- InChI
- InChI=1S/C10H14/c1-2-3-7-10-8-5-4-6-9-10/h4-6,8-9H,2-3,7H2,1H3
- InChI Key
- OCKPCBLVNKHBMX-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- CCCCc1ccccc1
- Molecular Weight1
- 134.22
- CAS
- 104-51-8
- Other Names
-
- 1-PHENYLBUTANE
- 1-butylbenzene
- Benzene, butyl-
- Butylbenzene
- UN 2709
- n-Butylbenzene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- 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).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (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).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3930 | KDB | |
| PAff | 791.90 | kJ/mol | NIST |
| BasG | 764.20 | kJ/mol | NIST |
| ΔcH°liquid | [-5873.00; -5872.10] | kJ/mol |
|
| ΔcH°liquid | -5873.00 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -5872.10 ± 1.10 | kJ/mol | NIST |
| μ | 0.40 | debye | KDB |
| ΔfG° | 144.80 | kJ/mol | KDB |
| Δc,grossH | 5872.08 | kJ/mol | KDB |
| Δc,netH | 5563.967 | kJ/mol | KDB |
| ΔfH°gas | [-13.82; -12.80] | kJ/mol |
|
| ΔfH°gas | -13.82 | kJ/mol | KDB |
| ΔfH°gas | -12.80 | kJ/mol | NIST |
| ΔfH°gas | -13.80 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | [-63.90; -62.90] | kJ/mol |
|
| ΔfH°liquid | -62.90 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -63.90 ± 1.30 | kJ/mol | NIST |
| ΔfusH° | 15.70 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [50.10; 51.37] | kJ/mol |
|
| ΔvapH° | 51.37 | kJ/mol | NIST |
| ΔvapH° | 50.80 | kJ/mol | NIST |
| ΔvapH° | 50.10 | kJ/mol | NIST |
| ΔvapH° | 51.00 ± 2.90 | kJ/mol | NIST |
| ΔvapH° | 50.10 | kJ/mol | NIST |
| IE | [8.68; 8.71] | eV |
|
| IE | 8.69 ± 0.01 | eV | NIST |
| IE | 8.68 | eV | NIST |
| IE | Outlier 8.71 ± 0.01 | eV | NIST |
| IE | 8.69 | eV | NIST |
| IE | 8.69 ± 0.01 | eV | NIST |
| IE | 8.69 ± 0.05 | eV | NIST |
| log10WS | [-4.06; -4.06] |
|
|
| log10WS | -4.06 | Aq. Sol... | |
| log10WS | -4.06 | Estimat... | |
| logPoct/wat | 3.029 | Crippen Calculated Property | |
| McVol | 128.000 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [2887.00; 2890.00] | kPa |
|
| Pc | 2890.00 | kPa | KDB |
| Pc | 2890.00 ± 40.00 | kPa | NIST |
| Pc | 2887.00 ± 7.00 | kPa | NIST |
| ρc | [269.64; 269.78] | kg/m3 |
|
| ρc | 269.78 ± 5.37 | kg/m3 | NIST |
| ρc | 269.64 ± 10.07 | kg/m3 | NIST |
| Inp | [170.00; 1078.00] |
|
|
| Inp | 1058.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1062.90 | NIST | |
| Inp | 1072.40 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1039.60 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1032.30 | NIST | |
| Inp | 1034.90 | NIST | |
| Inp | 1048.10 | NIST | |
| Inp | 1053.60 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1037.40 | NIST | |
| Inp | 1029.40 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1032.30 | NIST | |
| Inp | 1034.90 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1029.42 | 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 | 1066.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1037.40 | NIST | |
| Inp | 1035.80 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1035.20 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1047.40 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1053.70 | NIST | |
| Inp | 1053.30 | NIST | |
| Inp | 1050.10 | NIST | |
| Inp | 1053.70 | NIST | |
| Inp | 1055.90 | NIST | |
| Inp | 1036.40 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1043.20 | NIST | |
| Inp | 1050.10 | NIST | |
| Inp | 1053.70 | NIST | |
| Inp | 1055.90 | NIST | |
| Inp | 1053.70 | NIST | |
| Inp | 1053.30 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1041.77 | NIST | |
| Inp | 1042.19 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1066.40 | NIST | |
| Inp | 1056.40 | NIST | |
| Inp | 1062.20 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1071.80 | NIST | |
| Inp | 1074.50 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1037.42 | NIST | |
| Inp | 1040.68 | NIST | |
| Inp | 1043.02 | NIST | |
| Inp | 1054.18 | NIST | |
| Inp | 1057.89 | NIST | |
| Inp | 1060.55 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1066.87 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1046.30 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1062.90 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1036.20 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | Outlier 170.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1034.90 | NIST | |
| Inp | 1029.40 | NIST | |
| Inp | 1029.42 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1037.40 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1053.70 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1042.19 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1040.68 | NIST | |
| Inp | 1040.00 | NIST | |
| I | [1269.00; 1367.70] |
|
|
| I | 1309.10 | NIST | |
| I | 1356.40 | NIST | |
| I | Outlier 1362.10 | NIST | |
| I | Outlier 1367.70 | NIST | |
| I | 1284.00 | NIST | |
| I | 1337.60 | NIST | |
| I | 1301.90 | NIST | |
| I | 1284.00 | NIST | |
| I | 1328.00 | NIST | |
| I | 1335.00 | NIST | |
| I | 1343.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1306.00 | NIST | |
| I | 1322.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1304.00 | NIST | |
| I | 1308.00 | NIST | |
| I | 1306.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1284.00 | NIST | |
| I | 1320.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1284.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1301.00 | NIST | |
| I | 1323.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1312.00 | NIST | |
| I | 1319.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1297.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1309.00 | NIST | |
| I | 1284.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1312.00 | NIST | |
| I | 1309.00 | NIST | |
| I | 1312.00 | NIST | |
| I | 1316.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1312.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1320.00 | NIST | |
| S°gas | 437.86 | J/mol×K | NIST |
| S°liquid | [321.21; 321.30] | J/mol×K |
|
| S°liquid | 321.21 | J/mol×K | NIST |
| S°liquid | 321.30 | J/mol×K | NIST |
| Tboil | [442.15; 466.00] | K |
|
| Tboil | 456.46 | K | KDB |
| Tboil | 456.38 | K | Isobari... |
| Tboil | 456.40 | K | Isobari... |
| Tboil | 456.50 | K | NIST |
| Tboil | 456.00 | K | NIST |
| Tboil | 456.40 | K | NIST |
| Tboil | 456.43 ± 0.20 | K | NIST |
| Tboil | 454.00 ± 4.00 | K | NIST |
| Tboil | 456.60 ± 1.00 | K | NIST |
| Tboil | 456.00 ± 3.00 | K | NIST |
| Tboil | 456.41 ± 0.30 | K | NIST |
| Tboil | 455.00 ± 3.00 | K | NIST |
| Tboil | 455.70 ± 1.50 | K | NIST |
| Tboil | 456.05 ± 0.30 | K | NIST |
| Tboil | 456.50 ± 0.30 | K | NIST |
| Tboil | 456.25 ± 0.40 | K | NIST |
| Tboil | 456.41 ± 0.30 | K | NIST |
| Tboil | 456.00 ± 0.70 | K | NIST |
| Tboil | 456.42 ± 0.03 | K | NIST |
| Tboil | 456.30 ± 0.30 | K | NIST |
| Tboil | 456.41 ± 0.10 | K | NIST |
| Tboil | 456.30 ± 0.50 | K | NIST |
| Tboil | 456.41 ± 0.30 | K | NIST |
| Tboil | 456.50 ± 0.30 | K | NIST |
| Tboil | 456.25 ± 0.30 | K | NIST |
| Tboil | 456.25 ± 0.30 | K | NIST |
| Tboil | 456.50 ± 0.20 | K | NIST |
| Tboil | 456.50 ± 0.20 | K | NIST |
| Tboil | 456.34 ± 0.30 | K | NIST |
| Tboil | 455.00 ± 2.00 | K | NIST |
| Tboil | 453.00 ± 2.00 | K | NIST |
| Tboil | 455.00 ± 3.00 | K | NIST |
| Tboil | 454.50 ± 0.80 | K | NIST |
| Tboil | 456.25 ± 0.30 | K | NIST |
| Tboil | 456.41 ± 0.20 | K | NIST |
| Tboil | 456.41 ± 0.30 | K | NIST |
| Tboil | Outlier 466.00 ± 2.00 | K | NIST |
| Tboil | Outlier 442.15 ± 2.50 | K | NIST |
| Tboil | 453.00 ± 3.00 | K | NIST |
| Tboil | 451.00 ± 5.00 | K | NIST |
| Tboil | 457.00 ± 4.00 | K | NIST |
| Tboil | 456.45 ± 0.30 | K | NIST |
| Tboil | 453.00 ± 4.00 | K | NIST |
| Tboil | 453.00 ± 5.00 | K | NIST |
| Tboil | 456.25 ± 0.30 | K | NIST |
| Tboil | 453.65 ± 2.00 | K | NIST |
| Tboil | 453.15 ± 2.00 | K | NIST |
| Tc | [660.05; 661.00] | K |
|
| Tc | 660.50 | K | KDB |
| Tc | 660.50 ± 0.50 | K | NIST |
| Tc | 660.50 | K | NIST |
| Tc | 660.05 ± 0.50 | K | NIST |
| Tc | 660.45 ± 0.10 | K | NIST |
| Tc | 661.00 ± 0.50 | K | NIST |
| Tfus | [184.70; 192.00] | K |
|
| Tfus | 185.20 | K | KDB |
| Tfus | 185.19 | K | Aq. Sol... |
| Tfus | 185.15 ± 0.20 | K | NIST |
| Tfus | 185.15 ± 0.20 | K | NIST |
| Tfus | 185.61 ± 0.20 | K | NIST |
| Tfus | 185.61 ± 0.30 | K | NIST |
| Tfus | 185.00 ± 0.50 | K | NIST |
| Tfus | 185.18 ± 0.04 | K | NIST |
| Tfus | 185.00 ± 0.20 | K | NIST |
| Tfus | 185.18 ± 0.30 | K | NIST |
| Tfus | 184.97 ± 0.20 | K | NIST |
| Tfus | 184.70 ± 1.50 | K | NIST |
| Tfus | 184.70 ± 1.00 | K | NIST |
| Tfus | Outlier 192.00 ± 0.30 | K | NIST |
| Ttriple | [184.60; 185.30] | K |
|
| Ttriple | 185.30 ± 0.01 | K | NIST |
| Ttriple | 185.14 ± 0.01 | K | NIST |
| Ttriple | 184.60 ± 0.25 | K | NIST |
| Vc | [0.497; 0.497] | m3/kmol |
|
| Vc | 0.497 | m3/kmol | KDB |
| Vc | 0.497 | m3/kmol | NIST |
| Zc | 0.2615440 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [256.33; 335.30] | J/mol×K | [454.88; 659.45] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 260 280 300 320 340 500 600 | ||||
| Cp,gas | 256.33 | J/mol×K | 454.88 | Joback Calculated Property |
| Cp,gas | 271.45 | J/mol×K | 488.98 | Joback Calculated Property |
| Cp,gas | 285.75 | J/mol×K | 523.07 | Joback Calculated Property |
| Cp,gas | 299.25 | J/mol×K | 557.17 | Joback Calculated Property |
| Cp,gas | 311.99 | J/mol×K | 591.26 | Joback Calculated Property |
| Cp,gas | 323.99 | J/mol×K | 625.36 | Joback Calculated Property |
| Cp,gas | 335.30 | J/mol×K | 659.45 | Joback Calculated Property |
| Cp,liquid | [203.00; 243.34] | J/mol×K | [293.00; 298.20] |
|
| Cp,liquid | 203.00 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 241.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 243.34 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 240.20 | J/mol×K | 298.20 | NIST |
| η | [0.0007870; 0.0009010] | Pa×s | [303.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 7.80e-4 8.00e-4 8.20e-4 8.40e-4 8.60e-4 8.80e-4 9.00e-4 305 310 | ||||
| η | 0.0009010 | Pa×s | 303.15 | Physica... |
| η | 0.0009010 | Pa×s | 303.15 | Density... |
| η | 0.0008440 | Pa×s | 308.15 | Physica... |
| η | 0.0008440 | Pa×s | 308.15 | Density... |
| η | 0.0007870 | Pa×s | 313.15 | Physica... |
| η | 0.0007870 | Pa×s | 313.15 | Density... |
| ΔfusH | [10.98; 11.22] | kJ/mol | [184.60; 185.30] |
|
| ΔfusH | 10.98 | kJ/mol | 184.60 | NIST |
| ΔfusH | 11.22 | kJ/mol | 185.30 | NIST |
| ΔfusH | 11.22 | kJ/mol | 185.30 | NIST |
| ΔvapH | [37.50; 53.50] | kJ/mol | [323.00; 456.40] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 40 45 50 55 350 400 450 | ||||
| ΔvapH | 53.50 | kJ/mol | 323.00 | NIST |
| ΔvapH | 48.00 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 46.80 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 46.00 ± 0.10 | kJ/mol | 368.00 | NIST |
| ΔvapH | 45.20 | kJ/mol | 414.00 | NIST |
| ΔvapH | 45.70 | kJ/mol | 416.00 | NIST |
| ΔvapH | 47.40 ± 0.20 | kJ/mol | 422.00 | NIST |
| ΔvapH | 43.50 ± 0.20 | kJ/mol | 422.00 | NIST |
| ΔvapH | 40.60 ± 0.40 | kJ/mol | 422.00 | NIST |
| ΔvapH | 37.50 ± 0.70 | kJ/mol | 422.00 | NIST |
| ΔvapH | 39.25 | kJ/mol | 456.40 | KDB |
| ΔvapH | 38.87 | kJ/mol | 456.40 | NIST |
| n0 | [1.48450; 1.48950] | [293.10; 303.15] |
|
|
|
T(K) Refractive Index 1.48 1.49 1.49 1.49 1.49 1.49 295 300 | ||||
| n0 | 1.48940 | 293.10 | Extract... | |
| n0 | 1.48950 | 293.10 | Extract... | |
| n0 | 1.48950 | 293.15 | Densiti... | |
| n0 | 1.48735 | 298.15 | Effect ... | |
| n0 | 1.48740 | 298.15 | Excess ... | |
| n0 | 1.48742 | 298.15 | KDB | |
| n0 | 1.48450 | 303.15 | Densiti... | |
| ρl | [820.30; 892.80] | kg/m3 | [253.15; 343.15] |
|
|
T(K) Liquid Density (kg/m3) 820 840 860 880 900 300 | ||||
| ρl | 892.80 | kg/m3 | 253.15 | Densiti... |
| ρl | 892.60 | kg/m3 | 253.15 | Density... |
| ρl | 864.47 | kg/m3 | 288.15 | Density... |
| ρl | 864.70 | kg/m3 | 288.15 | Densiti... |
| ρl | 860.00 | kg/m3 | 293.00 | KDB |
| ρl | 860.69 | kg/m3 | 293.15 | Densiti... |
| ρl | 860.17 | kg/m3 | 293.15 | Density... |
| ρl | 860.60 | kg/m3 | 293.15 | Density... |
| ρl | 856.29 | kg/m3 | 298.15 | Thermod... |
| ρl | 856.68 | kg/m3 | 298.15 | Densiti... |
| ρl | 856.29 | kg/m3 | 298.15 | Excess ... |
| ρl | 852.13 | kg/m3 | 303.15 | Density... |
| ρl | 852.65 | kg/m3 | 303.15 | Densiti... |
| ρl | 852.56 | kg/m3 | 303.15 | Density... |
| ρl | 844.60 | kg/m3 | 313.15 | Densiti... |
| ρl | 844.50 | kg/m3 | 313.15 | Density... |
| ρl | 844.07 | kg/m3 | 313.15 | Density... |
| ρl | 836.41 | kg/m3 | 323.15 | Density... |
| ρl | 835.98 | kg/m3 | 323.15 | Density... |
| ρl | 836.51 | kg/m3 | 323.15 | Densiti... |
| ρl | 827.86 | kg/m3 | 333.15 | Density... |
| ρl | 828.38 | kg/m3 | 333.15 | Densiti... |
| ρl | 828.29 | kg/m3 | 333.15 | Density... |
| ρl | 820.30 | kg/m3 | 343.15 | Density... |
| ΔfusS | 59.50 | J/mol×K | 184.60 | NIST |
| γ | [0.03; 0.03] | N/m | [293.20; 294.20] |
|
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 294.20 | Density... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [334.90; 486.52] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45284e+01 | |||
| Coefficient B | -3.96130e+03 | |||
| Coefficient C | -5.67370e+01 | |||
| Temperature range, min. | 334.90 | |||
| Temperature range, max. | 486.52 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 334.90 | Calculated Property |
| Pvap | 3.01 | kPa | 351.75 | Calculated Property |
| Pvap | 6.21 | kPa | 368.59 | Calculated Property |
| Pvap | 11.91 | kPa | 385.44 | Calculated Property |
| Pvap | 21.43 | kPa | 402.29 | Calculated Property |
| Pvap | 36.51 | kPa | 419.13 | Calculated Property |
| Pvap | 59.33 | kPa | 435.98 | Calculated Property |
| Pvap | 92.52 | kPa | 452.83 | Calculated Property |
| Pvap | 139.13 | kPa | 469.67 | Calculated Property |
| Pvap | 202.64 | kPa | 486.52 | Calculated Property |
| Pvap | [8.50e-08; 2894.10] | kPa | [185.30; 660.55] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.12433e+02 | |||
| Coefficient B | -1.01044e+04 | |||
| Coefficient C | -1.42573e+01 | |||
| Coefficient D | 7.81134e-06 | |||
| Temperature range, min. | 185.30 | |||
| Temperature range, max. | 660.55 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 400 600 | ||||
| Pvap | 8.50e-08 | kPa | 185.30 | Calculated Property |
| Pvap | 5.07e-04 | kPa | 238.11 | Calculated Property |
| Pvap | 0.08 | kPa | 290.91 | Calculated Property |
| Pvap | 2.01 | kPa | 343.72 | Calculated Property |
| Pvap | 17.83 | kPa | 396.52 | Calculated Property |
| Pvap | 84.94 | kPa | 449.33 | Calculated Property |
| Pvap | 274.55 | kPa | 502.13 | Calculated Property |
| Pvap | 692.53 | kPa | 554.94 | Calculated Property |
| Pvap | 1489.29 | kPa | 607.74 | Calculated Property |
| Pvap | 2894.10 | kPa | 660.55 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, n-butyl-.
Mixtures
- Benzene, n-butyl- + Acetic acid, butyl ester
- Benzene, n-butyl- + Ethane, 1,1,2,2-tetrachloro-
- Benzene, n-butyl- + Anisole
- Benzene, n-butyl- + 1-Propanone, 1-phenyl-
- Benzene, n-butyl- + N-Formylmorpholine
- Benzene, n-butyl- + Decane
- Benzene, n-butyl- + Dodecane
- Benzene, n-butyl- + Tetradecane
- Benzene, n-butyl- + Hexadecane
- Heptadecane + Benzene, n-butyl-
- Benzene, n-butyl- + Hexadecane + Cyclohexane, butyl-
- Benzene, n-butyl- + Dodecane + Cyclohexane, butyl-
- Benzene, n-butyl- + Nonane, 2,2,4,4,6,8,8-heptamethyl-
- Heptane, 2,2,4,6,6-pentamethyl- + Benzene, n-butyl-
- Benzene, n-butyl- + Cyclohexane, butyl- + Nonane, 2,2,4,4,6,8,8-heptamethyl-
- Benzene, n-butyl- + Dodecane + Nonane, 2,2,4,4,6,8,8-heptamethyl-
- Benzene, n-butyl- + Benzene, chloro-
- Benzene, n-butyl- + Benzyl chloride
- Benzene, n-butyl- + Benzene, (2-chloroethyl)-
- Benzene, n-butyl- + Benzene, (3-chloropropyl)-
Find more mixtures with Benzene, n-butyl-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
- Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
- Phase equilibria of (CO2 + butylbenzene) and (CO2 + butylcyclohexane) at temperatures between (323.15 and 423.15) K and at pressures up to 21MPa
- Evaluation of 1-ethyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate as solvents for extraction of alkylbenzenes from hexadecane at 313 and 333 K
- Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
- Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
- Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
- Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
- Effect of Solvent Cation Alkyl-Chain Length on the Separation of Butylbenzene from n-Tetradecane Using Hexafluorophosphate-Based Ionic Liquids at (313.15 and 333.15) K and 101.3 kPa
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexylbenzene (1) or n-Butylbenzene (1) in 2,2,4,6,6-Pentamethylheptane (2) or 2,2,4,4,6,8,8-Heptamethylnonane (2) at 0.1 MPa
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
- Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Extraction of Butylbenzene from Dodecane Using Hexafluorophosphate-Based Ionic Liquids: Effect of Cation Change
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Physical Properties of Binary Mixtures of Ethyl Formate with Benzene, Isopropyl Benzene, Isobutyl Benzene, and Butylbenzene at (303.15, 308.15, and 313.15) K
- Density and Viscosity of Propyl Formate + Aromatic Hydrocarbons at T = (303.15, 308.15, and 313.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.