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Densities and volumetric characteristics of pseudo-binary mixtures of CO2 + crude oil from 363.15−393.15 K and 25−35 MPa

https://doi.org/10.2139/ssrn.6320693

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

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Study on fluid phase behavior characteristics of low permeability reservoir under different CO2 injection amounts

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Experimental and modeling study of the phase behavior of synthetic crude oil+CO2

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Binary interaction coefficients of asymmetric CH4, C2H6, and CO2 with high n-alkanes for the simplified PC-SAFT correlation and prediction

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On the CO2 storage potential of cyclic CO2 injection process for enhanced oil recovery

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Experimental and predictive PC-SAFT modeling results for density and isothermal compressibility for two crude oil samples at elevated temperatures and pressures

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Investigation of the viscosity and density of heavy oil/water blends at elevated temperatures and pressure; Part 1: Oil-only sample (absence of water)

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Phase composition and saturated liquid properties in binary and ternary systems containing carbon dioxide, n-decane, and n-tetradecane

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Experimental investigation of tertiary CO 2 injection for enhanced heavy oil recovery

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Simultaneous measurement of the density and viscosity for n-Decane + CO2 binary mixtures at temperature between (303.15 to 373.15) K and pressures up to 80 MPa

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A comparative study of oil compositional variations during CO2 and carbonated water injection scenarios for EOR

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Volumetric behaviour of (carbon dioxide + hydrocarbon) mixtures at high pressures

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Solubility of squalane, dinonyl phthalate and glycerol in supercritical CO2

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Solubility of carbon dioxide in eicosane, docosane, tetracosane, and octacosane at temperatures from 323 to 473 K and pressures up to 40 MPa

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Swelling/extraction test of Russian reservoir heavy oil by liquid carbon dioxide

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Global oil and gas development situation, trends and enlightenment in 2023

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Phase Transitions and Separation Time Scales of CO2–Crude Oil Fluid Systems: Wheel Flow Loop Experiments and Modeling

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Density and Viscosity of CO2 + Ethanol Binary Systems Measured by a Capillary Viscometer from 308.15 to 338.15 K and 15 to 45 MPa

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Density and Volumetric Behavior of Ternary CO2 + n-Decane + n-Butylcyclohexane Mixtures at High Pressure and High Temperature

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Molecular Simulation Study on the Density Behavior of n-Alkane/CO2 Systems

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Density Measurement and Prediction Model of the CO2–Water-Bearing Crude Oil System

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Oil Recovery Performance of Immiscible and Miscible CO2 Huff-and-Puff Processes

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Compressed Liquid Densities of Carbon Dioxide + Ethanol Mixtures at Four Compositions via a Vibrating Tube Densimeter up to 363 K and 25 MPa

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Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n -Alkanes (C7 to C14) at T = 293.15 K to 313.15 K

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The IAPWS Formulation 1995 for the Thermodynamic Properties of Ordinary Water Substance for General and Scientific Use

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A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple-Point Temperature to 1100 K at Pressures up to 800 MPa

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Apparatus to measure density and viscosity of high-pressure carbon dioxide–alcohol mixtures

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A Genetic Algorithm-Based Model to Predict CO-Oil Physical Properties for Dead and Live Oil

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Measurements and Correlations of the Physical Properties of CO2-Heavy Crude Oil Mixtures

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An Experimental Study of Nonequilibrium Carbon Dioxide/Oil Interactions

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Predicting Phase Behavior of Condensate/Crude-Oil Systems Using Methane Interaction Coefficients

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Molecular dynamics simulation of CO2 dissolution-diffusion in multi-component crude oil

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