Contents
Physical Properties
Temperature Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Cheméo can also estimate Critical Temperature , Critical Pressure , Critical Volume , Enthalpy of formation at standard conditions , Standard Gibbs free energy of formation , Acentric Factor , Log10 of Water solubility in mol/l
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Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[274.36; 365.49]
J/mol×K
[445.66; 654.83]
Cp,gas
274.36
J/mol×K
445.66
Joback Calculated Property
Cp,gas
292.47
J/mol×K
480.52
Joback Calculated Property
Cp,gas
309.23
J/mol×K
515.38
Joback Calculated Property
Cp,gas
324.78
J/mol×K
550.25
Joback Calculated Property
Cp,gas
339.25
J/mol×K
585.11
Joback Calculated Property
Cp,gas
352.77
J/mol×K
619.97
Joback Calculated Property
Cp,gas
365.49
J/mol×K
654.83
Joback Calculated Property
η
[0.0006350; 0.0016760]
Pa×s
[283.15; 353.15]
η
0.0016760
Pa×s
283.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0014090
Pa×s
293.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0013030
Pa×s
298.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0012030
Pa×s
303.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0010390
Pa×s
313.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0009080
Pa×s
323.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0008040
Pa×s
333.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0007100
Pa×s
343.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
η
0.0006350
Pa×s
353.15
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
Pvap
[100.70; 101.33]
kPa
[428.64; 428.65]
Pvap
101.33
kPa
428.64
Measurement and correlation of vapor-liquid equilibrium data for binary systems composed of camphene, (+)-3-carene, (-)-beta-caryophyllene, p-cymene, and alpha-pinene at 101.33 kPa
Pvap
100.70
kPa
428.65
Measurement and correlation of (vapor + liquid) equilibrium data for {alpha-pinene + p-cymene + (S)-(-)-limonene} ternary system at atmospheric pressure
Pvap
101.33
kPa
428.65
Measurement and correlation of vapor-liquid equilibrium data for binary systems composed of camphene, (+)-3-carene, (-)-beta-caryophyllene, p-cymene, and alpha-pinene at 101.33 kPa
n 0
[1.45420; 1.46570]
[293.15; 318.15]
n 0
1.46570
293.15
Vapor-Liquid Equilibria for the Binary Mixture alpha-Pinene + Octane
n 0
1.46260
298.15
Excess Molar Enthalpies of p-Cymene + r-Pinene + a-Pinene at (298.15, 308.15, and 318.15) K and at Atmospheric Pressure
n 0
1.45810
308.15
Excess Molar Enthalpies of p-Cymene + r-Pinene + a-Pinene at (298.15, 308.15, and 318.15) K and at Atmospheric Pressure
n 0
1.45420
318.15
Excess Molar Enthalpies of p-Cymene + r-Pinene + a-Pinene at (298.15, 308.15, and 318.15) K and at Atmospheric Pressure
ρl
853.88
kg/m3
298.15
Temperature Dependence on Mutual Solubility Data of the Binary (Methanol + r-Pinene or -Pinene) Systems and Ternary Liquid-Liquid Equilibria for the (Methanol + Ethanol + r-Pinene or -Pinene) Systems
Datasets
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
20000.00
880.0
283.15
25000.00
883.2
283.15
30000.00
886.3
283.15
35000.00
889.4
283.15
40000.00
892.5
298.15
20000.00
868.8
298.15
25000.00
872.1
298.15
30000.00
875.3
298.15
35000.00
878.6
298.15
40000.00
881.9
313.15
20000.00
858.0
313.15
25000.00
861.3
313.15
30000.00
864.7
313.15
35000.00
867.9
313.15
40000.00
871.3
328.15
20000.00
846.7
328.15
25000.00
850.4
328.15
30000.00
854.0
328.15
35000.00
857.5
328.15
40000.00
861.1
343.15
20000.00
835.9
343.15
25000.00
839.7
343.15
30000.00
843.8
343.15
35000.00
847.7
343.15
40000.00
851.4
358.15
20000.00
825.0
358.15
25000.00
829.2
358.15
30000.00
833.3
358.15
35000.00
837.4
358.15
40000.00
841.5
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
20000.00
880.0
283.15
25000.00
883.2
283.15
30000.00
886.3
283.15
35000.00
889.4
283.15
40000.00
892.5
298.15
20000.00
868.8
298.15
25000.00
872.1
298.15
30000.00
875.3
298.15
35000.00
878.6
298.15
40000.00
881.9
313.15
20000.00
858.0
313.15
25000.00
861.3
313.15
30000.00
864.7
313.15
35000.00
867.9
313.15
40000.00
871.3
328.15
20000.00
846.7
328.15
25000.00
850.4
328.15
30000.00
854.0
328.15
35000.00
857.5
328.15
40000.00
861.1
343.15
20000.00
835.9
343.15
25000.00
839.7
343.15
30000.00
843.8
343.15
35000.00
847.7
343.15
40000.00
851.4
358.15
20000.00
825.0
358.15
25000.00
829.2
358.15
30000.00
833.3
358.15
35000.00
837.4
358.15
40000.00
841.5
Reference
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.67]
kPa
[308.97; 460.34]
The Yaws Handbook of Vapor Pressure
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.41883e+01 Coefficient B -3.71789e+03 Coefficient C -4.15050e+01 Temperature range, min. 308.97
Temperature range, max. 460.34
Pvap
1.33
kPa
308.97
Calculated Property
Pvap
3.04
kPa
325.79
Calculated Property
Pvap
6.30
kPa
342.61
Calculated Property
Pvap
12.11
kPa
359.43
Calculated Property
Pvap
21.79
kPa
376.25
Calculated Property
Pvap
37.07
kPa
393.06
Calculated Property
Pvap
60.08
kPa
409.88
Calculated Property
Pvap
93.36
kPa
426.70
Calculated Property
Pvap
139.80
kPa
443.52
Calculated Property
Pvap
202.67
kPa
460.34
Calculated Property
Similar Compounds
Find more compounds similar to «alpha»-Pinene .
Mixtures
Sources
Cheméo Relay (1.0)
Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
Crippen Method
Crippen Method
Isothermal and isobaric (vapour + liquid) equilibria of (alpha-pinene + n-butanol + n-octane)
(Ternary liquid + liquid) equilibria for (water + acetone + alpha-pinene, or beta-pinene, or limonene) mixtures
Ternary (liquid + liquid) equilibria for (water + 2-propanol + a-pinene, or a-pinene) mixtures at four temperatures
P,[rho], T and heat capacity measurements of ([alpha]-pinene + [beta]-pinene) mixtures over the temperature range 283.15 K to 358.15 K and pressures up to 40 MPa: Experiments and modelling
Measurement and correlation of (vapor + liquid) equilibrium data for {alpha-pinene + p-cymene + (S)-(-)-limonene} ternary system at atmospheric pressure
Measurement and correlation of vapor-liquid equilibrium data for binary systems composed of camphene, (+)-3-carene, (-)-beta-caryophyllene, p-cymene, and alpha-pinene at 101.33 kPa
Vapor-Liquid Equilibria for the Binary Mixture alpha-Pinene + Octane
Excess Molar Enthalpies of p-Cymene + r-Pinene + a-Pinene at (298.15, 308.15, and 318.15) K and at Atmospheric Pressure
P, rho, and T Measurements of the Limonene + alpha-Pinene Mixtures
Liquid-Liquid Equilibria of Water + Pentan-1-ol + 2,6,6-Trimethylbicyclo[3.1.1]hep-2-ene or 6,6-Dimethyl-2-methylenebicyclo[3.1.1]heptane at (293.15, 303.15, 313.15, and 323.15) K
Vapor Liquid Equilibria Measurements of Bitter Orange Aroma Compounds Highly Diluted in Boiling Hydro-Alcoholic Solutions at 101.3 kPa
Temperature Dependence on Mutual Solubility Data of the Binary (Methanol + r-Pinene or -Pinene) Systems and Ternary Liquid-Liquid Equilibria for the (Methanol + Ethanol + r-Pinene or -Pinene) Systems
Density, Viscosity, and Refractive Index in the Range (283.15 to 353.15) K and Vapor Pressure of r-Pinene, d-Limonene, (()-Linalool, and Citral Over the Pressure Range 1.0 kPa Atmospheric Pressure
Joback Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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