- InChI
- InChI=1S/C10H14/c1-8(2)10-7-5-4-6-9(10)3/h4-8H,1-3H3
- InChI Key
- WWRCMNKATXZARA-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- Cc1ccccc1C(C)C
- Molecular Weight1
- 134.22
- CAS
- 527-84-4
- Other Names
-
- 1-(1-methylethyl)-2-methylbenzene
- 1-Isopropyl-2-methylbenzene
- 1-Methyl-2-(1-methylethyl)-benzene
- 1-Methyl-2-iso-propylbenzene
- 1-Methyl-2-isopropylbenzene
- 1-methyl,2-n-isopropylbenzene
- 1-methyl-2-propan-2-ylbenzene
- 2-Isopropyltoluene
- Benzene, 1-methyl-2-(1-methylethyl)-
- Cymene, ortho
- UN 2046
- o-Cymol
- o-Isopropyl-toluene
- o-Isopropyltoluene
- ortho-Cymene
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2769; 0.3690] |
|
|
| ω | 0.3690 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2769 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.2769 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | [-5862.62; -5859.90] | kJ/mol |
|
| ΔcH°liquid | -5862.62 ± 0.84 | kJ/mol | NIST |
| ΔcH°liquid | -5859.90 ± 2.20 | kJ/mol | NIST |
| μ | 0.60 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 137.36 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -25.61 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | [-76.10; -73.30] | kJ/mol |
|
| ΔfH°liquid | -73.30 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -76.10 ± 2.10 | kJ/mol | NIST |
| ΔfusH° | 11.79 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 50.60 | kJ/mol | NIST |
| IE | 8.40 | eV | Relay (1.0) Calculated Property |
| log10WS | [-3.76; -3.76] |
|
|
| log10WS | -3.76 | Aq. Solubility Prediction | |
| log10WS | -3.76 | Estimated Solubility | |
| logPoct/wat | 3.118 | Crippen Calculated Property | |
| McVol | 128.000 | ml/mol | McGowan Calculated Property |
| Pc | [2895.80; 2904.99] | kPa |
|
| Pc | 2904.99 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 2895.80 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 2895.87 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.77e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1001.00; 1051.30] |
|
|
| Inp | 1029.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1020.60 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | Outlier 1045.00 | NIST | |
| Inp | 1013.50 | NIST | |
| Inp | 1015.80 | NIST | |
| Inp | 1032.30 | NIST | |
| Inp | 1038.40 | NIST | |
| Inp | Outlier 1044.90 | NIST | |
| Inp | 1016.90 | NIST | |
| Inp | 1010.40 | NIST | |
| Inp | 1013.50 | NIST | |
| Inp | 1015.80 | NIST | |
| Inp | 1010.42 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1016.90 | NIST | |
| Inp | 1016.40 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1024.70 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | Outlier 1002.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | Outlier 1043.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1009.85 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1027.70 | NIST | |
| Inp | Outlier 1050.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1028.40 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1025.40 | NIST | |
| Inp | Outlier 1051.30 | NIST | |
| Inp | 1020.40 | NIST | |
| Inp | 1022.70 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | Outlier 1001.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | Outlier 1006.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | Outlier 1041.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1016.90 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | Outlier 1001.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1032.30 | NIST | |
| Inp | 1013.50 | NIST | |
| Inp | 1016.90 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Ip | [1248.00; 1334.00] |
|
|
| Ip | 1276.40 | NIST | |
| Ip | 1274.80 | NIST | |
| Ip | 1274.80 | NIST | |
| Ip | 1260.00 | NIST | |
| Ip | 1276.00 | NIST | |
| Ip | 1279.00 | NIST | |
| Ip | 1254.00 | NIST | |
| Ip | 1266.00 | NIST | |
| Ip | 1287.00 | NIST | |
| Ip | 1310.00 | NIST | |
| Ip | 1310.00 | NIST | |
| Ip | 1321.00 | NIST | |
| Ip | Outlier 1334.00 | NIST | |
| Ip | 1299.00 | NIST | |
| Ip | 1275.00 | NIST | |
| Ip | 1268.00 | NIST | |
| Ip | 1291.00 | NIST | |
| Ip | 1248.00 | NIST | |
| Ip | 1298.00 | NIST | |
| Ip | 1272.00 | NIST | |
| Ip | 1261.00 | NIST | |
| Ip | 1275.00 | NIST | |
| Ip | 1275.00 | NIST | |
| Ip | 1280.00 | NIST | |
| Ip | 1276.00 | NIST | |
| Ip | 1310.00 | NIST | |
| Ip | 1275.00 | NIST | |
| Ip | 1268.00 | NIST | |
| Ip | 1260.00 | NIST | |
| Tboil | [448.00; 451.50] | K |
|
| Tboil | 451.33 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 451.30 | K | NIST |
| Tboil | 451.00 ± 3.00 | K | NIST |
| Tboil | 451.00 ± 3.00 | K | NIST |
| Tboil | 451.28 ± 0.20 | K | NIST |
| Tboil | 451.38 ± 0.20 | K | NIST |
| Tboil | 451.50 ± 0.30 | K | NIST |
| Tboil | 451.33 ± 0.20 | K | NIST |
| Tboil | 451.28 ± 0.30 | K | NIST |
| Tboil | 451.28 ± 0.30 | K | NIST |
| Tboil | 448.00 ± 3.00 | K | NIST |
| Tboil | 450.40 ± 2.00 | K | NIST |
| Tboil | 450.40 ± 1.50 | K | NIST |
| Tboil | 451.50 ± 0.20 | K | NIST |
| Tboil | 451.50 ± 0.15 | K | NIST |
| Tboil | 451.50 ± 0.30 | K | NIST |
| Tboil | 448.20 ± 2.00 | K | NIST |
| Tboil | 449.00 ± 3.00 | K | NIST |
| Tboil | 448.00 ± 4.00 | K | NIST |
| Tboil | 448.00 ± 3.00 | K | NIST |
| Tc | [657.30; 670.15] | K |
|
| Tc | 657.30 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 669.82 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 670.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [188.95; 201.64] | K |
|
| Tfus | 201.40 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 201.64 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 201.40 | K | Aq. Solubility Prediction |
| Tfus | 197.91 ± 0.04 | K | NIST |
| Tfus | 201.58 ± 0.03 | K | NIST |
| Tfus | 201.58 ± 0.03 | K | NIST |
| Tfus | 201.61 ± 0.02 | K | NIST |
| Tfus | 191.62 ± 0.04 | K | NIST |
| Tfus | Outlier 188.95 ± 0.60 | K | NIST |
| Tfus | 201.44 ± 0.20 | K | NIST |
| Ttriple | 201.64 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.61 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.01 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.478; 0.490] | m3/kmol |
|
| Vc | 0.490 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.478 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2600000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 44.40 | kJ/mol | 403.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [162.89; 480.32] | J/mol×K | [273.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.05060e+02 | |||
| Coefficient B | -6.64900e+02 | |||
| Coefficient C | 6.52924e+00 | |||
| Coefficient D | -1.38260e-04 | |||
| Coefficient E | 2.17940e-08 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 162.89 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 233.05 | J/mol×K | 409.33 | Calculated Property |
| Cp,gas | 294.07 | J/mol×K | 545.67 | Calculated Property |
| Cp,gas | 342.56 | J/mol×K | 682.00 | Calculated Property |
| Cp,gas | 380.45 | J/mol×K | 818.33 | Calculated Property |
| Cp,gas | 410.16 | J/mol×K | 954.67 | Calculated Property |
| Cp,gas | 433.68 | J/mol×K | 1091.00 | Calculated Property |
| Cp,gas | 452.52 | J/mol×K | 1227.33 | Calculated Property |
| Cp,gas | 467.79 | J/mol×K | 1363.67 | Calculated Property |
| Cp,gas | 480.32 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [191.95; 312.34] | J/mol×K | [201.64; 451.33] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.30330e+02 | |||
| Coefficient B | -1.23140e+02 | |||
| Coefficient C | 3.67524e+00 | |||
| Coefficient D | 6.24640e-03 | |||
| Coefficient E | -4.99540e-06 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 451.33 | |||
| Cp,liquid | 191.95 | J/mol×K | 201.64 | Calculated Property |
| Cp,liquid | 204.65 | J/mol×K | 229.38 | Calculated Property |
| Cp,liquid | 217.88 | J/mol×K | 257.13 | Calculated Property |
| Cp,liquid | 231.52 | J/mol×K | 284.87 | Calculated Property |
| Cp,liquid | 245.44 | J/mol×K | 312.61 | Calculated Property |
| Cp,liquid | 259.45 | J/mol×K | 340.36 | Calculated Property |
| Cp,liquid | 273.37 | J/mol×K | 368.10 | Calculated Property |
| Cp,liquid | 286.98 | J/mol×K | 395.84 | Calculated Property |
| Cp,liquid | 300.05 | J/mol×K | 423.59 | Calculated Property |
| Cp,liquid | 312.34 | J/mol×K | 451.33 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0047230; 0.0001454] | Pa×s | [201.64; 600.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -8.16790e+00 | |||
| Coefficient B | 8.85640e+02 | |||
| Coefficient C | -2.91760e-01 | |||
| Coefficient D | -7.71610e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 600.00 | |||
| η | 0.0047230 | Pa×s | 201.64 | Calculated Property |
| η | 0.0019911 | Pa×s | 245.90 | Calculated Property |
| η | 0.0010754 | Pa×s | 290.16 | Calculated Property |
| η | 0.0006743 | Pa×s | 334.43 | Calculated Property |
| η | 0.0004657 | Pa×s | 378.69 | Calculated Property |
| η | 0.0003435 | Pa×s | 422.95 | Calculated Property |
| η | 0.0002654 | Pa×s | 467.21 | Calculated Property |
| η | 0.0002122 | Pa×s | 511.48 | Calculated Property |
| η | 0.0001740 | Pa×s | 555.74 | Calculated Property |
| η | 0.0001454 | Pa×s | 600.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [50.73; 10.34] | kJ/mol | [201.64; 657.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 8.44827e+01 | |||
| Coefficient B | 3.20572e+00 | |||
| Coefficient C | -8.33498e+00 | |||
| Coefficient D | 9.05519e+00 | |||
| Coefficient E | -3.39952e+00 | |||
| Critical temperature, Tc (K) | 6.70150e+02 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 657.00 | |||
| ΔvapH | 50.73 | kJ/mol | 201.64 | Calculated Property |
| ΔvapH | 48.62 | kJ/mol | 252.24 | Calculated Property |
| ΔvapH | 47.02 | kJ/mol | 302.83 | Calculated Property |
| ΔvapH | 45.36 | kJ/mol | 353.43 | Calculated Property |
| ΔvapH | 43.17 | kJ/mol | 404.02 | Calculated Property |
| ΔvapH | 40.08 | kJ/mol | 454.62 | Calculated Property |
| ΔvapH | 35.82 | kJ/mol | 505.21 | Calculated Property |
| ΔvapH | 30.17 | kJ/mol | 555.81 | Calculated Property |
| ΔvapH | 22.67 | kJ/mol | 606.40 | Calculated Property |
| ΔvapH | 10.34 | kJ/mol | 657.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.52e-05; 2896.52] | kPa | [201.64; 657.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 4.04152e+01 | |||
| Coefficient B | -6.53660e+03 | |||
| Coefficient C | -3.50740e+00 | |||
| Coefficient D | 6.02540e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 657.00 | |||
| Pvap | 2.52e-05 | kPa | 201.64 | Calculated Property |
| Pvap | 7.76e-03 | kPa | 252.24 | Calculated Property |
| Pvap | 0.32 | kPa | 302.83 | Calculated Property |
| Pvap | 4.12 | kPa | 353.43 | Calculated Property |
| Pvap | 26.72 | kPa | 404.02 | Calculated Property |
| Pvap | 109.75 | kPa | 454.62 | Calculated Property |
| Pvap | 329.39 | kPa | 505.21 | Calculated Property |
| Pvap | 790.46 | kPa | 555.81 | Calculated Property |
| Pvap | 1609.55 | kPa | 606.40 | Calculated Property |
| Pvap | 2896.52 | kPa | 657.00 | Calculated Property |
| Pvap | [8.77e-06; 2848.83] | kPa | [201.64; 662.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.51654e+01 | |||
| Coefficient B | -8.25896e+03 | |||
| Coefficient C | -8.66782e+00 | |||
| Coefficient D | 3.57058e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 662.00 | |||
| Pvap | 8.77e-06 | kPa | 201.64 | Calculated Property |
| Pvap | 5.34e-03 | kPa | 252.79 | Calculated Property |
| Pvap | 0.29 | kPa | 303.94 | Calculated Property |
| Pvap | 4.29 | kPa | 355.09 | Calculated Property |
| Pvap | 28.72 | kPa | 406.24 | Calculated Property |
| Pvap | 116.84 | kPa | 457.40 | Calculated Property |
| Pvap | 341.90 | kPa | 508.55 | Calculated Property |
| Pvap | 798.81 | kPa | 559.70 | Calculated Property |
| Pvap | 1594.84 | kPa | 610.85 | Calculated Property |
| Pvap | 2848.83 | kPa | 662.00 | Calculated Property |
| Pvap | [4.15; 104.97] | kPa | [354.32; 452.86] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50627e+01 | |||
| Coefficient B | -4.32994e+03 | |||
| Coefficient C | -3.68780e+01 | |||
| Reference | McDonald, Shrader, et al., 1959 | |||
| Temperature range, min. | 354.32 | |||
| Temperature range, max. | 452.86 | |||
| Pvap | 4.15 | kPa | 354.32 | Calculated Property |
| Pvap | 6.54 | kPa | 365.27 | Calculated Property |
| Pvap | 10.00 | kPa | 376.22 | Calculated Property |
| Pvap | 14.90 | kPa | 387.17 | Calculated Property |
| Pvap | 21.68 | kPa | 398.12 | Calculated Property |
| Pvap | 30.84 | kPa | 409.06 | Calculated Property |
| Pvap | 43.01 | kPa | 420.01 | Calculated Property |
| Pvap | 58.87 | kPa | 430.96 | Calculated Property |
| Pvap | 79.23 | kPa | 441.91 | Calculated Property |
| Pvap | 104.97 | kPa | 452.86 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [942.74; 349.29] | kg/m3 | [201.64; 657.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 2.32171e+00 | |||
| Coefficient B | 4.66450e-02 | |||
| Coefficient C | 6.70150e+02 | |||
| Coefficient D | 1.15260e-01 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 657.00 | |||
| ρl | 942.74 | kg/m3 | 201.64 | Calculated Property |
| ρl | 907.15 | kg/m3 | 252.24 | Calculated Property |
| ρl | 869.09 | kg/m3 | 302.83 | Calculated Property |
| ρl | 828.00 | kg/m3 | 353.43 | Calculated Property |
| ρl | 783.03 | kg/m3 | 404.02 | Calculated Property |
| ρl | 732.90 | kg/m3 | 454.62 | Calculated Property |
| ρl | 675.42 | kg/m3 | 505.21 | Calculated Property |
| ρl | 606.37 | kg/m3 | 555.81 | Calculated Property |
| ρl | 515.26 | kg/m3 | 606.40 | Calculated Property |
| ρl | 349.29 | kg/m3 | 657.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 2.59e-04] | N/m | [201.64; 657.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.28640e-02 | |||
| Coefficient B | 4.08470e+01 | |||
| Coefficient C | -2.93720e+00 | |||
| Coefficient D | -1.36300e-04 | |||
| Coefficient E | -3.17110e-06 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 657.00 | |||
| γ | 0.04 | N/m | 201.64 | Calculated Property |
| γ | 0.04 | N/m | 252.24 | Calculated Property |
| γ | 0.03 | N/m | 302.83 | Calculated Property |
| γ | 0.03 | N/m | 353.43 | Calculated Property |
| γ | 0.02 | N/m | 404.02 | Calculated Property |
| γ | 0.02 | N/m | 454.62 | Calculated Property |
| γ | 0.01 | N/m | 505.21 | Calculated Property |
| γ | 0.01 | N/m | 555.81 | Calculated Property |
| γ | 0.00 | N/m | 606.40 | Calculated Property |
| γ | 2.59e-04 | N/m | 657.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.08] | W/m×K | [201.64; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.04590e-05 | |||
| Coefficient B | 1.22170e+00 | |||
| Coefficient C | 1.83940e+02 | |||
| Coefficient D | 5.11670e+04 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 201.64 | Calculated Property |
| λgas | 0.01 | W/m×K | 290.35 | Calculated Property |
| λgas | 0.02 | W/m×K | 379.05 | Calculated Property |
| λgas | 0.02 | W/m×K | 467.76 | Calculated Property |
| λgas | 0.03 | W/m×K | 556.47 | Calculated Property |
| λgas | 0.04 | W/m×K | 645.17 | Calculated Property |
| λgas | 0.05 | W/m×K | 733.88 | Calculated Property |
| λgas | 0.06 | W/m×K | 822.59 | Calculated Property |
| λgas | 0.07 | W/m×K | 911.29 | Calculated Property |
| λgas | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.10] | W/m×K | [201.64; 451.33] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 6.14500e-02 | |||
| Coefficient B | -1.73560e+02 | |||
| Coefficient C | -2.35190e-01 | |||
| Coefficient D | -7.77580e-03 | |||
| Coefficient E | 3.87150e-06 | |||
| Temperature range, min. | 201.64 | |||
| Temperature range, max. | 451.33 | |||
| λliquid | 0.14 | W/m×K | 201.64 | Calculated Property |
| λliquid | 0.14 | W/m×K | 229.38 | Calculated Property |
| λliquid | 0.13 | W/m×K | 257.13 | Calculated Property |
| λliquid | 0.13 | W/m×K | 284.87 | Calculated Property |
| λliquid | 0.12 | W/m×K | 312.61 | Calculated Property |
| λliquid | 0.11 | W/m×K | 340.36 | Calculated Property |
| λliquid | 0.11 | W/m×K | 368.10 | Calculated Property |
| λliquid | 0.10 | W/m×K | 395.84 | Calculated Property |
| λliquid | 0.10 | W/m×K | 423.59 | Calculated Property |
| λliquid | 0.10 | W/m×K | 451.33 | Calculated Property |
Similar Compounds
Find more compounds similar to o-Cymene.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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