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Volumetric Properties of 1-Phenyldecane and 1-Phenylundecane at Pressures to 65 MPa and Temperature between 293.15 and 353.15 K

https://doi.org/10.1021/je0500936
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Outgoing claims: the papers this work cites, builds on, or argues with.

inferredcites →https://doi.org/10.1007/bf02083543openalex-snapshot
Determination of the viscosity of various hydrocarbons and mixtures of hydrocarbons versus temperature and pressure
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Extension of the application of the Simha equation of state to the calculation of the density of n-alkanes-benzene and alkylbenzenes mixtures
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Physical Properties of n-Hexadecane, n-Decylcyclopentane, n-Decylcyclohexane, 1-Hexadecene and n-Decylbenzene
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Speed of Sound, Density, and Compressibility of Alkylbenzenes as a Function of Pressure and Temperature: Tridecylbenzene and Pentadecylbenzene
inferredcites →https://doi.org/10.1021/je049685zopenalex-snapshot
Density Measurements under Pressure for the Binary System 1-Propanol + Toluene
inferredcites →https://doi.org/10.1088/0957-0233/3/8/002openalex-snapshot
Densimeter calibration method versus temperature and pressure

What points at this work

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Liquid Density of Binary Mixtures of N-Pentane and N-Dodecane at Temperatures from 283 to 363 K and Pressures Up to 100 Mpa
inferred← citeshttps://doi.org/10.2139/ssrn.4773908openalex-extracted
Experimental Investigation on the Liquid Density of Co2 + N-Decane at Temperatures from 283 K to 363 K and Pressures Up to 100 Mpa
inferred← citeshttps://doi.org/10.1016/j.chemolab.2011.10.014openalex-snapshot
Multiplicative algorithm for computing D-optimum designs for pVT measurements
inferred← citeshttps://doi.org/10.1016/j.fluid.2006.05.032openalex-snapshot
Volumetric and derivative properties under pressure for the system 1-propanol + toluene: A discussion of PC-SAFT and SAFT-VR
inferred← citeshttps://doi.org/10.1016/j.fluid.2006.12.011openalex-snapshot
Stereoisomeric effects on volumetric properties under pressure for the system cis-+trans-decalin
inferred← citeshttps://doi.org/10.1016/j.fluid.2008.06.007openalex-snapshot
Liquid density of 1-pentanol at pressures up to 140MPa and from 293.15 to 403.15K
inferred← citeshttps://doi.org/10.1016/j.fluid.2010.11.020openalex-snapshot
Liquid density of 1-butanol at pressures up to 140MPa and from 293.15K to 403.15K
inferred← citeshttps://doi.org/10.1016/j.fluid.2012.02.007openalex-snapshot
Liquid density of oxygenated additives to bio-fuels: 1-Hexanol at pressures up to 140MPa and from 293.15K to 403.15K
inferred← citeshttps://doi.org/10.1016/j.fluid.2013.11.031openalex-snapshot
(p, VE, T) Measurements of mixtures (DBE+alcohol) at temperatures from (293.15 to 353.15)K and at pressures up to 140MPa
inferred← citeshttps://doi.org/10.1016/j.fluid.2017.12.010openalex-snapshot
Compressed liquid densities of binary mixtures of n -decane + n -dodecane at temperatures from 283 K to 363 K and pressures up to 100 MPa
inferred← citeshttps://doi.org/10.1016/j.fluid.2019.02.028openalex-snapshot
Density of biofuel mixtures (Dibutyl ether + Heptane) at temperatures from (298.15–393.15) K and at pressures up to 140 MPa: Experimental data and PC-SAFT modeling
inferred← citeshttps://doi.org/10.1016/j.fluid.2019.06.003openalex-snapshot
Characterization and determination of thermodynamic properties of waste cooking oil biodiesel: Experimental, correlation and modeling density over a wide temperature range up to 393.15 and pressure up to 140 MPa
inferred← citeshttps://doi.org/10.1016/j.fluid.2024.114078openalex-snapshot
Liquid density of binary mixtures of n-pentane and n-dodecane at temperatures from 283K to 363K and pressures up to 100MPa
inferred← citeshttps://doi.org/10.1016/j.fluid.2025.114501openalex-snapshot
Experimental investigation of liquid density for n-pentane + n-decane mixtures at temperatures from 283 K to 363 K and pressures up to 100 MPa
inferred← citeshttps://doi.org/10.1016/j.fuel.2018.06.091openalex-snapshot
Thermophysical behavior of three algal biodiesels over wide ranges of pressure and temperature
inferred← citeshttps://doi.org/10.1016/j.jct.2008.01.006openalex-snapshot
High-pressure (up to 140 MPa) density and derivative properties of some (pentyl-, hexyl-, and heptyl-) amines between (293.15 and 353.15) K
inferred← citeshttps://doi.org/10.1016/j.jct.2011.06.006openalex-snapshot
Liquid density of biofuel mixtures: (Dibutyl ether + 1-butanol) system at pressures up to 140 MPa and temperatures from (293.15 to 393.15) K
inferred← citeshttps://doi.org/10.1016/j.jct.2012.05.016openalex-snapshot
Liquid density of oxygenated additive 2-propanol at pressures up to 140 MPa and from 293.15 K to 403.15 K
inferred← citeshttps://doi.org/10.1016/j.jct.2018.11.010openalex-snapshot
Experimental density and PC-SAFT modeling of biofuel mixtures (DBE + 1-Heptanol) at temperatures from (298.15 to 393.15) K and at pressures up to 140 MPa
inferred← citeshttps://doi.org/10.1016/j.jct.2019.105935openalex-snapshot
Compressed liquid densities of binary mixtures of difluoromethane (R32) and 2,3,3,3-tetrafluoroprop-1-Ene (R1234yf) at temperatures from (283 to 363) K and pressures up to 100 MPa
inferred← citeshttps://doi.org/10.1016/j.jngse.2014.12.005openalex-snapshot
Investigation of volumetric fluid properties of (heptane + hexadecane) at reservoir conditions
inferred← citeshttps://doi.org/10.1016/j.petrol.2015.10.021openalex-snapshot
Prediction of Saraline-based super lightweight completion fluid densities at elevated pressures and temperatures
inferred← citeshttps://doi.org/10.1021/acs.jced.5b00385openalex-snapshot
Liquid Density of 2-Methoxyethyl Acetate, 2-Ethylhexyl Acetate, and Diethyl Succinate at Temperatures from 283.15 K to 363.15 K and Pressures up to 100 MPa
inferred← citeshttps://doi.org/10.1021/acs.jced.5c00580openalex-snapshot
Undecane and n -Alkylbenzenes: Densities, Speeds of Sound, and Viscosities within the Range (288.15 to 333.15) K and at 0.1 MPa
inferred← citeshttps://doi.org/10.1021/acs.jced.6b00192openalex-snapshot
Densities of Diethylene Glycol, Monobutyl Ether, Diethylene Glycol Dibutyl Ether, and Ethylene Glycol Monobutyl Ether from (283.15 to 363.15) K at Pressures up to 60 MPa
inferred← citeshttps://doi.org/10.1021/acs.jced.8b00229openalex-snapshot
Liquid Density of n-Pentene, n-Hexene, and n-Heptene at Temperatures from 283.15 to 363.15 K and Pressures up to 100 MPa
inferred← citeshttps://doi.org/10.1021/acs.jced.9b00273openalex-snapshot
(ρ, VE, T) Measurements of the Ternary Mixture (Dibutyl Ether + 1-Heptanol + Heptane) at Temperatures up to 393.15 K and Pressures up to 140 MPa and Modeling Using the Peng–Robinson and PC-SAFT Equations of State
inferred← citeshttps://doi.org/10.1021/acs.jced.9b00391openalex-snapshot
High-Pressure Soybean Oil Biodiesel Density: Experimental Measurements, Correlation by Tait Equation, and Perturbed Chain SAFT (PC-SAFT) Modeling
inferred← citeshttps://doi.org/10.1021/je050261uopenalex-snapshot
High-Pressure Density Measurements for the Binary System Ethanol + Heptane
inferred← citeshttps://doi.org/10.1021/je101286aopenalex-snapshot
Liquid Density of Biofuel Additives: 1-Butoxybutane at Pressures up to 140 MPa and from (293.15 to 393.15) K
inferred← citeshttps://doi.org/10.1021/je700529yopenalex-snapshot
Solid−Liquid Equilibria under High Pressure of Nine Puren-Alkylbenzenes
inferred← citeshttps://doi.org/10.1021/je700737copenalex-snapshot
Density of Diethyl Adipate using a New Vibrating Tube Densimeter from (293.15 to 403.15) K and up to 140 MPa. Calibration and Measurements
inferred← citeshttps://doi.org/10.1021/je800786kopenalex-snapshot
Volumetric Properties of 2-Alkylamines (2-Aminobutane and 2-Aminooctane) at Pressures up to 140 MPa and Temperatures between (293.15 and 403.15) K
inferred← citeshttps://doi.org/10.1039/d0cp06458kopenalex-snapshot
Liquid dibromomethane under pressure: a computational study
inferred← citeshttps://doi.org/10.1080/00268976.2012.662303openalex-snapshot
SAFT- γ force field for the simulation of molecular fluids: 3. Coarse-grained models of benzene and hetero-group models of n -decylbenzene
inferred← citeshttps://doi.org/10.1080/10916466.2010.521791openalex-snapshot
A Tait-like Equation for Estimating the Density of Nontraditional Super Lightweight Completion Fluid at High Pressure and Temperature
inferred← citeshttps://doi.org/10.2118/180619-msopenalex-snapshot
Density and Viscosity Prediction of Super Lightweight Completion Fluid SLWCF at Reservoir Conditions
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