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
EA
-0.60
eV
NIST
EA
-1.60 ± 0.10
eV
NIST
Δf G°
-394.60
kJ/mol
KDB
Rg
0.9920
KDB
Δf H°gas
[-393.80; -393.51]
kJ/mol
Δf H°gas
-393.80
kJ/mol
KDB
Δf H°gas
-393.51 ± 0.13
kJ/mol
NIST
Δfus H°
11.09
kJ/mol
Joback Calculated Property
Δvap H°
13.60
kJ/mol
Relay (1.0) Calculated Property
IE
[13.00; 13.90]
eV
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
log 10 WS
0.72
Relay (1.0) Calculated Property
log Poct/wat
-0.584
Crippen Calculated Property
McVol
28.090
ml/mol
McGowan Calculated Property
Pc
[7340.00; 7420.00]
kPa
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
Ptriple
518.50
kPa
KDB
Ptriple
518.50 ± 0.50
kPa
NIST
ρc
[466.06; 475.30]
kg/m3
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]
Inp
154.00
NIST
Inp
153.00
NIST
Inp
152.00
NIST
Inp
152.00
NIST
S°gas,1 bar
213.78 ± 0.01
J/mol×K
NIST
Tboil
194.70
K
KDB
Tc
[304.10; 304.35]
K
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
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
Vc
0.094
m3 /kmol
KDB
Vc
0.092 ± 0.001
m3 /kmol
NIST
Zc
0.2741450
KDB
Zra
0.27
KDB
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[32.51; 42.55]
J/mol×K
[203.15; 331.33]
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]
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
Δsub H
[25.20; 27.20]
kJ/mol
[86.00; 207.00]
Δsub H
27.20 ± 0.40
kJ/mol
86.00
NIST
Δsub H
26.30
kJ/mol
167.00
NIST
Δsub H
25.20
kJ/mol
175.00
NIST
Δsub H
25.90
kJ/mol
188.50
NIST
Δsub H
26.10
kJ/mol
207.00
NIST
Δvap H
[15.33; 28.84]
kJ/mol
[82.30; 288.50]
Δvap H
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
Δvap H
15.33
kJ/mol
216.60
KDB
Δvap H
16.40
kJ/mol
244.50
NIST
Δvap H
16.50
kJ/mol
285.00
NIST
Δvap H
16.70
kJ/mol
288.50
NIST
Pvap
[410.40; 7360.50]
kPa
[213.22; 304.04]
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