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Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
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What this work says
Outgoing claims: the papers this work cites, builds on, or argues with.
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New group contribution method for estimating properties of pure compounds
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High pressure phase equilibria in the carbon dioxide ‐ n‐Hexadecane and carbon dioxide — water systems
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Generation, Capture, and Utilization of Industrial Carbon Dioxide
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Equilibrium constants from a modified Redlich-Kwong equation of state
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Improvement of the Van Der Waals equation of state
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Multiphase high pressure equilibria in ternary aqueous systems
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High pressure fluid phase equilibria: experimental methods and systems investigated (1978–1987)
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Estimation of the acentric factor and the liquid molar volume at 298 K using a new group contribution method
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Phase equilibria in systems containing hydrogen, carbon dioxide, water and hydrocarbons
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Prediction of vapor-liquid equilibrium with the LCVM model: a linear combination of the Vidal and Michelsen mixing rules coupled with the original UNIF
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High-pressure fluid-phase equilibria: Experimental methods and systems investigated (1988–1993)
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Physical properties of heavy petroleum fractions and crude oils
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Phase Behaviour of CO2–Brine and CO2–Oil Systems for CO2 Storage and Enhanced Oil Recovery: Experimental Studies
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A Survey of Public Perception of CCUS in China
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VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method
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Extension of the PPR78 model (predictive 1978, Peng–Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing aromatic compounds
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Extension of the PPR78 model (Predictive 1978, Peng–Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing naphtenic compounds
inferredcites →https://doi.org/10.1016/j.fluid.2006.05.014openalex-snapshot
Experimental determination and calculation of thermodynamic properties of CO2+octane to high temperatures and high pressures
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New isothermal vapor–liquid equilibria for the CO2+n-nonane, and CO2+n-undecane systems
inferredcites →https://doi.org/10.1016/j.fluid.2009.08.008openalex-snapshot
High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2000–2004)
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Relationship between the binary interaction parameters (kij) of the Peng–Robinson and those of the Soave–Redlich–Kwong equations of state: Application to the definition of the PR2SRK model
inferredcites →https://doi.org/10.1016/j.fluid.2010.09.017openalex-snapshot
High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2005–2008)
inferredcites →https://doi.org/10.1016/j.fluid.2012.04.010openalex-snapshot
Validation of a new apparatus using the dynamic method for determining the critical properties of binary mixtures containing CO2 and a n-alkane
inferredcites →https://doi.org/10.1016/j.fluid.2012.10.016openalex-snapshot
Reliability of the correlation allowing the kij to switch from an alpha function to another one in hydrogen-containing systems
inferredcites →https://doi.org/10.1016/j.fluid.2013.12.018openalex-snapshot
Experimental and modeling study of the phase behavior of synthetic crude oil+CO2
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Improved empirical correlation for petroleum fraction composition quantitative prediction
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High-pressure phase behaviour of the binary system {CO2+cis-decalin} from (292.75 to 373.75) K
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inferredcites →https://doi.org/10.1016/j.supflu.2007.09.026openalex-snapshot
Vapor–liquid phase equilibrium behavior of mixtures containing supercritical carbon dioxide near critical region
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Phase equilibria measurements of CO2+ methyl cyclopentane and CO2+ isopropyl cyclohexane binary mixtures at elevated pressures
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Aspects of the constitution of mineral oils
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Solubility of n-octadecane in supercritical carbon dioxide at 310, 313, 333, and 353 K, in the range 10–20 MPa
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A new quartic equation of state
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High-pressure fluid phase equilibria
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A New Two-Constant Equation of State
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Prediction of the Composition of Petroleum Fractions
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Investigation of Vapor−Liquid Equilibria for Supercritical Carbon Dioxide and Hydrocarbon Mixtures by Perturbed-Chain Statistical Associating Fluid Theory
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Phase Equilibrium in Two-Phase, Water-Rich-Liquid, Hydrate Systems: Experiment and Theory
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Phase Behavior for the Carbon Dioxide + N-Pentadecane Binary System
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Solubility of CO 2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
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Vapor–Liquid Equilibria of Binary and Ternary Systems Containing Carbon Dioxide, Alkane, and Benzothiophene
inferredcites →https://doi.org/10.1021/je400985uopenalex-snapshot
Vapor–Liquid Phase Equilibrium Data of CO2 in Some Physical Solvents from 285.19 K to 313.26 K
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Fast Determination of Binary Vapor–Liquid Equilibrium of CO2-Based Mixtures at Elevated Pressures
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Isothermal vapor-liquid equilibrium data for binary systems containing carbon dioxide at high pressures: methanol-carbon dioxide, n-hexane-carbon dioxide, and benzene-carbon dioxide systems
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Bubble and Dew Points of Carbon Dioxide + a Five-Component Synthetic Mixture: Experimental Data and Modeling with the PPR78 Model
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Equilibrium Studies for the System Methane + Carbon Dioxide + Neohexane + Water
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Experimental and Molecular Modeling Study of the Three-Phase Behavior of (n-Decane + Carbon Dioxide + Water) at Reservoir Conditions
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Guidelines for evaluating and expressing the uncertainty of NIST measurement results
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Incoming claims: where this work appears in other papers’ reference lists and arguments.
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The CO2 + 2,3,4-trimethylpentane and CO2 + 2,2,4,6,6-pentamethylheptane binary systems: high–pressure phase equilibria measurements
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High-pressure phase behavior and asymmetry effects in the CO2 + butylcyclohexane + o-terphenyl and CO2 + bicyclohexyl + o-terphenyl ternary systems
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An improved binary interaction parameter correlation for phase-equilibrium modeling of CO₂– heavy oil systems
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Experimental study of the phase behavior of methane and crude oil mixtures
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The miscible behaviors of C10H22(C7H17N)/C3H8 system: Insights from molecular dynamics simulations
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The solubility of CO2 in (hexane + cyclohexane) and (cyclopentane + ethylbenzene) and (toluene + undecane) systems at high pressures
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Experiment and model for solubility of CO2 in alkanes with ethyl acetate as cosolvent
inferred← citeshttps://doi.org/10.1016/j.jct.2025.107546openalex-snapshot
High-pressure phase equilibria and volumetric properties of the CO2 + hexadecane + butylcyclohexane system: Experimental and modeling study
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Integration of a fused silica capillary and in-situ Raman spectroscopy for investigating CO2 solubility in n-dodecane at near-critical and supercritical conditions of CO2
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Phase equilibrium data for carbon dioxide/methane/hydrogen + 2-methyl quinoline from T = 263–393 K and P up to 2.6 MPa
inferred← citeshttps://doi.org/10.1021/acs.energyfuels.9b03560openalex-snapshot
Phase Behavior for Crude Oil and Methane Mixtures: Crude Oil Property Comparison
inferred← citeshttps://doi.org/10.1021/acs.jced.0c00988openalex-snapshot
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