- 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.
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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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
|
| 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] |
|
| 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 | |||
| 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 | |||
| 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
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