa” [Fluid Phase Equilib. 268 (2008) 68–73]

scholarly article published in Fluid Phase Equilibria

Erratum: “New equipment and new technique for measuring activity coefficients and Henry's constants at infinite dilution” [Rev. Sci. Instrum. 82, 025108 (2011)]

scholarly article published in Review of Scientific Instruments

Estimating Sulfur Content of Hydrogen Sulfide at Elevated Temperatures and Pressures Using an Artificial Neural Network Algorithm

article

Estimating the Hydrate Safety Margin Using Surface Tension Data of Salt Aqueous Solution

article

Estimating the Hydrate Safety Margin in the Presence of Salt or Organic Inhibitor Using Refractive Index Data of Aqueous Solution

article

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

Evaluation of Thermal Conductivity of Gases at Atmospheric Pressure through a Corresponding States Method

Evaluation of experimental data for wax and diamondoids solubility in gaseous systems

Excess Molar Enthalpies for the Binary and Ternary Mixtures of Cyclohexane, Tetrahydropyran, and 1,4-Dioxane at 308.15 K and Atmospheric Pressure: Experimental Measurements and Correlations†

Excess Molar Enthalpies for the Binary and Ternary Mixtures of Cyclohexane, Tetrahydropyran, and Piperidine at 308.15 K and Atmospheric Pressure: Experimental Measurements and Correlations

Excess molar enthalpies for binary mixtures of 1,2-dichloroethane with ethers at 298.15K and atmospheric pressure

Experimental (vapour+liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene

Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions

Experimental Data Assessment Test for Composition of Vapor Phase in Equilibrium with Gas Hydrate and Liquid Water for Carbon Dioxide + Methane or Nitrogen + Water System

article

Experimental Data Assessment Test for Diamondoids Solubility in Gaseous System

Experimental Data and Predictions of Dissociation Conditions for Ethane and Propane Simple Hydrates in the Presence of Distilled Water and Methane, Ethane, Propane, and Carbon Dioxide Simple Hydrates in the Presence of Ethanol Aqueous Solutions

article by Amir H. Mohammadi et al published January 2008 in Journal of Chemical & Engineering Data

Experimental Data and Predictions of Dissociation Conditions for Ethane and Propane Simple Hydrates in the Presence of Methanol, Ethylene Glycol, and Triethylene Glycol Aqueous Solutions

Experimental Data and Predictions of Dissociation Conditions for Methane, Ethane, Propane, and Carbon Dioxide Simple Hydrates in the Presence of Glycerol Aqueous Solutions

Experimental Gas Hydrate Dissociation Data for Methane, Ethane, and Propane + 2-Propanol Aqueous Solutions and Methane + 1-Propanol Aqueous Solution Systems

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

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

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

Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, 1,4-Dioxane and Piperidine) or (Cyclohexane, Morpholine and Piperidine) at 308.15 K and Atmospheric Pressure

Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, Tetrahydropyran, and Morpholine) or (Cyclohexane, 1,4-Dioxane, and Morpholine) at 308.15 K and Atmospheric Pressure

Experimental Measurements and Predictions of Dissociation Conditions for Carbon Dioxide and Methane Hydrates in the Presence of Triethylene Glycol Aqueous Solutions

Experimental Measurements and Predictions of Dissociation Conditions for Methane, Ethane, Propane, and Carbon Dioxide Simple Hydrates in the Presence of Diethylene Glycol Aqueous Solutions

Experimental Study of Methane Hydrate Phase Equilibrium in the Presence of Polyethylene Glycol-400 Aqueous Solution

Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles

Experimental determination of phase diagram and modeling: Application to refrigerant mixtures

Experimental study and phase equilibrium modeling of systems containing acid gas and glycol

Experimental techniques for the determination of thermophysical properties to enhance chemical processes

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

article published in 2013

Extension of an Artificial Neural Network Algorithm for Estimating Sulfur Content of Sour Gases at Elevated Temperatures and Pressures

article

Fifth International Symposium of the ESIQIE, 29–31 May 2002, Mexico City

Gas Hydrate Formation in Carbon Dioxide + Nitrogen + Water System: Compositional Analysis of Equilibrium Phases

article

Gas Hydrate Phase Equilibrium in Methane + Ethylene Glycol, Diethylene Glycol, or Triethylene Glycol + Water System

Gas Hydrate Phase Equilibrium in Porous Media: Mathematical Modeling and Correlation

Gas Hydrate Phase Equilibrium in the Presence of Ethylene Glycol or Methanol Aqueous Solution

article published in 2010

Gas Solubility Measurement and Modeling for the Nitrogen + Water System from 274.18 K to 363.02 K

Gas Solubility: A Key to Estimating the Water Content of Natural Gases

article

Gas hydrates of methane, ethane, propane, and carbon dioxide in the presence of single NaCl, KCl, and CaCl2 aqueous solutions: Experimental measurements and predictions of dissociation conditions

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

Glycol Loss in a Gaseous System: Thermodynamic Assessment Test of Experimental Solubility Data

Group Contribution-Based Method for Determination of Solubility Parameter of Nonelectrolyte Organic Compounds

article

Group contribution model for determination of molecular diffusivity of non-electrolyte organic compounds in air at ambient conditions

Handling a very large data set for determination of surface tension of chemical compounds using Quantitative Structure–Property Relationship strategy

article by Farhad Gharagheizi et al published November 2011 in Chemical Engineering Science

High-Pressure Vapor−Liquid Equilibria for Ethylene + 4-Methyl-1-pentene and 1-Butene + 1-Hexene

High-Pressure Vapor−Liquid Equilibria of Two Binary Systems: Carbon Dioxide + Cyclohexanol and Carbon Dioxide + Cyclohexanone

High-Pressure Vapor−Liquid Equilibria, Liquid Densities, and Excess Molar Volumes for the Carbon Dioxide + 2-Propanol System from (308.10 to 348.00) K

Hydrate Phase Equilibria of Gaseous Mixtures of Methane + Carbon Dioxide + Hydrogen Sulfide

Hydrate phase equilibria for hydrogen+water and hydrogen+tetrahydrofuran+water systems: Predictions of dissociation conditions using an artificial neural network algorithm

scholarly article by Amir H. Mohammadi & Dominique Richon published May 2010 in Chemical Engineering Science

Hydrate phase equilibria of CO2+N2+aqueous solution of THF, TBAB or TBAF system

Ice–Clathrate Hydrate–Gas Phase Equilibria for Argon + Water and Carbon Dioxide + Water Systems

scholarly article by Amir H. Mohammadi & Dominique Richon published 5 October 2011 in Industrial & Engineering Chemistry Research

Ice−Clathrate Hydrate−Gas Phase Equilibria for Air, Oxygen, Nitrogen, Carbon Monoxide, Methane, or Ethane + Water System†

Isothermal Vapor–Liquid Equilibrium Data for the Butan-2-one + Methanol or Ethanol Systems Using a Static-Analytic Microcell

Isothermal Vapor–Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K

artículo científico publicado en 2012

Isothermal Vapor−Liquid Equilibrium Data for the Hexafluoroethane (R116) + Propane System at Temperatures from (263 to 323) K

Isothermal Vapor−Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K

Isothermal Vapor−Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer

Isothermal method for hydrate studies using a transparent variable volume cell

artículo científico publicado en 2014

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

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

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

Liquid Density Measurements for the Propylene + 2-Propanol + Water System

Liquid Density and Bubble Pressure Measurements for the Propylene + 2-Propanol System

Liquid densities and excess molar volumes for water + diethylene glycolamine, and water, methanol, ethanol, 1-propanol + triethylene glycol binary systems at atmospheric pressure and temperatures in the range of 283.15–363.15 K

Liquid–liquid equilibrium of (water+1-propanol+1-pentanol) system at 298.15 and 323.15K

Measurement of Henry's Law Constants and Infinite Dilution Activity Coefficients of Propyl Mercaptan, Butyl Mercaptan, and Dimethyl Sulfide in Methyldiethanolamine (1) + Water (2) withw1= 0.50 Using a Gas Stripping Technique

Measurement of activity coefficient at infinite dilution for some bio-oil components in water and mass transfer study of bubbles in the dilutor

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

Measurement of vapor–liquid–liquid phase equilibrium—Equipment and results

Measurement through a Gas Stripping Technique of Henry’s Law Constants and Infinite Dilution Activity Coefficients of Propyl Mercaptan, Butyl Mercaptan, and Dimethyl Sulfide in Methyldiethanolamine (1) + Water (2) withw1= 0.25 and 0.35

Methane hydrate phase equilibrium in the presence of NaBr, KBr, CaBr2, K2CO3, and MgCl2 aqueous solutions: Experimental measurements and predictions of dissociation conditions

Methane hydrate phase equilibrium in the presence of salt (NaCl, KCl, or CaCl2)+ethylene glycol or salt (NaCl, KCl, or CaCl2)+methanol aqueous solution: Experimental determination of dissociation condition

Micro-PVT Apparatus Without Mercury

Modeling of gaseous hydrocarbons solubility in aqueous-amine systems by VTPR model

Monodisperse Thermodynamic Model Based on Chemical + Flory–Hüggins Polymer Solution Theories for Predicting Asphaltene Precipitation

Needs of thermodynamic properties measurements and modeling in the frame of new regulations on refrigerants

New Predictive Methods for Estimating the Vaporization Enthalpies of Hydrocarbons and Petroleum Fractions

article

New Solubility Data of Hydrocarbons in Water and Modeling Concerning Vapor−Liquid−Liquid Binary Systems

New Vapor–Liquid–Liquid Equilibrium Data for Ethane and Propane in Alkanolamine Aqueous Solutions

article published in 2013

New Vapor–Liquid–Liquid Equilibrium Solubility Data for iso-Butane, n-Butane, n-Pentane, and n-Hexane in Alkanolamine Aqueous Solutions

New apparatus for simultaneous determination of phase equilibria and rheological properties of fluids at high pressures: Its application to coal pastes studies up to 773 K and 30 MPa

New equipment and new technique for measuring activity coefficients and Henry's constants at infinite dilution ⬇️

artículo científico publicado el 1 de febrero de 2011

On estimating the water content of gas in equilibrium with gas hydrate or ice

article

PHASE EQUILIBRIA OF CLATHRATE HYDRATES IN HYDROGEN SULFIDE + DIETHYLENE GLYCOL OR TRIETHYLENE GLYCOL + WATER SYSTEM

Phase Behavior Modeling of Alkyl Amine + Hydrocarbon and Alkyl Amine + Alcohol Systems Using a Group Contribution Associating Equation of State

Phase Behavior Modeling of Alkyl−Amine + Water Mixtures and Prediction of Alkane Solubilities in Alkanolamine Aqueous Solutions with Group Contribution with Association Equation of State

Phase Equilibria of Clathrate Hydrates of Cyclopentane + Hydrogen Sulfide and Cyclopentane + Methane

Phase Equilibria of Clathrate Hydrates of Ethane + Ethene

Phase Equilibria of Clathrate Hydrates of Methane + n-Propyl Mercaptan or n-Butyl Mercaptan + Water System

Phase Equilibria of Clathrate Hydrates of Tetrahydrofuran + Hydrogen Sulfide and Tetrahydrofuran + Methane

Phase Equilibria of Hydrogen Sulfide Clathrate Hydrates in the Presence of Methanol, Ethanol, NaCl, KCl, or CaCl2Aqueous Solutions

Phase Equilibria of Methane Hydrates in the Presence of Methanol and/or Ethylene Glycol Aqueous Solutions

Phase Equilibria of Methane and Carbon Dioxide Clathrate Hydrates in the Presence of Aqueous Solutions of Tributylmethylphosphonium Methylsulfate Ionic Liquid

Phase Equilibria of Mixtures Containing Glycol andn-Alkane: Experimental Study of Infinite Dilution Activity Coefficients and Modeling Using the Cubic-Plus-Association Equation of State

Phase Equilibria of Mixtures Containing Organic Sulfur Species (OSS) and Water/Hydrocarbons: VLE Measurements and Modeling Using the Cubic-Plus-Association Equation of State

Phase Equilibria of Propane and Ethane Simple Hydrates in the Presence of Methanol or Ethylene Glycol Aqueous Solutions

Phase Equilibria of Semi-Clathrate Hydrates of Tetra-n-butylammonium Bromide + Hydrogen Sulfide and Tetra-n-butylammonium Bromide + Methane

Phase Equilibria of Semiclathrate Hydrates of CO2, N2, CH4, or H2+ Tetra-n-butylammonium Bromide Aqueous Solution

Phase Equilibrium Modeling of Structure H Clathrate Hydrates of Methane + Water “Insoluble” Hydrocarbon Promoter Using Group Contribution-Support Vector Machine Technique

Phase Equilibrium Modeling of Structure H Clathrate Hydrates of Methane + Water “Insoluble” Hydrocarbon Promoter Using QSPR Molecular Approach

Phase behavior of mixture of supercritical CO2+ ionic liquid: Thermodynamic consistency test of experimental data

Phase equilibria of CO2+N2 and CO2+CH4 clathrate hydrates: Experimental measurements and thermodynamic modelling

Phase equilibria of binary clathrate hydrates of nitrogen+cyclopentane/cyclohexane/methyl cyclohexane and ethane+cyclopentane/cyclohexane/methyl cyclohexane

Phase equilibria of clathrate hydrates of carbon disulfide + nitrogen or carbon dioxide + water system

scholarly article by Amir H. Mohammadi & Dominique Richon published March 2013 in Chemical Engineering Science

Phase equilibria of clathrate hydrates of methane+carbon dioxide: New experimental data and predictions

Phase equilibria of clathrate hydrates of methyl cyclopentane, methyl cyclohexane, cyclopentane or cyclohexane+carbon dioxide

Phase equilibria of hydrogen sulfide and carbon dioxide simple hydrates in the presence of methanol, (methanol+NaCl) and (ethylene glycol+NaCl) aqueous solutions

Phase equilibria of hydrogen sulphide clathrate hydrates in the presence of single or mixed salt aqueous solution

Phase equilibria of neohexane/methyl cyclopentane+nitrogen clathrate hydrates

Phase equilibrium data for mixtures involving 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane between 312 and 343K

Phase equilibrium data for the hydrogen sulphide + methane system at temperatures from 186 to 313 K and pressures up to about 14 MPa

Phase equilibrium measurements for semi-clathrate hydrates of the (CO2+N2+tetra-n-butylammonium bromide) aqueous solution system

Phase equilibrium measurements for semi-clathrate hydrates of the (CO2+N2+tetra-n-butylammonium bromide) aqueous solution systems: Part 2

Phase equilibrium modeling of clathrate hydrates of methane, carbon dioxide, nitrogen, and hydrogen+water soluble organic promoters using Support Vector Machine algorithm

Predicting hydrate stability zones of petroleum fluids using sound velocity data of salt aqueous solutions

Pure Component and Binary Vapor−Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane

PρT and VLE for Ethane + Hydrogen Sulfide from (254.05 to 363.21) K at Pressures up to 20 MPa

PρTData for Hydrogen Sulfide + Propane from (263 to 363) K at Pressures up to 40 MPa

QSPR approach for determination of parachor of non-electrolyte organic compounds

article

QSPR molecular approach for representation/prediction of very large vapor pressure dataset

Quantitative structure—property relationship for thermal decomposition temperature of ionic liquids

Reply to “Comment on ‘Group Contribution-Based Method for Determination of Solubility Parameter of Nonelectrolyte Organic Compounds’ and ‘Solubility Parameters of Nonelectrolyte Organic Compounds: Determination Using Quantitative Structure–

article

Representation and Prediction of Molecular Diffusivity of Nonelectrolyte Organic Compounds in Water at Infinite Dilution Using the Artificial Neural Network-Group Contribution Method

article

Representation of hydrogen—hydrocarbon vapour—liquid equilibria and saturated densities at high pressures and temperatures

article published in 1986

Representation/Prediction of Solubilities of Pure Compounds in Water Using Artificial Neural Network−Group Contribution Method

scholarly article by Farhad Gharagheizi et al published 14 April 2011 in Journal of Chemical & Engineering Data

Response to comment on “QSPR approach for determination of parachor of non-electrolyte organic compounds” [Chem. Eng. Sci. 66 (2012) 2959–2967]

scholarly article by Farhad Gharagheizi et al published August 2013 in Chemical Engineering Science

Rheological properties of coal powder + solvent + nitrogen to 653 K for two different coals

Second International Workshop on Thermochemical, Thermodynamic and Transport Properties of Halogenated Hydrocarbons and Mixtures

article published in 2002

Semi-clathrate hydrate phase equilibrium measurements for the CO2+H2/CH4+tetra-n-butylammonium bromide aqueous solution system

scholarly article by Amir H. Mohammadi et al published May 2013 in Chemical Engineering Science

Semiempirical Method for Determining Water Content of Methane-Rich Hydrocarbon Gas in Equilibrium with Gas Hydrates

Solubilities of ferrocene and acetylferrocene in supercritical carbon dioxide

Solubility Parameters of Nonelectrolyte Organic Compounds: Determination Using Quantitative Structure–Property Relationship Strategy

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

Solubility of carbon monoxide in bio-oil compounds

Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS)

Solubility of hydrogen in bio-oil compounds

Spectroscopic studies of liquid alkanes using DCl as a molecular probe

Study of Gas Hydrate Formation in the Carbon Dioxide + Hydrogen + Water Systems: Compositional Analysis of the Gas Phase

article

The essential importance of experimental research and the use of experimental thermodynamics to the benefit of industry

Thermodynamic Consistency Test for Experimental Data of Sulfur Content of Hydrogen Sulfide

article published in 2011

Thermodynamic Consistency Test for Experimental Solubility Data in Carbon Dioxide/Methane + Water System Inside and Outside Gas Hydrate Formation Region

Thermodynamic Model for Predicting Liquid Water−Hydrate Equilibrium of the Water−Hydrocarbon System

article

Thermodynamic Modeling of Salt Precipitation and Gas Hydrate Inhibition Effect of Salt Aqueous Solution

Thermodynamic behavior of the CO2+SO2 mixture: Experimental and Monte Carlo simulation studies

article published in 2009

Thermodynamic consistency test for experimental data of water content of methane

Thermodynamic model for predicting phase equilibria of simple clathrate hydrates of refrigerants

Thermodynamic modeling of phase equilibria of semi-clathrate hydrates of CO2, CH4, or N2+tetra-n-butylammonium bromide aqueous solution

Thermodynamic stability conditions of clathrate hydrates for refrigerant (R134a or R410a or R507) with MgCl 2 aqueous solution

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

article published in 2011

Use of Artificial Neural Network-Group Contribution Method to Determine Surface Tension of Pure Compounds

scholarly article by Farhad Gharagheizi et al published 12 May 2011 in Journal of Chemical & Engineering Data

Use of Artificial Neural Networks for Estimating Water Content of Natural Gases

article

Use of Boiling Point Elevation Data of Aqueous Solutions for Estimating Hydrate Stability Zone

article

Use of an Artificial Neural Network Algorithm To Determine Pressure−Temperature Phase Diagrams oftert-Butylamine + Methane andtert-Butylamine + Hydrogen Binary Hydrates

scholarly article by Amir H. Mohammadi & Dominique Richon published 20 October 2010 in Industrial & Engineering Chemistry Research

Use of an artificial neural network algorithm to predict hydrate dissociation conditions for hydrogen+water and hydrogen+tetra-n-butyl ammonium bromide+water systems

scholarly article by Amir H. Mohammadi et al published July 2010 in Chemical Engineering Science

Useful Remarks To Reduce the Experimental Information Required To Determine the Equilibrium Water Content of Gas Near and Inside Gas Hydrate or Ice Formation Regions

VII Iberoamerican conference on phase equilibria and fluid properties for process design

Vapor-liquid Equilibrium Data Concerning Refrigerant Systems (R116 + R143a)

Vapor-liquid equilibrium data for the propane-methanol and propane-methanol-carbon dioxide system

Vapor-liquid equilibrium measurements up to 558 K and 7 MPa: a new apparatus

Vapor–Liquid Equilibrium Data for the Sulfur Dioxide (SO2) + Difluoromethane (R32) System at Temperatures from 288.07 to 403.16 K and at Pressures up to 7.31 MPa

Vapor–Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System

Vapor–Liquid Equilibrium of Methane with Water and Methanol. Measurements and Modeling

Vapor–liquid equilibria of the (hexafluoroethane+1,1,1-trifluoroethane) binary system from 258 to 343K up to 3.89MPa

Vapor–liquid equilibrium data and critical points for the system H2S+COS. Extension of the PSRK group contribution equation of state

Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa

Vapor–liquid equilibrium data for the carbon dioxide (CO2) + difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa

Vapor–liquid equilibrium data for the difluoromethane (R32)–dimethyl ether (RE170) system at temperatures from 283.03 to 363.21K and pressures up to 5.5MPa

Vapor–liquid equilibrium data for the hexafluoroethane+carbon dioxide system at temperatures from 253 to 297K and pressures up to 6.5MPa

Vapor–liquid equilibrium in the n-butane+methanol system, measurement and modeling from 323.2 to 443.2K

Vapor–liquid equilibrium measurements and modeling of the n-butane+ethanol system from 323 to 423K

Vapor−Liquid Equilibrium Data for the Azeotropic Difluoromethane + Propane System at Temperatures from 294.83 to 343.26 K and Pressures up to 5.4 MPa

Vapor−Liquid Equilibrium Measurements and Modeling for Cyclohexane + Cyclohexanone†

Vapor−Liquid Equilibrium Measurements and Modeling of the Propyl Mercaptan + Methane + Water System

Vapour-liquid equilibria hydrogen-white oil up to 625.1 K and 35 MPa

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

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Vapour–liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a)+dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3MPa

Vapour–liquid equilibrium data for the hydrogen sulphide+n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa

Vibration—Rotation spectra of DCl in hexadecane solvents of different molecular shapes

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Vibration—rotation spectra of CO in liquid alkanes

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Volumetric Properties of Mono-, Di-, Tri-, and Polyethylene Glycol Aqueous Solutions from (273.15 to 363.15) K: Experimental Measurements and Correlations

Volumetric Properties of Water + Monoethanolamine + Methanol Mixtures at Atmospheric Pressure from 283.15 to 353.15 K

Volumetric properties of (piperidine+water) binary system: Measurements and modeling

Volumetric properties of hexamethyleneimine and of its mixtures with water

Volumetric properties of the (tetrahydrofuran+water) and (tetra-n-butyl ammonium bromide+water) systems: Experimental measurements and correlations

Volumetric properties of the boldine+alcohol mixtures at atmospheric pressure from 283.15 to 333.15K

Volumetric properties of the isopropanolamine–water mixture at atmospheric pressure from 283.15 to 353.15K

Volumetric properties of the monoethanolamine–methanol mixture at atmospheric pressure from 283.15 to 353.15K

Volumetric properties of the water+3-(dimethylamino) propylamine (DMAPA) mixture at atmospheric pressure from 283.15 to 353.15K

Volumetric properties of the water+ethylenediamine mixture at atmospheric pressure from 288.15 to 353.15K

Water Content Measurement and Modeling in the Nitrogen + Water System

Wax Solubility in Gaseous System: Thermodynamic Consistency Test of Experimental Data

article published in 2011

p−T−xMeasurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)

“Vapor–liquid” equilibrium measurements and modeling for the cyclohexane+cyclohexanol binary system

“Vapor–liquid” equilibrium measurements and modeling for the cyclohexane+n-hexanoic acid binary system