Chemical Properties of Carbon dioxide (CAS 124-38-9)

Carbon dioxide

InChI
InChI=1S/CO2/c2-1-3
InChI Key
CURLTUGMZLYLDI-UHFFFAOYSA-N
Formula
CO2
SMILES
O=C=O
Molecular Weight1
44.01
CAS
124-38-9
Other Names
  • Anhydride carbonique
  • CARBONIC ANHYDRIDE
  • CO2
  • Carbon oxide (CO2)
  • Carbonic acid anhydride
  • Carbonic acid, gas
  • Carbonica
  • Cardice
  • Dricold
  • Drikold
  • Dry ice
  • Khladon 744
  • Kohlendioxyd
  • Kohlensaure
  • R 744
  • UN 1013
  • UN 1845
  • UN 2187
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Contents

  1. Physical Properties
  2. Temperature Dependent Properties
  3. Datasets
  4. Correlations
  5. Similar Compounds
  6. Mixtures
  7. Sources

Physical Properties

Property Value Unit Source
ω 0.2390 KDB
PAff 540.50 kJ/mol NIST
BasG 515.80 kJ/mol NIST
μ 0.00 debye KDB
EA [-1.60; -0.60] eV Show Hide
EA -0.60 eV NIST
EA -1.60 ± 0.10 eV NIST
Δf -394.60 kJ/mol KDB
Rg 0.9920 KDB
Δfgas [-393.80; -393.51] kJ/mol Show Hide
Δfgas -393.80 kJ/mol KDB
Δfgas -393.51 ± 0.13 kJ/mol NIST
Δfus 11.09 kJ/mol Joback Calculated Property
Δvap 13.60 kJ/mol Relay (1.0) Calculated Property
IE [13.00; 13.90] eV Show Hide
IE 13.78 ± 0.00 eV NIST
IE 13.78 ± 0.00 eV NIST
IE 13.78 eV NIST
IE 13.78 ± 0.00 eV NIST
IE Outlier 13.00 ± 1.00 eV NIST
IE 13.89 ± 0.03 eV NIST
IE 13.79 ± 0.05 eV NIST
IE 13.77 eV NIST
IE 13.78 ± 0.00 eV NIST
IE 13.83 ± 0.05 eV NIST
IE 13.79 eV NIST
IE 13.78 ± 0.00 eV NIST
IE 13.77 ± 0.00 eV NIST
IE 13.90 ± 0.20 eV NIST
IE 13.78 ± 0.01 eV NIST
IE 13.78 eV NIST
IE 13.77 ± 0.00 eV NIST
IE 13.80 ± 0.01 eV NIST
IE 13.79 ± 0.01 eV NIST
IE 13.78 ± 0.01 eV NIST
IE 13.77 eV NIST
IE 13.75 ± 0.05 eV NIST
IE 13.77 ± 0.00 eV NIST
IE 13.77 ± 0.03 eV NIST
IE 13.77 eV NIST
IE 13.78 eV NIST
IE 13.78 eV NIST
IE 13.79 eV NIST
log10WS 0.72 Relay (1.0) Calculated Property
logPoct/wat -0.584 Crippen Calculated Property
McVol 28.090 ml/mol McGowan Calculated Property
Pc [7340.00; 7420.00] kPa Show Hide
Pc 7375.00 kPa KDB
Pc 7420.00 kPa Critical Properties of Binary and Ternary Mixtures of Hexane + Methanol, Hexane + Carbon Dioxide, Methanol + Carbon Dioxide and Hexane + Carbon Dioxide + Methanol
Pc 7360.00 kPa Phase Behaviors, Density, and Isothermal Compressibility of Styrene + CO2, Ethylbenzene + CO2, and Ethylbezene + Styrene + CO2 Systems
Pc 7420.00 kPa Critical Properties of the Reacting Mixture in the Esterification of Acetic Acid with Ethanol
Pc 7380.00 kPa Critical Properties of the Reacting Mixture in the Selective Oxidation of Cyclohexane by Oxygen in the Presence of Carbon Dioxide
Pc 7380.00 kPa Critical Temperatures and Pressures of Several Binary and Ternary Mixtures Concerning the Alkylation of 2-Methylpropane with 1-Butene in the Presence of Methane or Carbon Dioxide
Pc 7380.00 ± 15.00 kPa NIST
Pc 7340.00 ± 50.00 kPa NIST
Pc 7382.50 ± 0.50 kPa NIST
Ptriple [518.50; 518.50] kPa Show Hide
Ptriple 518.50 kPa KDB
Ptriple 518.50 ± 0.50 kPa NIST
ρc [466.06; 475.30] kg/m3 Show Hide
ρc 466.50 ± 2.20 kg/m3 NIST
ρc 466.06 ± 0.31 kg/m3 NIST
ρc 475.30 ± 8.80 kg/m3 NIST
ρc 468.26 ± 1.50 kg/m3 NIST
Inp [152.00; 154.00]   Show Hide
Inp 154.00 NIST
Inp 153.00 NIST
Inp 152.00 NIST
Inp 152.00 NIST
gas,1 bar 213.78 ± 0.01 J/mol×K NIST
Tboil 194.70 K KDB
Tc [304.10; 304.35] K Show Hide
Tc 304.14 K KDB
Tc 304.30 K Validation of a New Apparatus Using the Dynamic Method for Determining the Critical Properties of Binary Gas/Gas Mixtures
Tc 304.30 K Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Tc 304.18 ± 0.04 K NIST
Tc 304.10 ± 0.10 K NIST
Tc 304.35 ± 0.40 K NIST
Tc 304.20 ± 0.02 K NIST
Tc 304.23 K NIST
Tfus 216.58 K KDB
Ttriple [216.52; 216.60] K Show Hide
Ttriple 216.58 K KDB
Ttriple 216.52 K Solid Liquid Equilibria for the CO2 + R23 and N2O + R23 Systems
Ttriple 216.60 K Solid-liquid equilibria measurements of the carbondioxide + 2,3,3,3-tetrafluoroprop-1-ene and carbondioxide + trans-1,3,3,3-tetrafluoropropene mixtures
Ttriple 216.58 ± 0.01 K NIST
Ttriple 216.58 ± 0.03 K NIST
Vc [0.092; 0.094] m3/kmol Show Hide
Vc 0.094 m3/kmol KDB
Vc 0.092 ± 0.001 m3/kmol NIST
Zc 0.2741450 KDB
Zra 0.27 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [32.51; 42.55] J/mol×K [203.15; 331.33] Show Hide
Cp,gas 32.51 J/mol×K 203.15 Joback Calculated Property
Cp,gas 34.58 J/mol×K 224.51 Joback Calculated Property
Cp,gas 36.48 J/mol×K 245.88 Joback Calculated Property
Cp,gas 38.22 J/mol×K 267.24 Joback Calculated Property
Cp,gas 39.81 J/mol×K 288.60 Joback Calculated Property
Cp,gas 41.25 J/mol×K 309.97 Joback Calculated Property
Cp,gas 42.55 J/mol×K 331.33 Joback Calculated Property
η [0.0000236; 0.0000452] Pa×s [500.00; 1100.00] Show Hide
η 0.0000236 Pa×s 500.00 Viscosity of H2-CO2 Mixtures at (500, 800, and 1100) K
η 0.0000356 Pa×s 800.00 Viscosity of H2-CO2 Mixtures at (500, 800, and 1100) K
η 0.0000452 Pa×s 1100.00 Viscosity of H2-CO2 Mixtures at (500, 800, and 1100) K
ΔsubH [25.20; 27.20] kJ/mol [86.00; 207.00] Show Hide
ΔsubH 27.20 ± 0.40 kJ/mol 86.00 NIST
ΔsubH 26.30 kJ/mol 167.00 NIST
ΔsubH 25.20 kJ/mol 175.00 NIST
ΔsubH 25.90 kJ/mol 188.50 NIST
ΔsubH 26.10 kJ/mol 207.00 NIST
ΔvapH [15.33; 28.84] kJ/mol [82.30; 288.50] Show Hide
ΔvapH 28.84 kJ/mol 82.30 Measurements of enthalpy of sublimation of Ne, N2, O2, Ar, CO2, Kr, Xe, and H2O using a double paddle oscillator
ΔvapH 15.33 kJ/mol 216.60 KDB
ΔvapH 16.40 kJ/mol 244.50 NIST
ΔvapH 16.50 kJ/mol 285.00 NIST
ΔvapH 16.70 kJ/mol 288.50 NIST
Pvap [410.40; 7360.50] kPa [213.22; 304.04] Show Hide
Pvap 410.40 kPa 213.22 Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213 to 299 K and pressures up to 16 MPa
Pvap 552.50 kPa 218.15 Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
Pvap 682.90 kPa 223.14 Vapor-liquid equilibrium data for the carbon dioxide and nitrogen (CO2+N2 ) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPa
Pvap 681.80 kPa 223.15 Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213 to 299 K and pressures up to 16 MPa
Pvap 1000.72 kPa 233.07 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 1000.81 kPa 233.07 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 1004.40 kPa 233.15 Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
Pvap 1009.00 kPa 233.19 Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap 1420.40 kPa 243.01 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 1420.51 kPa 243.01 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 1426.30 kPa 243.13 Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213 to 299 K and pressures up to 16 MPa
Pvap 1428.00 kPa 243.15 Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
Pvap 1426.50 kPa 243.15 Experimental research on (vapor + liquid) equilibria for the {trifluoroiodomethane (CF3I) + carbon dioxide (CO2)} system from 243.150 to 273.150 K
Pvap 1432.00 kPa 243.22 Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap 1672.60 kPa 248.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 1964.80 kPa 253.15 Vapor liquid equilibria for the carbon dioxide + propane system over a temperature range from 253.15 to 323.15K
Pvap 1968.40 kPa 253.15 Experimental research on (vapor + liquid) equilibria for the {trifluoroiodomethane (CF3I) + carbon dioxide (CO2)} system from 243.150 to 273.150 K
Pvap 1970.00 kPa 253.21 Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap 1974.16 kPa 253.22 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 1974.47 kPa 253.22 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 2293.70 kPa 258.15 Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
Pvap 2294.00 kPa 258.44 (Vapor + liquid) equilibrium data for (carbon dioxide + 1,1-difluoroethane) system at temperatures from (258 to 343) K and pressures up to about 8 MPa
Pvap 2646.70 kPa 263.13 Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213 to 299 K and pressures up to 16 MPa
Pvap 2647.50 kPa 263.15 Experimental research on (vapor + liquid) equilibria for the {trifluoroiodomethane (CF3I) + carbon dioxide (CO2)} system from 243.150 to 273.150 K
Pvap 2641.80 kPa 263.15 Vapor liquid equilibria for the carbon dioxide + propane system over a temperature range from 253.15 to 323.15K
Pvap 2645.00 kPa 263.21 Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap 2661.57 kPa 263.31 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 2661.88 kPa 263.32 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 3476.00 kPa 272.78 Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
Pvap 3387.00 kPa 273.00 Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap 3485.10 kPa 273.15 Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap 3483.80 kPa 273.15 Experimental research on (vapor + liquid) equilibria for the {trifluoroiodomethane (CF3I) + carbon dioxide (CO2)} system from 243.150 to 273.150 K
Pvap 3478.50 kPa 273.15 Vapor liquid equilibria for the carbon dioxide + propane system over a temperature range from 253.15 to 323.15K
Pvap 3487.00 kPa 273.15 Phase equilibrium and critical point data for ethylene and chlorodifluoromethane binary mixtures using a new static-analytic apparatus
Pvap 3484.60 kPa 273.15 Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
Pvap 3485.70 kPa 273.16 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 3485.90 kPa 273.17 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 3473.00 kPa 273.19 Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
Pvap 3491.30 kPa 273.22 Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213 to 299 K and pressures up to 16 MPa
Pvap 3522.07 kPa 273.55 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 3522.39 kPa 273.56 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 3958.00 kPa 277.83 Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
Pvap 3960.00 kPa 278.15 Isothermal Vapor-Liquid Equilibria for the Binary System of Carbon Dioxide (CO2) + 1,1,1,2,3,3,3-Heptafluoropropane (R-227ea)
Pvap 3962.00 kPa 278.15 Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
Pvap 3977.00 kPa 278.20 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 3975.00 kPa 278.20 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 3977.00 kPa 278.25 (Vapor + liquid) equilibrium data for (carbon dioxide + 1,1-difluoroethane) system at temperatures from (258 to 343) K and pressures up to about 8 MPa
Pvap 4392.00 kPa 282.15 Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
Pvap 4487.00 kPa 282.87 Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
Pvap 4406.00 kPa 283.00 Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap 4502.30 kPa 283.15 Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213 to 299 K and pressures up to 16 MPa
Pvap 4497.80 kPa 283.15 Vapor liquid equilibria for the carbon dioxide + propane system over a temperature range from 253.15 to 323.15K
Pvap 4502.00 kPa 283.15 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 4500.50 kPa 283.15 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 4543.19 kPa 283.51 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 4543.58 kPa 283.52 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 4961.00 kPa 287.11 Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
Pvap 5069.00 kPa 287.92 Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
Pvap 5080.00 kPa 288.15 Isothermal Vapor-Liquid Equilibria for the Binary System of Carbon Dioxide (CO2) + 1,1,1,2,3,3,3-Heptafluoropropane (R-227ea)
Pvap 5087.00 kPa 288.15 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 5090.50 kPa 288.15 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 5089.60 kPa 288.19 Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
Pvap 5555.00 kPa 291.84 Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
Pvap 5705.00 kPa 292.95 Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
Pvap 5627.00 kPa 293.00 Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap 5720.90 kPa 293.08 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 5721.42 kPa 293.09 Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
Pvap 5726.40 kPa 293.14 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 5726.50 kPa 293.14 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 5723.70 kPa 293.15 Vapor liquid equilibria for the carbon dioxide + propane system over a temperature range from 253.15 to 323.15K
Pvap 6020.00 kPa 295.45 A synthetic-dynamic method for water solubility measurements in high pressure CO2 using ATR FTIR spectroscopy
Pvap 6214.00 kPa 296.64 Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
Pvap 6240.00 kPa 297.05 A synthetic-dynamic method for water solubility measurements in high pressure CO2 using ATR FTIR spectroscopy
Pvap 6404.00 kPa 297.99 Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
Pvap 6323.00 kPa 298.10 Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
Pvap 6425.00 kPa 298.15 Isothermal Vapor-Liquid Equilibria for the Binary System of Carbon Dioxide (CO2) + 1,1,1,2,3,3,3-Heptafluoropropane (R-227ea)
Pvap 6436.10 kPa 298.15 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 6430.10 kPa 298.15 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 6436.90 kPa 298.17 Vapor-liquid equilibrium data for the carbon dioxide and nitrogen (CO2+N2 ) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPa
Pvap 6502.60 kPa 298.84 (Vapor + liquid) equilibrium data for (carbon dioxide + 1,1-difluoroethane) system at temperatures from (258 to 343) K and pressures up to about 8 MPa
Pvap 6520.00 kPa 299.05 A synthetic-dynamic method for water solubility measurements in high pressure CO2 using ATR FTIR spectroscopy
Pvap 6595.00 kPa 299.22 Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213 to 299 K and pressures up to 16 MPa
Pvap 6928.00 kPa 301.38 Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
Pvap 7090.00 kPa 302.65 A synthetic-dynamic method for water solubility measurements in high pressure CO2 using ATR FTIR spectroscopy
Pvap 7171.20 kPa 302.94 Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa
Pvap 7176.00 kPa 303.03 Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
Pvap 7206.20 kPa 303.15 Vapor liquid equilibria for the carbon dioxide + propane system over a temperature range from 253.15 to 323.15K
Pvap 7214.40 kPa 303.15 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 7210.50 kPa 303.16 Vapor-liquid equilibrium data for the carbon dioxide and nitrogen (CO2+N2 ) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPa
Pvap 7212.80 kPa 303.19 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 7180.00 kPa 303.25 A synthetic-dynamic method for water solubility measurements in high pressure CO2 using ATR FTIR spectroscopy
Pvap 7290.90 kPa 303.64 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 7297.40 kPa 303.65 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 7326.10 kPa 303.85 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 7329.00 kPa 303.85 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 7360.50 kPa 304.04 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
Pvap 7358.80 kPa 304.04 A novel technique based in a cylindrical microwave resonator for high pressure phase equilibrium determination
ρg 1.56 kg/m3 344.15 High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
γ 0.00 N/m 273.20 KDB

Datasets

  1. Viscosity, Pa*s (2)
  2. Kinematic viscosity, m2/s (1)
  3. Mass density, kg/m3 (1)
  4. Mass density, kg/m3 (10)
  5. Speed of sound, m/s (1)
  6. Thermal conductivity, W/m/K (1)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Viscosity, Pa*s - Gas
298.15 604.50 0.0000
298.15 498.50 0.0000
298.15 402.90 0.0000
298.15 303.30 0.0000
298.15 204.60 0.0000
298.15 100.80 0.0000
323.16 598.70 0.0000
323.16 500.40 0.0000
323.16 400.70 0.0000
323.16 304.90 0.0000
323.16 200.90 0.0000
323.16 151.60 0.0000
323.16 100.80 0.0000
373.16 802.60 0.0000
373.16 604.90 0.0000
373.16 399.90 0.0000
373.16 296.80 0.0000
373.16 201.10 0.0000
373.16 151.40 0.0000
373.16 100.40 0.0000
423.14 998.90 0.0000
423.14 800.80 0.0000
423.14 600.40 0.0000
423.14 397.60 0.0000
423.14 302.00 0.0000
423.14 204.10 0.0000
423.14 153.30 0.0000
423.14 100.20 0.0000
473.15 1200.90 0.0000
473.15 997.80 0.0000
473.15 803.00 0.0000
473.15 601.10 0.0000
473.15 403.50 0.0000
473.15 202.50 0.0000
473.15 153.00 0.0000
473.16 100.10 0.0000
253.15 401.40 0.0000
253.15 300.50 0.0000
253.15 200.50 0.0000
253.15 153.00 0.0000
253.15 100.20 0.0000
273.17 502.80 0.0000
273.17 399.40 0.0000
273.17 301.70 0.0000
273.17 203.40 0.0000
273.17 151.80 0.0000
273.17 100.40 0.0000
298.15 502.80 0.0000
298.15 400.00 0.0000
298.15 303.20 0.0000
298.15 201.60 0.0000
298.15 150.40 0.0000
298.15 100.80 0.0000
298.15 499.70 0.0000
Reference
Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Viscosity, Pa*s - Gas
308.20 1200.00 0.0000
308.20 2070.00 0.0000
308.20 11330.00 0.0001
308.20 22090.00 0.0001
308.20 34970.00 0.0001
308.20 68930.00 0.0001
308.20 101200.00 0.0002
308.20 150520.00 0.0002
323.20 1270.00 0.0000
323.20 2050.00 0.0000
323.20 5040.00 0.0000
323.20 11440.00 0.0000
323.20 20670.00 0.0001
323.20 50820.00 0.0001
323.20 105530.00 0.0002
323.20 150430.00 0.0002
Reference

Kinematic viscosity, m2/s

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Kinematic viscosity, m2/s - Gas
220.00 195.46 2.3670e-06
220.00 226.71 2.0030e-06
220.00 254.44 1.7918e-06
220.00 288.21 1.5567e-06
220.00 324.47 1.3750e-06
220.00 362.71 1.2250e-06
220.00 393.15 1.1195e-06
220.00 425.51 1.0287e-06
220.00 449.74 9.6990e-07
220.00 479.78 9.0190e-07
235.00 224.78 2.3120e-06
235.00 359.42 1.4232e-06
235.00 452.88 1.1143e-06
235.00 545.18 9.1340e-07
235.00 638.46 7.6650e-07
235.00 723.88 6.7080e-07
235.00 803.31 5.9510e-07
250.00 274.20 2.1534e-06
250.00 372.33 1.5676e-06
250.00 491.25 1.1702e-06
250.00 595.84 9.5340e-07
250.00 702.28 7.9850e-07
250.00 818.89 6.7540e-07
250.00 953.03 5.7150e-07
250.00 1060.25 5.0650e-07
250.00 1177.57 4.4970e-07
250.00 1291.60 4.0310e-07
250.00 1438.24 3.5440e-07
270.00 196.61 3.5040e-06
270.00 354.95 1.9530e-06
270.00 526.01 1.2881e-06
270.00 705.02 9.4740e-07
270.00 898.25 7.2770e-07
270.00 1076.54 5.9890e-07
270.00 1287.09 4.9110e-07
270.00 1446.70 4.3090e-07
270.00 1630.02 3.7630e-07
270.00 1846.01 3.2620e-07
270.00 2079.64 2.8370e-07
270.00 2316.11 2.4940e-07
270.00 2509.61 2.2580e-07
285.00 371.48 2.0695e-06
285.00 575.25 1.3113e-06
285.00 787.74 9.4370e-07
285.00 1012.98 7.2170e-07
285.00 1228.51 5.8740e-07
285.00 1500.40 4.7160e-07
285.00 1707.23 4.0860e-07
285.00 1947.24 3.5240e-07
285.00 2221.25 3.0320e-07
285.00 2559.66 2.5760e-07
285.00 2841.89 2.2710e-07
285.00 3057.76 2.0620e-07
300.00 313.43 2.7182e-06
300.00 531.89 1.5815e-06
300.00 748.54 1.1095e-06
300.00 993.26 8.2570e-07
300.00 1237.01 6.5390e-07
300.00 1526.14 5.2160e-07
300.00 1747.76 4.5020e-07
300.00 1991.46 3.8990e-07
300.00 2272.21 3.3700e-07
300.00 2577.86 2.9160e-07
300.00 2893.94 2.5700e-07
300.00 3145.79 2.3340e-07
304.77 317.81 2.7820e-06
304.77 527.05 1.6498e-06
304.77 745.25 1.1528e-06
304.77 979.77 8.6610e-07
304.77 1201.73 6.9810e-07
304.77 1478.86 5.5930e-07
304.77 1699.38 4.8160e-07
304.77 1949.98 4.1420e-07
304.77 2235.18 3.5660e-07
304.77 2552.72 3.0720e-07
304.77 2881.02 2.6860e-07
304.77 3135.88 2.4410e-07
310.00 342.08 2.6610e-06
310.00 552.05 1.6300e-06
310.00 773.76 1.1495e-06
310.00 1018.04 8.6350e-07
310.00 1259.27 6.8960e-07
310.00 1549.04 5.5330e-07
310.00 1786.58 4.7450e-07
310.00 2055.58 4.0750e-07
310.00 2362.96 3.4940e-07
310.00 2708.78 3.0030e-07
310.00 3077.99 2.6050e-07
330.00 201.27 5.1680e-06
330.00 402.42 2.5505e-06
330.00 626.86 1.6211e-06
330.00 846.53 1.1907e-06
330.00 1059.35 9.4440e-07
330.00 1332.98 7.4280e-07
330.00 1559.26 6.2980e-07
330.00 1813.09 5.3710e-07
330.00 2103.20 4.5860e-07
330.00 2423.40 3.9430e-07
330.00 2778.74 3.3960e-07
330.00 3067.62 3.0590e-07
350.00 234.16 4.9710e-06
350.00 440.84 2.6127e-06
350.00 660.10 1.7308e-06
350.00 905.02 1.2532e-06
350.00 1143.54 9.8560e-07
350.00 1347.77 8.3120e-07
350.00 1584.41 7.0260e-07
350.00 1872.95 5.9010e-07
350.00 2228.51 4.9200e-07
350.00 2447.32 4.4510e-07
350.00 2827.17 3.8190e-07
350.00 3133.84 3.4210e-07
370.00 335.49 3.8230e-06
370.00 537.70 2.3746e-06
370.00 749.31 1.6966e-06
370.00 964.83 1.3150e-06
370.00 1228.54 1.0256e-06
370.00 1449.30 8.6650e-07
370.00 1714.08 7.2880e-07
370.00 2019.04 6.1490e-07
370.00 2382.70 5.1790e-07
370.00 2771.65 4.4220e-07
370.00 3095.89 3.9340e-07
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Mass density, kg/m3 - Gas
273.15 1001.00 21.2
273.15 2001.00 45.7
273.15 3001.00 77.3
273.15 3300.00 89.9
283.15 1000.00 20.4
283.15 2001.00 43.1
283.15 3001.00 70.9
283.15 4000.00 108.4
283.15 4400.00 130.1
293.15 1011.00 19.8
293.15 2001.00 41.0
293.15 3001.00 66.2
293.15 4000.00 97.3
293.15 5000.00 140.4
293.15 5600.00 182.2
Reference

Mass density, kg/m3

Fixed Measured
Pressure, kPa - Fluid (supercritical or subcritical phases) Temperature, K - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
6100.00 291.30 817.0
7100.00 291.50 834.0
8100.00 291.70 849.0
9200.00 291.90 861.0
10200.00 292.00 872.0
15200.00 292.10 916.0
20200.00 292.10 948.0
25300.00 292.10 975.0
30100.00 292.10 997.0
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
323.20 10968.00 497.981
323.25 12967.00 633.58
323.24 14966.00 698.2
323.25 16965.00 739.597
323.24 18962.00 770.445
323.26 20966.00 795.018
323.25 22962.00 815.681
323.24 24961.00 833.514
323.25 26959.00 849.181
323.25 28037.00 856.967
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
308.00 10000.00 714.84
308.00 12000.00 768.42
308.00 15000.00 816.06
308.00 18000.00 848.87
308.00 21000.00 874.4
318.00 10000.00 502.57
318.00 12000.00 659.73
318.00 15000.00 743.17
318.00 18000.00 790.18
318.00 21000.00 823.71
328.00 10000.00 326.4
328.00 12000.00 506.85
328.00 15000.00 654.94
328.00 18000.00 724.13
328.00 21000.00 768.74
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
304.29 10390.00 768.95
398.60 20324.00 391.9
469.77 20740.00 272.48
304.29 21349.00 895.09
304.29 31385.00 950.66
469.78 36325.00 466.7
398.62 36685.00 645.59
398.62 36789.00 646.63
304.29 42233.00 992.73
398.61 52521.00 764.26
469.73 54964.00 621.41
304.29 56603.00 1034.73
304.29 69065.00 1063.89
469.74 69479.00 702.01
398.61 70281.00 846.15
304.30 86449.00 1097.67
398.61 86718.00 900.46
469.75 86961.00 773.96
469.74 103717.00 827.38
398.61 103727.00 944.72
469.74 103847.00 827.75
304.30 104549.00 1127.06
469.76 116457.00 861.27
398.61 118142.00 975.99
304.30 119826.00 1148.82
398.62 119829.00 979.32
304.30 136467.00 1169.87
469.76 137604.00 908.75
398.62 137833.00 1012.46
Reference
Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
10000.00 303.15 770.5
20000.00 303.15 890.1
30000.00 303.15 949.2
40000.00 303.15 989.1
50000.00 303.15 1020.0
60000.00 303.15 1045.8
70000.00 303.15 1068.0
10000.00 313.15 628.9
20000.00 313.15 839.3
30000.00 313.15 909.2
40000.00 313.15 955.5
50000.00 313.15 990.5
60000.00 313.15 1019.0
70000.00 313.15 1043.5
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
310.00 1998.00 37.614
310.00 5002.00 116.171
310.00 10014.00 686.16
310.00 19987.00 856.152
310.00 29966.00 921.817
310.00 49929.00 999.875
310.00 75042.00 1062.566
310.00 100055.00 1108.29
310.00 125012.00 1144.813
310.00 139289.00 1162.991
310.00 149970.00 1175.569
310.00 159844.00 1186.558
350.00 2011.00 32.349
350.00 5001.00 89.638
350.00 9986.00 228.244
350.00 19981.00 613.586
350.00 30013.00 758.897
350.00 50017.00 884.809
350.00 74904.00 969.636
350.00 99977.00 1027.564
350.00 124895.00 1071.804
400.00 999.00 13.455
400.00 1998.00 27.43
400.00 4998.00 72.779
400.00 10021.00 161.96
400.00 14986.00 267.104
400.00 20028.00 381.082
400.00 25054.00 482.518
400.00 29994.00 561.435
400.00 35005.00 623.368
400.00 39985.00 672.037
400.00 49967.00 745.445
400.00 59920.00 799.163
400.00 69997.00 842.031
400.00 79880.00 876.766
400.00 89950.00 906.957
400.00 99838.00 932.857
400.00 109931.00 956.349
400.00 120079.00 977.599
400.00 126010.00 989.102
400.00 139527.00 1013.251
450.00 4998.00 62.269
450.00 9998.00 131.635
450.00 19983.00 284.802
450.00 29992.00 430.142
450.00 49933.00 626.132
450.00 75024.00 762.158
450.00 99833.00 847.163
450.00 122193.00 903.768
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
343.13 761.77 12.0399
343.13 761.77 12.0258
343.13 405.34 6.3329
343.13 405.34 6.3325
343.13 214.49 3.3311
343.13 2584.25 43.5107
343.13 4543.03 82.704
343.13 214.49 3.3345
343.13 2584.25 43.3646
343.13 4543.03 82.3364
343.13 5888.24 114.0166
343.13 5888.24 113.4483
343.13 556.21 8.7319
343.13 1040.75 16.6004
343.13 1416.95 22.8886
343.13 1919.84 31.5581
343.13 7469.20 157.1781
343.13 556.21 8.7265
343.13 1040.75 16.5719
343.13 1416.95 22.8367
343.13 1919.84 31.4693
343.13 7469.20 156.3104
343.13 295.01 4.5929
343.13 3447.34 59.9881
343.13 295.01 4.5951
343.13 3447.34 59.7539
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
313.15 340.00 8.2
313.15 690.00 15.1
313.15 1030.00 21.4
313.15 1380.00 26.7
313.15 1720.00 34.2
313.15 2070.00 38.6
313.15 2410.00 48.4
313.15 2760.00 56.7
313.15 3100.00 64.1
313.15 3450.00 72.9
313.15 3800.00 80.9
313.15 4140.00 87.5
313.15 4480.00 99.4
313.15 4830.00 109.8
313.15 5170.00 122.0
313.15 5510.00 134.0
313.15 5860.00 145.4
313.15 6200.00 158.0
313.15 6550.00 175.1
313.15 6890.00 194.5
313.15 7240.00 218.9
313.15 7580.00 239.9
313.15 7930.00 272.8
313.15 8270.00 315.6
313.15 8620.00 383.1
313.15 8960.00 478.5
313.15 9310.00 554.1
313.15 9650.00 599.1
313.15 10000.00 630.0
313.15 10340.00 649.1
313.15 10690.00 667.8
313.15 11030.00 682.9
313.15 11380.00 696.2
313.15 11720.00 708.0
313.15 12070.00 718.3
313.15 12410.00 727.4
313.15 12750.00 737.3
313.15 13100.00 744.1
313.15 13440.00 751.0
313.15 13790.00 757.9
313.15 14130.00 765.3
313.15 14480.00 770.0
313.15 14820.00 775.9
313.15 15160.00 781.5
313.15 15510.00 786.4
313.15 15860.00 791.7
313.15 16200.00 796.1
313.15 16550.00 801.2
313.15 16900.00 805.8
313.15 17240.00 809.8
333.15 340.00 7.7
333.15 690.00 13.4
333.15 1030.00 19.9
333.15 1380.00 25.1
333.15 1720.00 31.9
333.15 2070.00 38.4
333.15 2410.00 44.1
333.15 2760.00 51.2
333.15 3100.00 59.1
333.15 3450.00 65.1
333.15 3800.00 73.1
333.15 4140.00 79.7
333.15 4480.00 87.9
333.15 4830.00 96.5
333.15 5170.00 105.1
333.15 5510.00 114.2
333.15 5860.00 123.8
333.15 6200.00 133.4
333.15 6550.00 144.2
333.15 6890.00 154.3
333.15 7240.00 166.4
333.15 7580.00 178.8
333.15 7930.00 190.1
333.15 8270.00 205.2
333.15 8620.00 219.5
333.15 8960.00 235.1
333.15 9310.00 252.4
333.15 9650.00 271.0
333.15 10000.00 291.4
333.15 10340.00 313.6
333.15 10690.00 337.0
333.15 11030.00 361.9
333.15 11380.00 388.0
333.15 11720.00 411.1
333.15 12070.00 437.9
333.15 12410.00 463.8
333.15 12750.00 489.2
333.15 13100.00 510.1
333.15 13440.00 530.7
333.15 13790.00 549.9
333.15 14130.00 567.7
333.15 14480.00 582.0
333.15 14820.00 596.0
333.15 15160.00 609.4
333.15 15510.00 621.0
333.15 15860.00 627.4
333.15 16200.00 642.1
333.15 16550.00 651.8
333.15 16900.00 661.7
333.15 17240.00 669.7
353.15 340.00 7.4
353.15 690.00 13.5
353.15 1030.00 18.8
353.15 1380.00 24.6
353.15 1720.00 31.4
353.15 2070.00 36.1
353.15 2410.00 41.9
353.15 2760.00 48.0
353.15 3100.00 54.1
353.15 3450.00 61.4
353.15 3800.00 67.2
353.15 4140.00 73.8
353.15 4480.00 80.5
353.15 4830.00 88.0
353.15 5170.00 94.9
353.15 5510.00 102.4
353.15 5860.00 110.2
353.15 6200.00 118.0
353.15 6550.00 126.2
353.15 6890.00 134.4
353.15 7240.00 143.4
353.15 7580.00 152.1
353.15 7930.00 161.4
353.15 8270.00 171.1
353.15 8620.00 180.8
353.15 8960.00 191.1
353.15 9310.00 201.8
353.15 9650.00 211.9
353.15 10000.00 223.5
353.15 10340.00 235.0
353.15 10690.00 247.4
353.15 11030.00 259.8
353.15 11380.00 272.4
353.15 11720.00 283.9
353.15 12070.00 298.3
353.15 12410.00 312.1
353.15 12750.00 328.4
353.15 13100.00 342.0
353.15 13440.00 356.7
353.15 13790.00 372.8
353.15 14130.00 388.6
353.15 14480.00 403.0
353.15 14820.00 417.8
353.15 15160.00 433.0
353.15 15510.00 447.5
353.15 15860.00 461.0
353.15 16200.00 475.0
353.15 16550.00 488.1
353.15 16900.00 501.0
353.15 17240.00 513.0
373.15 340.00 6.5
373.15 690.00 10.9
373.15 1030.00 17.1
373.15 1380.00 23.2
373.15 1720.00 28.6
373.15 2070.00 32.7
373.15 2410.00 39.2
373.15 2760.00 44.8
373.15 3100.00 50.3
373.15 3450.00 56.1
373.15 3800.00 63.2
373.15 4140.00 67.9
373.15 4480.00 73.1
373.15 4830.00 80.0
373.15 5170.00 86.2
373.15 5510.00 93.0
373.15 5860.00 99.2
373.15 6200.00 106.0
373.15 6550.00 112.9
373.15 6890.00 120.0
373.15 7240.00 127.0
373.15 7580.00 135.4
373.15 7930.00 143.1
373.15 8270.00 151.1
373.15 8620.00 158.1
373.15 8960.00 166.1
373.15 9310.00 174.4
373.15 9650.00 182.7
373.15 10000.00 191.9
373.15 10340.00 199.4
373.15 10690.00 208.4
373.15 11030.00 217.3
373.15 11380.00 223.2
373.15 11720.00 233.1
373.15 12070.00 242.8
373.15 12410.00 252.7
373.15 12750.00 262.8
373.15 13100.00 272.5
373.15 13440.00 283.1
373.15 13790.00 293.1
373.15 14130.00 304.7
373.15 14480.00 314.9
373.15 14820.00 325.0
373.15 15160.00 336.1
373.15 15510.00 347.6
373.15 15860.00 358.1
373.15 16200.00 368.7
373.15 16550.00 379.8
373.15 16900.00 390.2
373.15 17240.00 400.4
393.15 340.00 5.7
393.15 690.00 9.5
393.15 1030.00 16.3
393.15 1380.00 22.1
393.15 1720.00 26.9
393.15 2070.00 32.0
393.15 2410.00 37.0
393.15 2760.00 47.5
393.15 3100.00 47.4
393.15 3450.00 52.9
393.15 3800.00 58.2
393.15 4140.00 63.6
393.15 4480.00 69.2
393.15 4830.00 74.7
393.15 5170.00 80.4
393.15 5510.00 86.2
393.15 5860.00 92.4
393.15 6200.00 98.1
393.15 6550.00 104.7
393.15 6890.00 110.5
393.15 7240.00 113.6
393.15 7580.00 123.1
393.15 7930.00 129.9
393.15 8270.00 136.2
393.15 8620.00 142.9
393.15 8960.00 149.4
393.15 9310.00 156.2
393.15 9650.00 163.2
393.15 10000.00 170.4
393.15 10340.00 176.4
393.15 10690.00 183.2
393.15 11030.00 191.1
393.15 11380.00 198.2
393.15 11720.00 203.9
393.15 12070.00 210.8
393.15 12410.00 218.0
393.15 12750.00 226.3
393.15 13100.00 234.0
393.15 13440.00 242.1
393.15 13790.00 250.9
393.15 14130.00 258.0
393.15 14480.00 266.4
393.15 14820.00 275.0
393.15 15160.00 283.9
393.15 15510.00 291.1
393.15 15860.00 300.7
393.15 16200.00 308.4
393.15 16550.00 316.8
393.15 16900.00 325.1
393.15 17240.00 333.1
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
308.15 10000.00 717.2
308.15 15000.00 816.1
308.15 20000.00 866.1
308.15 30000.00 929.0
308.15 40000.00 971.7
313.15 10000.00 636.6
313.15 15000.00 781.3
313.15 20000.00 840.2
313.15 30000.00 909.7
313.15 40000.00 955.5
323.15 10000.00 397.3
323.15 15000.00 701.8
323.15 20000.00 784.9
323.15 30000.00 870.3
323.15 40000.00 922.8
333.15 10000.00 296.1
333.15 15000.00 607.0
333.15 20000.00 724.4
333.15 30000.00 829.6
333.15 40000.00 889.8
Reference
Fixed Measured
Pressure, kPa - Fluid (supercritical or subcritical phases) Temperature, K - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
10000.00 313.00 570.0
15000.00 313.00 780.0
20000.00 308.00 870.0
20000.00 313.00 850.0
20000.00 318.00 820.0
20000.00 323.00 790.0
20000.00 328.00 760.0
20000.00 333.00 730.0
20000.00 313.00 830.0
25000.00 313.00 890.0
36000.00 313.00 900.0
Reference

Speed of sound, m/s

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Speed of sound, m/s - Gas
260.00 884.92 242.761
260.00 822.03 243.577
260.00 760.19 244.37
260.00 701.21 245.119
260.00 626.77 246.054
260.00 562.69 246.845
260.00 501.31 247.598
260.00 434.17 248.411
260.00 379.95 249.058
260.00 317.37 249.804
270.00 977.38 247.218
270.00 906.73 248.028
270.00 819.89 249.014
270.00 732.10 249.996
270.00 644.89 250.959
270.00 556.68 251.923
270.00 460.73 252.96
270.00 362.27 254.006
270.00 305.05 254.606
280.00 981.82 252.563
280.00 884.20 253.546
280.00 798.98 254.394
280.00 692.20 255.443
280.00 621.46 256.133
280.00 537.04 256.947
280.00 453.25 257.75
280.00 362.38 258.608
280.00 280.31 259.377
290.00 819.49 259.125
290.00 733.65 259.876
290.00 655.16 260.559
290.00 571.60 261.28
290.00 490.56 261.978
290.00 421.86 262.559
290.00 355.64 263.124
290.00 282.86 263.732
290.00 228.71 264.19
300.00 1017.33 262.36
300.00 927.15 263.073
300.00 847.25 263.703
300.00 755.49 264.422
300.00 663.90 265.134
300.00 583.49 265.756
300.00 500.85 266.392
300.00 415.37 267.046
300.00 340.26 267.619
300.00 280.85 268.065
304.09 968.58 264.694
304.09 868.88 265.446
304.09 772.25 266.17
304.09 544.65 267.858
304.09 434.91 268.664
312.75 959.38 268.804
312.75 858.54 269.494
312.75 729.55 270.371
312.75 636.23 271.003
312.75 534.77 271.688
312.75 441.68 272.312
312.75 394.20 272.63
322.75 929.78 273.533
322.75 832.63 274.131
322.75 735.59 274.723
322.75 624.83 275.397
322.75 522.36 276.021
322.75 412.26 276.687
322.75 314.03 277.276
332.75 958.15 277.777
332.75 857.33 278.334
332.75 755.50 278.895
332.75 664.72 279.393
332.75 544.84 280.054
332.75 520.66 280.185
332.75 415.50 280.761
332.75 316.28 281.299
Reference

Thermal conductivity, W/m/K

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Thermal conductivity, W/m/K - Gas
298.89 6100.00 0.0331
299.02 5760.00 0.0290
299.19 5400.00 0.0263
299.31 5035.00 0.0244
299.50 4555.00 0.0227
299.60 3980.00 0.0211
299.73 3285.00 0.0197
299.85 2555.00 0.0186
300.06 1702.00 0.0178
300.37 714.00 0.0171
302.67 6635.00 0.0370
302.77 6400.00 0.0331
302.80 6025.00 0.0290
302.86 5675.00 0.0269
302.92 5290.00 0.0247
302.97 4870.00 0.0234
303.08 4340.00 0.0218
303.22 3765.00 0.0205
303.51 3160.00 0.0196
303.81 2415.00 0.0187
303.99 1612.00 0.0180
304.21 724.00 0.0174
324.87 7960.00 0.0321
324.90 7750.00 0.0312
324.92 7440.00 0.0295
324.95 5960.00 0.0250
325.01 6900.00 0.0277
325.04 6760.00 0.0272
325.10 5575.00 0.0243
325.12 6360.00 0.0261
325.28 5060.00 0.0232
325.42 4605.00 0.0225
325.48 4040.00 0.0218
325.64 3500.00 0.0213
325.81 2880.00 0.0205
325.93 2218.00 0.0200
326.03 1514.00 0.0196
326.17 684.00 0.0192
326.26 497.00 0.0191
350.83 9985.00 0.0332
350.89 8840.00 0.0303
350.96 7540.00 0.0277
351.12 6040.00 0.0255
351.44 4275.00 0.0235
351.82 2214.00 0.0220
351.87 1820.00 0.0218
351.91 1420.00 0.0215
352.10 994.00 0.0214
352.23 572.00 0.0214
375.68 14930.00 0.0418
375.71 13880.00 0.0389
375.75 12560.00 0.0362
375.80 11100.00 0.0332
375.85 9640.00 0.0308
375.91 8060.00 0.0289
376.01 6260.00 0.0267
376.11 4240.00 0.0250
376.28 2004.00 0.0238
376.51 1015.00 0.0235
400.85 15010.00 0.0384
400.93 13550.00 0.0362
400.98 11950.00 0.0339
401.03 10340.00 0.0319
401.15 8495.00 0.0300
401.30 6660.00 0.0285
401.42 4600.00 0.0271
401.60 2382.00 0.0260
401.66 1690.00 0.0258
401.74 975.00 0.0257
427.12 12000.00 0.0343
427.23 9898.00 0.0325
427.38 8240.00 0.0313
427.51 6160.00 0.0297
427.67 3970.00 0.0288
427.70 3020.00 0.0283
427.95 2050.00 0.0281
428.05 1040.00 0.0280
Reference

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 6891.42] kPa [153.41; 264.19] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A2.05818e+01
Coefficient B-3.08771e+03
Coefficient C-1.26700e+00
Temperature range, min.153.41
Temperature range, max.264.19
Pvap 1.33 kPa 153.41 Calculated Property
Pvap 6.09 kPa 165.72 Calculated Property
Pvap 22.50 kPa 178.03 Calculated Property
Pvap 70.16 kPa 190.34 Calculated Property
Pvap 190.37 kPa 202.65 Calculated Property
Pvap 460.43 kPa 214.95 Calculated Property
Pvap 1011.47 kPa 227.26 Calculated Property
Pvap 2048.49 kPa 239.57 Calculated Property
Pvap 3870.88 kPa 251.88 Calculated Property
Pvap 6891.42 kPa 264.19 Calculated Property

Similar Compounds

CO2+. Carbon monoxide. Formyl radical. Carbonyl sulfide. Methyl-d1 radical, oxo-. Dicarbon monoxide. Isocyanato radical. Dicarbon monoxide. Phosphorus mononitride. Formaldehyde. Carbonic difluoride. methanal-d. Phosgene. Hydrocarboxyl radical. 1,2-Propadiene-1,3-dione.

Find more compounds similar to Carbon dioxide.

Mixtures

Find more mixtures with Carbon dioxide.

Sources

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