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Volumetric Behavior of Decane + Carbon Dioxide at High Pressures. Measurement and Calculation

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

inferredcites →https://doi.org/10.1002/aic.690210313openalex-snapshot
A generalized thermodynamic correlation based on three‐parameter corresponding states
inferredcites →https://doi.org/10.1002/aic.690250412openalex-snapshot
A new correlation for saturated densities of liquids and their mixtures
inferredcites →https://doi.org/10.1002/aic.690250413openalex-snapshot
Theoretical prediction of effective heat transfer parameters in packed beds
inferredcites →https://doi.org/10.1002/aic.690260302openalex-snapshot
A Corresponding States equation for saturated liquid densities. I. Applications to LNG
inferredcites →https://doi.org/10.1002/aic.690260303openalex-snapshot
A Corresponding States equation for saturated liquid densities. II. Applications to the calculation of swelling factors of CO2—crude oil systems
inferredcites →https://doi.org/10.1016/0009-2509(84)87009-8openalex-snapshot
Viscosity of crude oils
inferredcites →https://doi.org/10.1016/0021-9614(87)90031-0openalex-snapshot
Excess molar enthalpies and excess molar volumes of {xCO2 + (1−x)C6H5CH3} at 298.15, 304.10, and 308.15 K from 7.5 to 12.6 MPa
inferredcites →https://doi.org/10.1021/i260067a020openalex-snapshot
Calculation of High-Pressure Vapor-Liquid Equilibria from a Corresponding-States Correlation with Emphasis on Asymmetric Mixtures
inferredcites →https://doi.org/10.1021/je00038a008openalex-snapshot
Densities and viscosities of mixtures of carbon dioxide and n-decane from 310 to 403 K and 7 to 30 MPa
inferredcites →https://doi.org/10.1021/je60053a012openalex-snapshot
Improved equation for prediction of saturated liquid density
inferredcites →https://doi.org/10.1021/je60053a036openalex-snapshot
Activity coefficients for systems sodium toluenesulfonate-xylose-water and sodium toluenesulfonate-urea-water at 25.deg. from isopiestic measurements
inferredcites →https://doi.org/10.1021/je9501503openalex-snapshot
Volumetric Properties of Pentane + Carbon Dioxide at High Pressures
inferredcites →https://doi.org/10.1021/je950256yopenalex-snapshot
Liquid Viscosities of Carbon Dioxide + Hydrocarbons from 310 K to 403 K
inferredcites →https://doi.org/10.1021/je960058mopenalex-snapshot
Liquid Densities at Elevated Pressures of n-Alkanes from C5 to C16: A Critical Evaluation of Experimental Data
inferredcites →https://doi.org/10.1023/a:1010187418455openalex-snapshot
Measurement and Calculation of Heat Capacity of Heavy Distillation Cuts Under Pressure up to 40 MPa
inferredcites →https://doi.org/10.1063/1.1750658openalex-snapshot
An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures I. Methane, Ethane, Propane and n -Butane
inferredcites →https://doi.org/10.1088/0957-0233/11/5/401openalex-snapshot
Apparatus for simultaneous determination of the densities and heat capacities of liquids and of liquids with dissolved gas under an extended range of pressure (0.1-100 MPa)
inferredcites →https://doi.org/10.1088/0957-0233/3/8/002openalex-snapshot
Densimeter calibration method versus temperature and pressure
inferredcites →https://doi.org/10.1252/jcej.10.176openalex-snapshot
Correlation of the binary interaction parameter of the modified generalized BWR equation of state.
inferredcites →https://doi.org/10.1252/jcej.8.356openalex-snapshot
AN IMPROVED GENERALIZED BWR EQUATION OF STATE APPLICABLE TO LOW REDUCED TEMPERATURES

What points at this work

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

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Experimental Investigation on the Liquid Density of Co2 + N-Decane at Temperatures from 283 K to 363 K and Pressures Up to 100 Mpa
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The density characteristics of CO2 and alkane mixtures using PC‐SAFT EoS
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Hybrid connectionist model determines CO2–oil swelling factor
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The effect of gas and liquid phase composition on miscibility through interfacial tension measurements of model oils in compressed CO2
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Modern fundamental equations of state for the most important hydrocarbons of oil, gas condensates, and associated gases
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Oil detachment mechanism in CO2 flooding from silica surface: Molecular dynamics simulation
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Densities and Excess Volumes of CO2 + Decane Solution from 12 to 18 MPa and 313.15 to 343.15 K
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Density Behavior of CO2 + Decane Mixtures by Modified SAFT Equation of State
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Determination of high-pressure liquid density for n-perfluorohexane and n-perfluorononane
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Density Modeling of High-Pressure Mixtures using Cubic and Non-Cubic EoS and an Excess Volume Method
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Molecular dynamics simulation on volume swelling of CO2–alkane system
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Universal intelligent models for liquid density of CO2 + hydrocarbon mixtures
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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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Simulation and measurements of volumetric and phase behavior of carbon dioxide + higher alkanes at high pressure: CO 2 + n -decane at temperatures (313–410) K and pressures up to 76 MPa
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Compressed liquid densities and excess molar volumes for (CO2+ 1-pentanol) binary system at temperatures from 313 to 363 K and pressures up to 25 MPa
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High pressure solubility data of carbon dioxide in (tri-iso-butyl(methyl)phosphonium tosylate + water) systems
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Thermodynamic properties of coenzyme Q10 in supercritical carbon dioxide
inferred← citeshttps://doi.org/10.1016/j.supflu.2011.06.004openalex-snapshot
High pressure densities of carbon dioxide + dipentaerythritol hexaheptanoate: New experimental setup and volumetric behavior
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Effect of operational parameters on the performance of carbonated water injection: Experimental and numerical modeling study
inferred← citeshttps://doi.org/10.1016/j.supflu.2015.09.021openalex-snapshot
Fractionation technologies for liquid mixtures using dense carbon dioxide
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Volumetric behaviour of (carbon dioxide + hydrocarbon) mixtures at high pressures
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Volumetric properties of carbon dioxide + acrylic acid binary in the context of supercritical precipitation polymerization
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Review of Density Measurements and Predictions of CO2–Alkane Solutions for Enhancing Oil Recovery
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Miscibility Process of Hydrocarbon Mixture Gas and Crude Oil: Insights from Molecular Dynamics
inferred← citeshttps://doi.org/10.1021/acs.iecr.6b03729openalex-snapshot
Mass Transfer of CO2 in a Carbonated Water–Oil System at High Pressures
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Density and Volumetric Behavior of Binary CO2 + n-Decane and Ternary CO2 + n-Decane + Naphthalene Systems at High Pressure and High Temperature
inferred← citeshttps://doi.org/10.1021/acs.jced.6b00026openalex-snapshot
Density and Volumetric Behavior of CO2 + Undecane System from 313.15 to 353.15 K and Pressures up to 19 MPa
inferred← citeshttps://doi.org/10.1021/acs.jced.7b00995openalex-snapshot
Measurements and Modeling of Volumetric and Phase Behavior of Carbon Dioxide + Higher Alkanes: CO2 + n -Pentadecane at Temperatures 313 to 410 K and Pressures up to 77 MPa
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Measurements and Modeling of Phase Behavior, Density, and Viscosity of Oil + Carbon Dioxide: Squalane + CO2 at Temperatures (313 to 363) K and Pressures up to 77 MPa
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Density of Hydrocarbon Mixtures and Bitumen Diluted with Solvents and Dissolved Gases
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Phase Equilibria,PVTBehavior, and Critical Phenomena in Carbon Dioxide +n-Alkane Mixtures Using the Perturbed-Chain Statistical Associating Fluid Theory Approach
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Compressed Liquid Densities and Excess Volumes of CO2 + Decane Mixtures from (313 to 363) K and Pressures up to 25 MPa
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Short Fundamental Equations of State for 20 Industrial Fluids
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Densities and Volumetric Characteristics of Binary System of CO2 + Decane from (303.15 to 353.15) K and Pressures up to 19 MPa
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The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004
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High-Pressure Solubility Data of Methane in Aniline and Aqueous Aniline Systems
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Measurements of Compressed Liquid Densities for CO2(1) + Butan-1-ol (2) via a Vibrating Tube Densimeter at Temperatures from (313 to 363) K and Pressures up to 25 MPa
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Temperature and Pressure Dependence of Branched Pentaerythritol Ester Density
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PρT Measurements of Nonafluorobutyl Methyl Ether and Nonafluorobutyl Ethyl Ether Between 283.15 and 323.15 K at Pressures Up to 40 MPa
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Measurements of Volumetric Phase Behavior of Mixtures of n-decane and CO2 at High Pressures and High Temperatures
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Measurement of Bubble Point Pressures of n-Decane, CO2 and N2 Mixtures
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A Tangent-Line Approach for Effective Density Used in the Ideal Mixing Rule: Part II—Evaluation of Mixing Characteristics of Oil/Gas Systems and Application Criteria
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Phase Behavior and Widom-Line Analogy in CO2–n-Hexadecane Mixtures: From Subcritical to Supercritical Regions
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Determination of Compressed Liquid Densities for CO2 + n-Decane Using a Vibrating Tube Densimeter
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