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Application of the Cubic-Plus-Association (CPA) Equation of State to Cross-Associating Systems

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Outgoing claims: the papers this work cites, builds on, or argues with.

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Prediction of thermodynamic properties of polar mixtures by a group solution model
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(Liquid + liquid) equilibria of (octan-1-ol + water) at temperatures from 288.15 K to 323.15 K
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Thermodynamic properties of aqueous non-electrolyte mixtures II. Vapour pressures and excess Gibbs energies for water + ethanol at 303.15 to 363.15 K determined by an accurate static method
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(Solid + liquid) phase equilibria and solid-hydrate formation in water + methyl, + ethyl, + isopropyl, and + tertiary butyl alcohols
inferredcites →https://doi.org/10.1016/0021-9614(88)90081-xopenalex-snapshot
Excess Gibbs free energies of (n-hexane + propan-1-ol) at 338.15 and 348.15 K and of (n-hexane + propan-2-ol) at 323.15, 338.15, and 348.15 K
inferredcites →https://doi.org/10.1016/0022-2860(92)85083-sopenalex-snapshot
CRC Handbook of Chemistry and Physics
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Vapour-liquid equilibrium and solid-solid equilibrium in the system formed by octan-1-ol and n-decane: measurement and calculation
inferredcites →https://doi.org/10.1016/0378-3812(88)80010-4openalex-snapshot
Vapour—liquid equilibria in the heptane - 1-pentanol and heptane - 3-methyl-1-butanol systems at 75, 85 and 95 °C
inferredcites →https://doi.org/10.1016/0378-3812(88)80073-6openalex-snapshot
Vapor—liquid equilibria of 2-propanol + water + N,N-dimethyl formamide
inferredcites →https://doi.org/10.1016/0378-3812(93)85129-aopenalex-snapshot
Phase equilibrium study for the separation of ethanol-water solution using subcritical and supercritical hydrocarbon solvent extraction
inferredcites →https://doi.org/10.1016/0378-3812(93)87018-vopenalex-snapshot
Vapor liquid equilibria in ternary mixtures of water-aloohol-non polar gases
inferredcites →https://doi.org/10.1016/0378-3812(95)02947-8openalex-snapshot
Solid - liquid phase diagram for ethylene glycol + water
inferredcites →https://doi.org/10.1016/j.fluid.2004.05.006openalex-snapshot
Liquid–liquid equilibrium data for binary alcohol + n-alkane (C10–C16) systems: methanol + decane, ethanol + tetradecane, and ethanol + hexadecane
inferredcites →https://doi.org/10.1016/s0021-9614(72)80015-6openalex-snapshot
Solid-liquid phase equilibria in water + ethylene glycol
inferredcites →https://doi.org/10.1016/s0378-3812(96)03200-1openalex-snapshot
Vapor-liquid equilibria for systems using the CPA Equation of state
inferredcites →https://doi.org/10.1016/s0378-3812(99)00060-6openalex-snapshot
Multicomponent phase equilibrium calculations for water–methanol–alkane mixtures
inferredcites →https://doi.org/10.1016/s0378-3812(99)00131-4openalex-snapshot
Prediction of phase equilibria in water/alcohol/alkane systems
inferredcites →https://doi.org/10.1021/ie00012a025openalex-snapshot
Multiphase equilibrium analysis via a generalized equation of state for associating mixtures
inferredcites →https://doi.org/10.1021/ie00107a014openalex-snapshot
Equation of state for small, large, polydisperse, and associating molecules
inferredcites →https://doi.org/10.1021/ie0206103openalex-snapshot
Extension of the Cubic-Plus-Association Equation of State to Glycol−Water Cross-Associating Systems
inferredcites →https://doi.org/10.1021/ie50412a024openalex-snapshot
Phase Equilibria in Hydrocarbon Systems. n-Butane–Water System in Three-Phase Region
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Phase Equilibria in Hydrocarbon Systems. n-Butane-Water System in the Two-Phase Region.
inferredcites →https://doi.org/10.1021/ie9600203openalex-snapshot
An Equation of State for Associating Fluids
inferredcites →https://doi.org/10.1021/ja01056a003openalex-snapshot
Vapor-Liquid Equilibrium. XII. The System Ethanol-Cyclohexane from 5 to 65°
inferredcites →https://doi.org/10.1021/ja01185a038openalex-snapshot
Densities and Liquid—Vapor Equilibria of the System Ethanol—Isoöctane (2,2,4-Trimethylpentane) between 0 and 50°
inferredcites →https://doi.org/10.1021/je00014a005openalex-snapshot
Isothermal Vapor-Liquid Equilibrium Data for the Binaries Isobutane-Ethanol, Isobutane-1-Propanol, and Propane-Ethanol
inferredcites →https://doi.org/10.1021/je00019a033openalex-snapshot
Isothermal Vapor-Liquid Equilibria for Methanol + Ethanol + Water, Methanol + Water, and Ethanol + Water
inferredcites →https://doi.org/10.1021/je0002989openalex-snapshot
Solid−Liquid Equilibria for Seven Binary Systems
inferredcites →https://doi.org/10.1021/je60002a003openalex-snapshot
Vapor-Liquid Equilibrium at High Pressures. The Systems Ethanol-Water and 2-Propanol-Water.
inferredcites →https://doi.org/10.1021/je60022a017openalex-snapshot
Solid-Liquid Phase Diagram of the System Methanol-Water.
inferredcites →https://doi.org/10.1021/je60056a011openalex-snapshot
Excess Gibbs free energies for binary systems. Isopropyl alcohol with benzene, cyclohexane, methylcyclohexane
inferredcites →https://doi.org/10.1021/je9700683openalex-snapshot
Solid−Liquid Equilibria of Viscous Binary Mixtures with Alcohols
inferredcites →https://doi.org/10.1023/a:1005110719402openalex-snapshot
Liquid–Solid Phase Diagrams of PrOH–Water and BuOH–Water Systems from Differential Scanning Calorimetry
inferredcites →https://doi.org/10.1039/ft9959100273openalex-snapshot
Vapour-liquid equilibrium of the ethanol–propanal system
inferredcites →https://doi.org/10.1039/jr9330000674openalex-snapshot
173. The free energy of the normal aliphatic alcohols in aqueous solution. Part I. The partial vapour pressures of aqueous solutions of methyl, n-propyl, and n-butyl alcohols. Part II. The solubilities of some normal aliphatic alcohols in water. Part III. The theory of binary solutions, and its…
inferredcites →https://doi.org/10.1071/ch9792353openalex-snapshot
Vapour Pressure Study of Deuterium Exchange Reactions in Water-Ethanol Systems: Equilibrium Constant Determination
inferredcites →https://doi.org/10.1088/0031-9112/19/12/023openalex-snapshot
Physical Properties of Molecular Crystals, Liquids and Glasses
inferredcites →https://doi.org/10.1252/jcej.26.482openalex-snapshot
Phase Equilibrium Model for the Separation of Ethanol-waler Solution Using Super- and Subcritical Propane Solvent Extraction.
inferredcites →https://doi.org/10.1252/jcej.8.492openalex-snapshot
TERNARY LIQUID-LIQUID EQUILIBRIA FOR THE SYSTEMS OF AQUEOUS METHANOL SOLUTIONS AND PROPANE OR n-BUTANE
inferredcites →https://doi.org/10.1515/zpch-1977-258123openalex-snapshot
Die Beeinflußbarkeit des Dampf-Flüssigkeits-Gleichgewichtsverhaltens n-Propanol / Wasser durch Harnstoff bei 60 °C
inferredcites →https://doi.org/10.1524/zpch.1995.189.part_1.081openalex-snapshot
Mixing Properties of the Liquid System 2-Propanol + Cyclohexane

What points at this work

Incoming claims: where this work appears in other papers’ reference lists and arguments.

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Applications of CPA to the Oil and Gas Industry
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Applications of CPA to Chemical Industries
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The Cubic‐Plus‐Association Equation of State
inferred← citeshttps://doi.org/10.1002/aic.11766openalex-snapshot
Description of the mutual solubilities of fatty acids and water with the CPA EoS
inferred← citeshttps://doi.org/10.1002/aic.18451openalex-snapshot
An efficient polar cubic equation of state for predictive modeling of phase behavior and critical phenomena of mixtures
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Thermodynamic Modeling of CO2-Rich Natural Gas Fluid Systems
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Recovery of Thermodynamic Hydrate Inhibitors with Supersonic Separators in Offshore Processing of Natural Gas: The Cases of Methanol, Ethanol, and Monoethylene Glycol
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Phase Equilibrium
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Experiments, Correlation, and Modeling of Curcumin Solubility in Subcritical Water (Water/Ethanol)
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Modeling Interfacial Tension of Hexane $$+$$ Alcohol Mixtures at Different Temperatures Using Linear Gradient Theory with Cubic Plus Association Equation of State
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Investigation on the Surface Tension and Viscosity of (dimethylsulfoxide + alcohol) Mixtures by Using Gradient Theory and Eyring’s Rate Theory
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Modeling Interfacial Tension of Heptane + Alcohol Mixtures Using Cubic Plus Association Equation of State Plus Simplified Gradient Theory
inferred← citeshttps://doi.org/10.1007/s10765-022-03131-9openalex-snapshot
The Thermodynamic Properties of Non-Associating and Associating Fluids: A Systematic Evaluation of SAFT-Type Equations of State
inferred← citeshttps://doi.org/10.1007/s10953-015-0361-xopenalex-snapshot
Solubility of Carbon Dioxide in Secondary Butyl Alcohol at High Pressures: Experimental and Modeling with CPA
inferred← citeshttps://doi.org/10.1007/s10953-026-01656-3openalex-snapshot
Modeling the Excess Molar Volumes of Six (Monoethanolamine+Alcohol) Mixtures: The influence of Equation of State, Association Scheme and Cross Association Energy on the Accuracy of the Estimations
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Thermodynamic modeling of PVTx properties for several water/hydrocarbon systems in near-critical and supercritical conditions
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Modeling the viscosity of (water + methanol), (water + ethanol), (water + 1-propanol) and (water + 2-propanol) mixture up to the high pressures
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Phase equilibria modeling of cross-associating systems guided by a quantum chemical multi-conformational framework
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On the predictive capabilities of CPA for applications in the chemical industry: Multicomponent mixtures containing methyl-methacrylate, dimethyl-ether or acetic acid
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Sustainable offshore natural gas processing with thermodynamic gas-hydrate inhibitor reclamation: Supersonic separation affords carbon capture
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Methane solubility in ionic liquids: Comparison of cubic-plus-association and modified Sanchez-Lacombe equation of states
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A unified approach for description of gas hydrate formation kinetics in the presence of kinetic promoters in gas hydrate converters
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Advances on modeling and simulation of alcoholic distillation. Part 1: Thermodynamic modeling
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Thermodynamic modeling of the vapor–liquid equilibrium of the water/ethanol/CO2 system
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Vapor–liquid, liquid–liquid and vapor–liquid–liquid equilibrium of binary and multicomponent systems with MEG
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High-pressure vapor–liquid equilibria of systems containing ethylene glycol, water and methane
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Data and prediction of water content of high pressure nitrogen, methane and natural gas
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Measurement and modelling of hydrogen bonding in 1-alkanol+n-alkane binary mixtures
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Modeling phase equilibria of alkanols with the simplified PC-SAFT equation of state and generalized pure compound parameters
inferred← citeshttps://doi.org/10.1016/j.fluid.2007.05.023openalex-snapshot
Mutual solubilities of hydrocarbons and water with the CPA EoS
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Modeling of solid–liquid equilibria for systems with solid-complex phase formation
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Surface tension of chain molecules through a combination of the gradient theory with the CPA EoS
inferred← citeshttps://doi.org/10.1016/j.fluid.2008.10.007openalex-snapshot
Application of the CPA equation of state to reservoir fluids in presence of water and polar chemicals
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Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
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Phase equilibria modeling of methanol-containing systems with the CPA and sPC-SAFT equations of state
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Solid–liquid equilibria for binary and ternary systems with the Cubic-Plus-Association (CPA) equation of state
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The Cubic-Two-State Equation of State: Cross-associating mixtures and Monte Carlo study of self-associating prototypes
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Towards predictive association theories
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Application of association models to mixtures containing alkanolamines
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Distribution of MEG and methanol in well-defined hydrocarbon and water systems: Experimental measurement and modeling using the CPA EoS
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Thermodynamic model for process design, simulation and optimization in the production of biodiesel
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The role of monomer fraction data in association theories—Can we improve the performance for phase equilibrium calculations?
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Measurement of vapor–liquid–liquid phase equilibrium—Equipment and results
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Experimental measurements and modelling of carbon dioxide hydrate phase equilibrium with and without ethanol
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Review and new insights into the application of molecular-based equations of state to water and aqueous solutions
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Pitfalls of using the geometric-mean combining rule in the density gradient theory
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A density gradient theory based method for surface tension calculations
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Re-evaluating the CPA EoS for improving critical points and derivative properties description
inferred← citeshttps://doi.org/10.1016/j.fluid.2017.07.021openalex-snapshot
General approach for solving the density gradient theory in the interfacial tension calculations
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Modeling surface tension and interface of (water+methanol), (water+ethanol), (water+1-propanol), and (water+MEG) mixtures
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eCPA: An ion-specific approach to parametrization
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Applying the Patel-Teja EoS with regular solution theory to predict the onset of asphaltene precipitation
inferred← citeshttps://doi.org/10.1016/j.fluid.2018.10.020openalex-snapshot
Prediction of solid solute solubility in supercritical CO2 with cosolvents using the CPA EoS
inferred← citeshttps://doi.org/10.1016/j.fluid.2018.11.003openalex-snapshot
Accounting for cross association in non-self-associating species using a physically consistent SAFT-VR Mie approach
inferred← citeshttps://doi.org/10.1016/j.fluid.2019.112365openalex-snapshot
Renormalization group theory applied to the CPA equation of state: Impacts on phase equilibrium and derivative properties
inferred← citeshttps://doi.org/10.1016/j.fluid.2020.112557openalex-snapshot
Evaluation of different thermodynamic models in predicting asphaltene precipitation: A comparative study
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Xylitol solubility in DMF + ethylene glycol or 1,2-propylene glycol: Measurement and modeling with PC-SAFT and CPA equations of state and UNIFAC activity coefficient model
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Thermodynamic modeling of CO2 solubility in saline water using NVT flash with the cubic-Plus-association equation of state
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Accounting for quadrupolar interactions in the CPA equation of state: A modelling approach for binary mixtures of CO2 or benzene with n-alkanes and 1-alkanols
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Towards a predictive Cubic Plus Association equation of state
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Natural gas hydrate stability conditions and water activity in aqueous solutions containing mono ethylene glycol (MEG) and salt: Experimental measurements and thermodynamic modeling
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Thermodynamic modelling of industrially important associating mixtures with a group-contribution equation of state
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Patel-Teja cubic equation of state – A review of modifications and applications till 2022
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Dew pressure point and liquid dropout of CH4 + alcohol (methanol or ethanol) system with high gas content at high-pressure and high-temperature
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Ethane (1) -Water (2) Solubility Modeling and New Water Content Measurements of Liquid Ethane in Equilibrium with Water and Hydrates
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Modelling thermophysical properties of mixtures of 2-hydroxyethyl ammonium-based ionic liquids + water, methanol, or ethanol with the electrolyte-cubic plus association equation of state
inferred← citeshttps://doi.org/10.1016/j.fluid.2024.114100openalex-snapshot
Molecular dynamics simulation of methane hydrates: Prediction of the phase equilibria using extracted microscopic parameters from SAFT-VR Mie EOS
inferred← citeshttps://doi.org/10.1016/j.fluid.2024.114114openalex-snapshot
Solubility measurement of methane in triethylene glycol aqueous solutions (90,95,98 wt.% triethylene glycol) from 298 to 323 K and 0.17 to 2.5 MPa
inferred← citeshttps://doi.org/10.1016/j.fluid.2024.114131openalex-snapshot
Cubic-two-state equation of state for modeling liquid-liquid and vapor-liquid equilibria of nitriles + hydrocarbons or water mixtures
inferred← citeshttps://doi.org/10.1016/j.fluid.2024.114219openalex-snapshot
Prediction of solubility of CO2, H2S, and their mixture in ionic liquids using the Cubic Two State equation of state
inferred← citeshttps://doi.org/10.1016/j.fluid.2025.114338openalex-snapshot
Study of surface tension of CO2+water and CO2+ethanol solutions from combined CPA and PC-SAFT EoSs with gradient theory and artificial neural network
inferred← citeshttps://doi.org/10.1016/j.fluid.2026.114877openalex-snapshot
Locally constrained optimization of PC-SAFT parameters for reliable restricted group contribution calculations for associating fluids
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Liquid–liquid equilibria for the canola oil biodiesel + ethanol + glycerol system
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Modeling of asphaltene precipitation utilizing Association Equation of State
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Liquid–liquid equilibria for ternary systems containing ethyl esters, ethanol and glycerol at 323.15 and 353.15K
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Liquid–liquid equilibria for ethyl esters+ethanol+water systems: Experimental measurements and CPA EoS modeling
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Prediction of asphaltene phase behavior in live oil with CPA equation of state
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Density prediction of CO2–hydrocarbon mixtures using an extensive databank: Comparison of interpretable machine learning models with cubic and association-based EoSs
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A comprehensive thermodynamic study of heat stable acetic acid salt of monoethanolamine
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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
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Extension of the new proposed association equation of state (AEOS) to associating fluid mixtures
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Experimental measurement and thermodynamic modelling of phase equilibria of semi-clathrate hydrates of (CO2+ tetra-n-butyl-ammonium bromide) aqueous solution
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Prediction of vapor-liquid-hydrate equilibrium conditions for single and mixed guest hydrates with the SAFT-VR Mie EOS
inferred← citeshttps://doi.org/10.1016/j.jct.2020.106336openalex-snapshot
Solubility of H2S in ammonium-based ionic liquids
inferred← citeshttps://doi.org/10.1016/j.jct.2022.106762openalex-snapshot
Density, speed of sound, refractive index of binary mixtures containing 2-ethoxyethanol and some alcohols: Measurement and correlation
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Economic leverage affords post-combustion capture of 43% of carbon emissions: Supersonic separators for methanol hydrate inhibitor recovery from raw natural gas and CO2 drying
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Solubility of fructose and sucrose in mixtures of methanol and water: Experiment and application of equations of state and activity coefficient model
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Water vapour monitoring in natural gas in the presence of methanol
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Recovery of thermodynamic hydrate inhibitors methanol, ethanol and MEG with supersonic separators in offshore natural gas processing
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Carbon capture and high-capacity supercritical fluid processing with supersonic separator: Natural gas with ultra-high CO2 content
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Modeling the equilibrium of two and three-phase systems including water, alcohol, and hydrocarbons with CPA EOS and its improvement for electrolytic systems by Debye-Huckel equation
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Support vector machine and CPA EoS for the prediction of high-pressure liquid densities of normal alkanols
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Comments on “Prediction of the surface tension of binary liquid mixtures of associating compounds using the Cubic Plus Association (CPA) equation of state”
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Calculation of complex phase equilibria of DMF/alkane and acetonitrile/alkane systems using a modified Peng-Robinson EoS and the Huron-Vidal mixing rules
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Modeling the liquid-liquid equilibria of polar aprotic solvents/alkanes type mixtures using a modified PR EoS and the Huron-Vidal mixing rules
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Unraveling hydrate stoichiometry in water/alkyl alcohol systems by thermodynamic modeling
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Evaluation of the CO2 behavior in binary mixtures with alkanes, alcohols, acids and esters using the Cubic-Plus-Association Equation of State
inferred← citeshttps://doi.org/10.1016/j.supflu.2013.09.016openalex-snapshot
Vapor–liquid equilibria of isopropyl alcohol+propylene at high pressures: Experimental measurement and modeling with the CPA EoS
inferred← citeshttps://doi.org/10.1016/j.supflu.2018.04.008openalex-snapshot
Solubility of caffeic acid in CO2 + ethanol: Experimental and predicted data using Cubic Plus Association Equation of State
inferred← citeshttps://doi.org/10.1021/acs.cgd.5b00735openalex-snapshot
Thermodynamic Modeling for Efficient Cocrystal Formation
inferred← citeshttps://doi.org/10.1021/acs.cgd.6b00024openalex-snapshot
Predicting the Aqueous Solubility of Pharmaceutical Cocrystals As a Function of pH and Temperature
inferred← citeshttps://doi.org/10.1021/acs.cgd.6b00554openalex-snapshot
Polymorphs, Hydrates, Cocrystals, and Cocrystal Hydrates: Thermodynamic Modeling of Theophylline Systems
inferred← citeshttps://doi.org/10.1021/acs.cgd.6b00664openalex-snapshot
Predicting the Effect of pH on Stability and Solubility of Polymorphs, Hydrates, and Cocrystals
inferred← citeshttps://doi.org/10.1021/acs.iecr.5b01410openalex-snapshot
Cubic Plus Association Equation of State for Flow Assurance Projects
inferred← citeshttps://doi.org/10.1021/acs.iecr.6b00747openalex-snapshot
Development of a Full CO2 Capture Process Based on the Rectisol Wash Technology
inferred← citeshttps://doi.org/10.1021/acs.iecr.7b00899openalex-snapshot
Predicting the Solvation of Organic Compounds in Aqueous Environments: From Alkanes and Alcohols to Pharmaceuticals
inferred← citeshttps://doi.org/10.1021/acs.iecr.7b03522openalex-snapshot
Improved Prediction of Water Properties and Phase Equilibria with a Modified Cubic Plus Association Equation of State
inferred← citeshttps://doi.org/10.1021/acs.iecr.8b03799openalex-snapshot
Heterosegmental Modeling of Long-Chain Molecules and Related Mixtures using PC-SAFT: 1. Polar Compounds
inferred← citeshttps://doi.org/10.1021/acs.iecr.9b00157openalex-snapshot
Heterosegmental Modeling of Long-Chain Molecules and Related Mixtures Using PC-SAFT: 2. Associating Compounds
inferred← citeshttps://doi.org/10.1021/acs.iecr.9b05367openalex-snapshot
Solubility and Pseudo Polymorphic Behavior of Nicotinic Acid in Alcoholic Solutions: Experimental Data and Phase Equilibrium Modeling
inferred← citeshttps://doi.org/10.1021/acs.jced.1c00131openalex-snapshot
Measurements and Modeling of Physicochemical Properties of Pure and Binary Mixtures Containing 1,2-Dimethoxyethane and Some Alcohols
inferred← citeshttps://doi.org/10.1021/acs.jced.9b00312openalex-snapshot
Loss of Methanol and Monoethylene Glycol in VLE and LLE: Prediction of Hydrate Inhibitor Partition
inferred← citeshttps://doi.org/10.1021/acs.jpcb.3c01058openalex-snapshot
Multipolar SAFT-VR Mie Equation of State: Predictions of Phase Equilibria in Refrigerant Systems with No Binary Interaction Parameter
inferred← citeshttps://doi.org/10.1021/ef502129popenalex-snapshot
Comparison of Cubic-Plus-Association and Perturbed-Chain Statistical Associating Fluid Theory Methods for Modeling Asphaltene Phase Behavior and Pressure–Volume–Temperature Properties
inferred← citeshttps://doi.org/10.1021/ie0509241openalex-snapshot
Application of the Cubic-Plus-Association Equation of State to Mixtures with Polar Chemicals and High Pressures
inferred← citeshttps://doi.org/10.1021/ie050976qopenalex-snapshot
Application of the Cubic-Plus-Association (CPA) Equation of State to Complex Mixtures with Aromatic Hydrocarbons
inferred← citeshttps://doi.org/10.1021/ie051305vopenalex-snapshot
Ten Years with the CPA (Cubic-Plus-Association) Equation of State. Part 1. Pure Compounds and Self-Associating Systems
inferred← citeshttps://doi.org/10.1021/ie051306nopenalex-snapshot
Ten Years with the CPA (Cubic-Plus-Association) Equation of State. Part 2. Cross-Associating and Multicomponent Systems
inferred← citeshttps://doi.org/10.1021/ie051341uopenalex-snapshot
Investigating Models for Associating Fluids Using Spectroscopy
inferred← citeshttps://doi.org/10.1021/ie060313oopenalex-snapshot
Evaluation of the Truncated Perturbed Chain-Polar Statistical Associating Fluid Theory for Complex Mixture Fluid Phase Equilibria
inferred← citeshttps://doi.org/10.1021/ie061147nopenalex-snapshot
Modeling the Liquid−Liquid Equilibria of Water + Fluorocarbons with the Cubic-Plus-Association Equation of State
inferred← citeshttps://doi.org/10.1021/ie071397jopenalex-snapshot
Cubic Two-State Equation of State for Associating Fluids
inferred← citeshttps://doi.org/10.1021/ie101611jopenalex-snapshot
Liquid−Liquid Equilibrium for Ternary Systems Containing Ethyl Esters, Anhydrous Ethanol and Water at 298.15, 313.15, and 333.15 K
inferred← citeshttps://doi.org/10.1021/ie102045gopenalex-snapshot
Modeling Liquid–Liquid and Liquid–Vapor Equilibria of Binary Systems Containing Water with an Alkane, an Aromatic Hydrocarbon, an Alcohol or a Gas (Methane, Ethane, CO2 or H2S), Using Group Contribution Polar Perturbed-Chain Statistical Associating Fluid Theory
inferred← citeshttps://doi.org/10.1021/ie200521kopenalex-snapshot
New Association Scheme for 1-Alcohols in Alcohol/Water Mixtures with sPC-SAFT: The 2C Association Scheme
inferred← citeshttps://doi.org/10.1021/ie301388dopenalex-snapshot
Capabilities and Limitations of an Association Theory for Chemicals in Liquid or Supercritical Solvents
inferred← citeshttps://doi.org/10.1021/ie302144topenalex-snapshot
Potential Theory of Adsorption for Associating Mixtures: Possibilities and Limitations
inferred← citeshttps://doi.org/10.1021/ie501993yopenalex-snapshot
Modeling Water Containing Systems with the Simplified PC-SAFT and CPA Equations of State
inferred← citeshttps://doi.org/10.1021/ie800040gopenalex-snapshot
Modeling Systems Containing Alkanolamines with the CPA Equation of State
inferred← citeshttps://doi.org/10.1021/ie800689fopenalex-snapshot
Extension of the Elliott−Suresh−Donohue Equation of State to Dipolar Systems
inferred← citeshttps://doi.org/10.1021/ie901264dopenalex-snapshot
Modeling of Biodiesel Multicomponent Systems with the Cubic-Plus-Association (CPA) Equation of State
inferred← citeshttps://doi.org/10.1021/je050485copenalex-snapshot
Liquid−Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS
inferred← citeshttps://doi.org/10.1021/je400684kopenalex-snapshot
Vapor–Liquid Equilibrium of Methane with Water and Methanol. Measurements and Modeling
inferred← citeshttps://doi.org/10.1021/jp1067457openalex-snapshot
Modeling the Dissociation Conditions of Salt Hydrates and Gas Semiclathrate Hydrates: Application to Lithium Bromide, Hydrogen Iodide, and Tetra-n-butylammonium Bromide + Carbon Dioxide Systems
inferred← citeshttps://doi.org/10.1080/00268976.2016.1167264openalex-snapshot
Modelling the phase equilibria of multicomponent mixtures containing CO2, alkanes, water, and/or alcohols using the quadrupolar CPA equation of state
inferred← citeshttps://doi.org/10.1134/s1070427207040040openalex-snapshot
Application of the PC-SAFT equation of state to modeling of solid-liquid equilibria in systems with organic components forming chemical compounds
inferred← citeshttps://doi.org/10.18689/ijpr-1000123openalex-snapshot
Predicting Asphaltene Precipitation from Heavy Oils Diluted by n-Heptane Using a Four-Parameter EOS
inferred← citeshttps://doi.org/10.2118/110009-msopenalex-snapshot
Application of the CPA Equation of State to Reservoir Fluids in Presence of Water and Polar Chemicals
inferred← citeshttps://doi.org/10.2139/ssrn.6889083openalex-snapshot
Locally constrained optimization of PC-SAFT parameters for reliable group contribution predictions of associating fluids
inferred← citeshttps://doi.org/10.2516/ogst:2008025openalex-snapshot
Solvation Phenomena in Association Theories with Applications to Oil & Gas and Chemical Industries
inferred← citeshttps://doi.org/10.47749/t/unicamp.2011.835088openalex-snapshot
Equilíbrio líquido-liquido na produção de biodiesel etílico
inferred← citeshttps://doi.org/10.70675/632b1ef5z7f25z4888zbd55zb8c34b0ad342openalex-snapshot
Thermodynamic study of complex systems containing gas, water, and electrolytes : application to underground gas storage
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