- InChI
- InChI=1S/C10H14/c1-3-5-10-7-4-6-9(2)8-10/h4,6-8H,3,5H2,1-2H3
- InChI Key
- QUEBYVKXYIKVSO-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- CCCc1cccc(C)c1
- Molecular Weight1
- 134.22
- CAS
- 1074-43-7
- Other Names
-
- 1-Methyl-3-n-propylbenzene
- 1-Methyl-3-propylbenzene
- 3-Propyl-toluene
- 3-n-Propyltoluene
- M-METHYLPROPYLBENZENE
- Toluene, m-propyl-
- m-Propyltoluene
- 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 | [0.4120; 0.4128] |
|
|
| ω | 0.4128 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.4120 | KDB | |
| ΔcH°liquid | [-5860.60; -5859.70] | kJ/mol |
|
| ΔcH°liquid | -5859.70 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -5860.60 ± 2.20 | kJ/mol | NIST |
| μ | 0.12 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 135.20 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -24.14 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | [-76.20; -75.40] | kJ/mol |
|
| ΔfH°liquid | -76.20 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -75.40 ± 2.20 | kJ/mol | NIST |
| ΔfusH° | 15.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.10 | kJ/mol | NIST |
| IE | 8.46 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.59 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.948 | Crippen Calculated Property | |
| McVol | 128.000 | ml/mol | McGowan Calculated Property |
| Pc | [2860.00; 2904.00] | kPa |
|
| Pc | 2860.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2904.00 | kPa | KDB |
| Ptriple | 7.21e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1003.00; 1066.00] |
|
|
| Inp | 1040.60 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1034.80 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1030.40 | NIST | |
| Inp | 1032.80 | NIST | |
| Inp | 1043.40 | NIST | |
| Inp | 1048.20 | NIST | |
| Inp | 1054.40 | NIST | |
| Inp | 1031.60 | NIST | |
| Inp | 1027.80 | NIST | |
| Inp | 1030.40 | NIST | |
| Inp | 1032.80 | NIST | |
| Inp | 1027.78 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | Outlier 1066.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1031.60 | NIST | |
| Inp | 1033.40 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1037.10 | NIST | |
| Inp | 1030.50 | NIST | |
| Inp | Outlier 1065.30 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1042.50 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1042.90 | NIST | |
| Inp | 1058.20 | NIST | |
| Inp | 1036.50 | NIST | |
| Inp | 1034.50 | NIST | |
| Inp | 1037.50 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1037.02 | NIST | |
| Inp | 1037.76 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1037.58 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1057.61 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | Outlier 1003.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1058.10 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1037.50 | NIST | |
| Inp | 1037.58 | NIST | |
| Inp | Outlier 1003.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1042.50 | NIST | |
| Ip | [1259.00; 1354.00] |
|
|
| Ip | 1259.00 | NIST | |
| Ip | 1262.00 | NIST | |
| Ip | 1301.00 | NIST | |
| Ip | 1277.20 | NIST | |
| Ip | 1277.20 | NIST | |
| Ip | 1297.00 | NIST | |
| Ip | 1314.00 | NIST | |
| Ip | 1315.00 | NIST | |
| Ip | 1326.00 | NIST | |
| Ip | 1338.00 | NIST | |
| Ip | Outlier 1354.00 | NIST | |
| Ip | 1302.00 | NIST | |
| Ip | 1277.00 | NIST | |
| Ip | 1301.00 | NIST | |
| Ip | 1277.00 | NIST | |
| Ip | 1284.00 | NIST | |
| Ip | 1297.00 | NIST | |
| Ip | 1259.00 | NIST | |
| Ip | 1301.00 | NIST | |
| Tboil | [450.20; 455.21] | K |
|
| Tboil | 455.13 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 455.20 | K | KDB |
| Tboil | 455.20 | K | NIST |
| Tboil | 455.15 ± 0.50 | K | NIST |
| Tboil | 455.20 ± 0.20 | K | NIST |
| Tboil | 455.21 ± 0.20 | K | NIST |
| Tboil | 455.13 ± 0.30 | K | NIST |
| Tboil | 455.21 ± 0.20 | K | NIST |
| Tboil | 453.00 ± 2.00 | K | NIST |
| Tboil | 454.90 ± 0.40 | K | NIST |
| Tboil | 454.90 ± 0.40 | K | NIST |
| Tboil | 454.90 ± 0.40 | K | NIST |
| Tboil | 454.90 ± 0.40 | K | NIST |
| Tboil | 454.90 ± 0.40 | K | NIST |
| Tboil | 451.00 ± 5.00 | K | NIST |
| Tboil | 451.00 ± 5.00 | K | NIST |
| Tboil | Outlier 450.20 ± 3.00 | K | NIST |
| Tc | [656.00; 666.60] | K |
|
| Tc | 656.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 666.60 | K | KDB |
| Tfus | [190.57; 190.65] | K |
|
| Tfus | 190.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 190.57 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 190.57 ± 0.02 | K | NIST |
| Ttriple | 190.57 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.62 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.01 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.482 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2490000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.25 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 47.80 | kJ/mol | 409.50 | NIST |
| ρl | 859.01 | kg/m3 | 293.10 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [175.20; 477.28] | J/mol×K | [298.15; 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 | 9.71270e+01 | |||
| Coefficient B | -5.99110e+02 | |||
| Coefficient C | 6.36524e+00 | |||
| Coefficient D | 1.16650e-05 | |||
| Coefficient E | -1.90030e-08 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 175.20 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 242.44 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 298.63 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 343.47 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 379.14 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 407.72 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 430.80 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 449.54 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 464.83 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 477.28 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [245.06; 351.42] | J/mol×K | [298.15; 490.50] |
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 | 1.56110e+02 | |||
| Coefficient B | -3.80930e+01 | |||
| Coefficient C | 3.25124e+00 | |||
| Coefficient D | 5.03130e-03 | |||
| Coefficient E | -1.52470e-06 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 490.50 | |||
| Cp,liquid | 245.06 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 254.01 | J/mol×K | 319.52 | Calculated Property |
| Cp,liquid | 263.61 | J/mol×K | 340.89 | Calculated Property |
| Cp,liquid | 273.87 | J/mol×K | 362.27 | Calculated Property |
| Cp,liquid | 284.84 | J/mol×K | 383.64 | Calculated Property |
| Cp,liquid | 296.56 | J/mol×K | 405.01 | Calculated Property |
| Cp,liquid | 309.04 | J/mol×K | 426.38 | Calculated Property |
| Cp,liquid | 322.33 | J/mol×K | 447.76 | Calculated Property |
| Cp,liquid | 336.44 | J/mol×K | 469.13 | Calculated Property |
| Cp,liquid | 351.42 | J/mol×K | 490.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0154100; 0.0000866] | Pa×s | [190.57; 603.15] |
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 | -1.73010e+01 | |||
| Coefficient B | 1.60140e+03 | |||
| Coefficient C | 9.10180e-01 | |||
| Coefficient D | -1.47070e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 190.57 | |||
| Temperature range, max. | 603.15 | |||
| η | 0.0154100 | Pa×s | 190.57 | Calculated Property |
| η | 0.0035715 | Pa×s | 236.41 | Calculated Property |
| η | 0.0013487 | Pa×s | 282.25 | Calculated Property |
| η | 0.0006718 | Pa×s | 328.10 | Calculated Property |
| η | 0.0003968 | Pa×s | 373.94 | Calculated Property |
| η | 0.0002618 | Pa×s | 419.78 | Calculated Property |
| η | 0.0001861 | Pa×s | 465.62 | Calculated Property |
| η | 0.0001395 | Pa×s | 511.47 | Calculated Property |
| η | 0.0001085 | Pa×s | 557.31 | Calculated Property |
| η | 0.0000866 | Pa×s | 603.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [56.34; 7.76] | kJ/mol | [190.57; 654.00] |
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 | 6.19457e+01 | |||
| Coefficient B | 5.24158e-02 | |||
| Coefficient C | 1.08883e+00 | |||
| Coefficient D | -1.22236e+00 | |||
| Coefficient E | 4.39479e-01 | |||
| Critical temperature, Tc (K) | 6.56000e+02 | |||
| Temperature range, min. | 190.57 | |||
| Temperature range, max. | 654.00 | |||
| ΔvapH | 56.34 | kJ/mol | 190.57 | Calculated Property |
| ΔvapH | 53.71 | kJ/mol | 242.06 | Calculated Property |
| ΔvapH | 50.80 | kJ/mol | 293.55 | Calculated Property |
| ΔvapH | 47.67 | kJ/mol | 345.05 | Calculated Property |
| ΔvapH | 44.32 | kJ/mol | 396.54 | Calculated Property |
| ΔvapH | 40.69 | kJ/mol | 448.03 | Calculated Property |
| ΔvapH | 36.62 | kJ/mol | 499.52 | Calculated Property |
| ΔvapH | 31.73 | kJ/mol | 551.02 | Calculated Property |
| ΔvapH | 25.01 | kJ/mol | 602.51 | Calculated Property |
| ΔvapH | 7.76 | kJ/mol | 654.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [335.55; 484.55] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44657e+01 | |||
| Coefficient B | -3.84928e+03 | |||
| Coefficient C | -6.40540e+01 | |||
| Temperature range, min. | 335.55 | |||
| Temperature range, max. | 484.55 | |||
| Pvap | 1.33 | kPa | 335.55 | Calculated Property |
| Pvap | 3.01 | kPa | 352.11 | Calculated Property |
| Pvap | 6.23 | kPa | 368.66 | Calculated Property |
| Pvap | 11.94 | kPa | 385.22 | Calculated Property |
| Pvap | 21.49 | kPa | 401.77 | Calculated Property |
| Pvap | 36.61 | kPa | 418.33 | Calculated Property |
| Pvap | 59.47 | kPa | 434.88 | Calculated Property |
| Pvap | 92.67 | kPa | 451.44 | Calculated Property |
| Pvap | 139.26 | kPa | 467.99 | Calculated Property |
| Pvap | 202.66 | kPa | 484.55 | Calculated Property |
| Pvap | [4.26e-07; 2811.68] | kPa | [190.57; 654.00] |
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 | 1.00551e+02 | |||
| Coefficient B | -9.50877e+03 | |||
| Coefficient C | -1.24892e+01 | |||
| Coefficient D | 6.77692e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 190.57 | |||
| Temperature range, max. | 654.00 | |||
| Pvap | 4.26e-07 | kPa | 190.57 | Calculated Property |
| Pvap | 1.02e-03 | kPa | 242.06 | Calculated Property |
| Pvap | 0.11 | kPa | 293.55 | Calculated Property |
| Pvap | 2.26 | kPa | 345.05 | Calculated Property |
| Pvap | 18.49 | kPa | 396.54 | Calculated Property |
| Pvap | 85.05 | kPa | 448.03 | Calculated Property |
| Pvap | 271.21 | kPa | 499.52 | Calculated Property |
| Pvap | 680.67 | kPa | 551.02 | Calculated Property |
| Pvap | 1457.80 | kPa | 602.51 | Calculated Property |
| Pvap | 2811.68 | kPa | 654.00 | Calculated Property |
| Pvap | [1.30; 202.50] | kPa | [334.15; 485.15] |
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 | 1.05651e+02 | |||
| Coefficient B | -9.71981e+03 | |||
| Coefficient C | -1.32760e+01 | |||
| Coefficient D | 7.64429e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 334.15 | |||
| Temperature range, max. | 485.15 | |||
| Pvap | 1.30 | kPa | 334.15 | Calculated Property |
| Pvap | 2.97 | kPa | 350.93 | Calculated Property |
| Pvap | 6.21 | kPa | 367.71 | Calculated Property |
| Pvap | 11.98 | kPa | 384.48 | Calculated Property |
| Pvap | 21.63 | kPa | 401.26 | Calculated Property |
| Pvap | 36.88 | kPa | 418.04 | Calculated Property |
| Pvap | 59.85 | kPa | 434.82 | Calculated Property |
| Pvap | 93.07 | kPa | 451.59 | Calculated Property |
| Pvap | 139.49 | kPa | 468.37 | Calculated Property |
| Pvap | 202.50 | kPa | 485.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [938.93; 290.11] | kg/m3 | [190.57; 654.00] |
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 | 2.44572e+01 | |||
| Coefficient B | 1.51520e-01 | |||
| Coefficient C | 6.56000e+02 | |||
| Coefficient D | 2.01780e-01 | |||
| Temperature range, min. | 190.57 | |||
| Temperature range, max. | 654.00 | |||
| ρl | 938.93 | kg/m3 | 190.57 | Calculated Property |
| ρl | 901.07 | kg/m3 | 242.06 | Calculated Property |
| ρl | 861.00 | kg/m3 | 293.55 | Calculated Property |
| ρl | 818.22 | kg/m3 | 345.05 | Calculated Property |
| ρl | 771.94 | kg/m3 | 396.54 | Calculated Property |
| ρl | 720.96 | kg/m3 | 448.03 | Calculated Property |
| ρl | 663.21 | kg/m3 | 499.52 | Calculated Property |
| ρl | 594.52 | kg/m3 | 551.02 | Calculated Property |
| ρl | 503.66 | kg/m3 | 602.51 | Calculated Property |
| ρl | 290.11 | kg/m3 | 654.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 2.57e-06] | N/m | [190.57; 646.12] |
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 | -8.65110e-03 | |||
| Coefficient B | 6.11400e+01 | |||
| Coefficient C | -3.18880e+00 | |||
| Coefficient D | 4.56900e-04 | |||
| Coefficient E | -4.67290e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 654 K. | |||
| Temperature range, min. | 190.57 | |||
| Temperature range, max. | 646.12 | |||
| γ | 0.04 | N/m | 190.57 | Calculated Property |
| γ | 0.04 | N/m | 241.19 | Calculated Property |
| γ | 0.03 | N/m | 291.80 | Calculated Property |
| γ | 0.02 | N/m | 342.42 | Calculated Property |
| γ | 0.02 | N/m | 393.04 | Calculated Property |
| γ | 0.01 | N/m | 443.65 | Calculated Property |
| γ | 0.01 | N/m | 494.27 | Calculated Property |
| γ | 0.01 | N/m | 544.89 | Calculated Property |
| γ | 0.00 | N/m | 595.50 | Calculated Property |
| γ | 2.57e-06 | N/m | 646.12 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.07] | W/m×K | [190.57; 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 | 8.35130e-05 | |||
| Coefficient B | 1.05170e+00 | |||
| Coefficient C | 5.70800e+02 | |||
| Coefficient D | 3.37900e+04 | |||
| Temperature range, min. | 190.57 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 190.57 | Calculated Property |
| λgas | 0.01 | W/m×K | 280.51 | Calculated Property |
| λgas | 0.02 | W/m×K | 370.44 | Calculated Property |
| λgas | 0.02 | W/m×K | 460.38 | Calculated Property |
| λgas | 0.03 | W/m×K | 550.32 | Calculated Property |
| λgas | 0.04 | W/m×K | 640.25 | Calculated Property |
| λgas | 0.05 | W/m×K | 730.19 | Calculated Property |
| λgas | 0.06 | W/m×K | 820.13 | Calculated Property |
| λgas | 0.06 | W/m×K | 910.06 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.09] | W/m×K | [190.57; 454.95] |
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 | -7.41980e-02 | |||
| Coefficient B | 4.02300e+00 | |||
| Coefficient C | -1.43640e+00 | |||
| Coefficient D | -4.22520e-04 | |||
| Coefficient E | -8.56200e-07 | |||
| Temperature range, min. | 190.57 | |||
| Temperature range, max. | 454.95 | |||
| λliquid | 0.14 | W/m×K | 190.57 | Calculated Property |
| λliquid | 0.14 | W/m×K | 219.95 | Calculated Property |
| λliquid | 0.13 | W/m×K | 249.32 | Calculated Property |
| λliquid | 0.13 | W/m×K | 278.70 | Calculated Property |
| λliquid | 0.12 | W/m×K | 308.07 | Calculated Property |
| λliquid | 0.12 | W/m×K | 337.45 | Calculated Property |
| λliquid | 0.11 | W/m×K | 366.82 | Calculated Property |
| λliquid | 0.10 | W/m×K | 396.20 | Calculated Property |
| λliquid | 0.10 | W/m×K | 425.57 | Calculated Property |
| λliquid | 0.09 | W/m×K | 454.95 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1-methyl-3-propyl-.
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).
- 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
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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