- InChI
- InChI=1S/C9H12/c1-2-6-9-7-4-3-5-8-9/h3-5,7-8H,2,6H2,1H3
- InChI Key
- ODLMAHJVESYWTB-UHFFFAOYSA-N
- Formula
- C9H12
- SMILES
- CCCc1ccccc1
- Molecular Weight1
- 120.19
- CAS
- 103-65-1
- Other Names
-
- 1-Propylbenzene
- 1-phenylpropane
- Benzene, n-propyl-
- Isocumene
- NSC 16941
- Phenylpropane
- UN 2364
- n-propylbenzene
- propylbenzene
- 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).
- Csat : Molar heat capacity at saturation pressure (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).
- Ptriple : Triple Point 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.
- 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).
- λ : Gas thermal conductivity (W/m×K).
- λ : 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 | [0.3440; 0.3450] |
|
|
| ω | 0.3450 | ChemSep v8.3 pure component data | |
| ω | 0.3440 | KDB | |
| PAff | 790.10 | kJ/mol | NIST |
| BasG | 762.40 | kJ/mol | NIST |
| ΔcH°liquid | [-5218.24; -5214.80] | kJ/mol |
|
| ΔcH°liquid | -5218.24 ± 0.67 | kJ/mol | NIST |
| ΔcH°liquid | -5214.80 | kJ/mol | NIST |
| μ | 0.37 | debye | ChemSep v8.3 pure component data |
| ΔfG° | [137.30; 137.60] | kJ/mol |
|
| ΔfG° | 137.60 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfG° | 137.30 | kJ/mol | KDB |
| Δc,grossH | 5218.24 | kJ/mol | KDB |
| Δc,netH | 4954.149 | kJ/mol | KDB |
| ΔfH°gas | [7.82; 7.90] | kJ/mol |
|
| ΔfH°gas | 7.90 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | 7.83 | kJ/mol | KDB |
| ΔfH°gas | 7.82 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | -38.40 ± 0.84 | kJ/mol | NIST |
| ΔfusH° | 13.11 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [45.00; 46.24] | kJ/mol |
|
| ΔvapH° | 46.24 | kJ/mol | NIST |
| ΔvapH° | 46.20 | kJ/mol | NIST |
| ΔvapH° | Outlier 45.00 | kJ/mol | NIST |
| ΔvapH° | 46.20 | kJ/mol | NIST |
| ΔvapH° | 46.10 ± 2.10 | kJ/mol | NIST |
| ΔvapH° | 46.20 | kJ/mol | NIST |
| ΔvapH° | 46.22 | kJ/mol | NIST |
| ΔvapH° | 46.20 | kJ/mol | NIST |
| IE | [8.71; 8.77] | eV |
|
| IE | 8.71 ± 0.01 | eV | NIST |
| IE | 8.71 | eV | NIST |
| IE | Outlier 8.77 ± 0.08 | eV | NIST |
| IE | 8.71 | eV | NIST |
| IE | 8.72 ± 0.01 | eV | NIST |
| IE | 8.72 ± 0.01 | eV | NIST |
| log10WS | [-3.37; -3.37] |
|
|
| log10WS | -3.37 | Aq. Solubility Prediction | |
| log10WS | -3.37 | Estimated Solubility | |
| logPoct/wat | 2.639 | Crippen Calculated Property | |
| McVol | 113.910 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3170.00; 3200.00] | kPa |
|
| Pc | 3200.00 | kPa | ChemSep v8.3 pure component data |
| Pc | 3200.00 | kPa | KDB |
| Pc | 3200.00 ± 10.00 | kPa | NIST |
| Pc | 3200.00 ± 6.00 | kPa | NIST |
| Pc | 3170.00 ± 4.90 | kPa | NIST |
| Ptriple | 1.81e-07 | kPa | ChemSep v8.3 pure component data |
| ρc | [272.71; 272.83] | kg/m3 |
|
| ρc | 272.83 ± 1.20 | kg/m3 | NIST |
| ρc | 272.71 ± 3.61 | kg/m3 | NIST |
| Inp | [141.80; 980.00] |
|
|
| Inp | 943.00 | NIST | |
| Inp | 946.90 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 946.90 | NIST | |
| Inp | 938.65 | NIST | |
| Inp | 976.60 | NIST | |
| Inp | 938.87 | NIST | |
| Inp | 934.43 | NIST | |
| Inp | 956.30 | NIST | |
| Inp | 932.20 | NIST | |
| Inp | 937.20 | NIST | |
| Inp | 938.14 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 943.90 | NIST | |
| Inp | 964.60 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 947.50 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 937.70 | NIST | |
| Inp | 938.10 | NIST | |
| Inp | 941.80 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 932.70 | NIST | |
| Inp | 935.10 | NIST | |
| Inp | 949.30 | NIST | |
| Inp | 954.60 | NIST | |
| Inp | 960.70 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 932.70 | NIST | |
| Inp | 935.10 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 932.50 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 929.74 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 938.10 | NIST | |
| Inp | 938.10 | NIST | |
| Inp | 936.10 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 940.20 | NIST | |
| Inp | 932.60 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 955.30 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 946.15 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 944.40 | NIST | |
| Inp | 946.90 | NIST | |
| Inp | 950.50 | NIST | |
| Inp | 952.30 | NIST | |
| Inp | 933.50 | NIST | |
| Inp | 959.10 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 939.60 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 960.70 | NIST | |
| Inp | 935.40 | NIST | |
| Inp | 942.10 | NIST | |
| Inp | 939.60 | NIST | |
| Inp | 946.90 | NIST | |
| Inp | 950.50 | NIST | |
| Inp | 952.30 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 938.20 | NIST | |
| Inp | 938.65 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 963.90 | NIST | |
| Inp | 958.20 | NIST | |
| Inp | 960.80 | NIST | |
| Inp | 976.60 | NIST | |
| Inp | 971.50 | NIST | |
| Inp | 974.40 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 942.10 | NIST | |
| Inp | 938.87 | NIST | |
| Inp | 940.40 | NIST | |
| Inp | 935.60 | NIST | |
| Inp | 935.20 | NIST | |
| Inp | 939.50 | NIST | |
| Inp | 934.43 | NIST | |
| Inp | 937.74 | NIST | |
| Inp | 939.69 | NIST | |
| Inp | 950.62 | NIST | |
| Inp | 954.04 | NIST | |
| Inp | 956.30 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 964.41 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 957.90 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 960.70 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 947.50 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 936.30 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | Outlier 141.80 | NIST | |
| Inp | Outlier 149.30 | NIST | |
| Inp | Outlier 142.80 | NIST | |
| Inp | Outlier 145.10 | NIST | |
| Inp | Outlier 149.59 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 960.70 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 932.20 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 937.70 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 935.10 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 932.50 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 929.00 | NIST | |
| I | [1180.00; 1261.60] |
|
|
| I | 1210.10 | NIST | |
| I | 1245.20 | NIST | |
| I | 1250.70 | NIST | |
| I | Outlier 1256.10 | NIST | |
| I | Outlier 1261.60 | NIST | |
| I | 1238.50 | NIST | |
| I | 1239.50 | NIST | |
| I | 1205.40 | NIST | |
| I | 1190.30 | NIST | |
| I | 1230.00 | NIST | |
| I | 1239.00 | NIST | |
| I | 1247.00 | NIST | |
| I | 1222.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1219.00 | NIST | |
| I | 1231.40 | NIST | |
| I | 1203.00 | NIST | |
| I | 1216.00 | NIST | |
| I | 1217.00 | NIST | |
| I | 1221.00 | NIST | |
| I | 1212.00 | NIST | |
| I | 1226.00 | NIST | |
| I | 1207.00 | NIST | |
| I | 1212.00 | NIST | |
| I | 1207.00 | NIST | |
| I | 1204.00 | NIST | |
| I | 1203.00 | NIST | |
| I | 1206.00 | NIST | |
| I | 1213.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1213.00 | NIST | |
| I | 1217.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1212.00 | NIST | |
| I | 1213.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1207.00 | NIST | |
| I | 1222.00 | NIST | |
| I | 1224.00 | NIST | |
| I | 1237.00 | NIST | |
| I | 1247.00 | NIST | |
| I | Outlier 1258.00 | NIST | |
| I | 1212.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1210.00 | NIST | |
| I | 1211.00 | NIST | |
| I | 1224.00 | NIST | |
| I | 1194.00 | NIST | |
| I | 1206.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1196.00 | NIST | |
| I | 1194.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1214.00 | NIST | |
| I | 1210.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1210.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1196.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1222.00 | NIST | |
| I | 1212.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1210.00 | NIST | |
| I | 1217.00 | NIST | |
| I | 1213.00 | NIST | |
| I | 1188.00 | NIST | |
| S°gas | 397.86 | J/mol×K | NIST |
| S°liquid | 287.78 | J/mol×K | NIST |
| Tboil | [150.21; 434.20] | K |
|
| Tboil | 432.35 | K | ChemSep v8.3 pure component data |
| Tboil | 432.39 | K | KDB |
| Tboil | 432.40 | K | NIST |
| Tboil | 433.07 ± 0.30 | K | NIST |
| Tboil | 431.70 ± 1.00 | K | NIST |
| Tboil | 432.39 ± 0.10 | K | NIST |
| Tboil | 431.70 ± 0.60 | K | NIST |
| Tboil | 427.00 ± 15.00 | K | NIST |
| Tboil | 431.00 ± 5.00 | K | NIST |
| Tboil | 433.00 ± 3.00 | K | NIST |
| Tboil | 431.90 ± 1.00 | K | NIST |
| Tboil | 433.00 ± 2.00 | K | NIST |
| Tboil | Outlier 160.00 ± 2.00 | K | NIST |
| Tboil | 427.00 ± 10.00 | K | NIST |
| Tboil | 431.10 ± 0.50 | K | NIST |
| Tboil | 432.60 ± 0.30 | K | NIST |
| Tboil | 422.00 ± 4.00 | K | NIST |
| Tboil | 432.40 ± 0.60 | K | NIST |
| Tboil | 432.36 ± 0.03 | K | NIST |
| Tboil | 434.20 ± 2.00 | K | NIST |
| Tboil | 431.00 ± 3.00 | K | NIST |
| Tboil | 431.70 ± 0.50 | K | NIST |
| Tboil | 432.40 ± 0.15 | K | NIST |
| Tboil | Outlier 150.21 ± 0.02 | K | NIST |
| Tboil | 432.46 ± 0.25 | K | NIST |
| Tboil | 432.20 ± 0.30 | K | NIST |
| Tboil | 430.15 ± 2.00 | K | NIST |
| Tboil | 432.50 ± 0.15 | K | NIST |
| Tboil | 432.37 ± 0.06 | K | NIST |
| Tboil | 432.55 ± 0.20 | K | NIST |
| Tboil | 432.36 ± 0.10 | K | NIST |
| Tboil | 432.33 ± 0.30 | K | NIST |
| Tboil | 431.80 ± 0.70 | K | NIST |
| Tboil | 430.00 ± 3.00 | K | NIST |
| Tboil | 430.00 ± 2.00 | K | NIST |
| Tboil | 430.00 ± 4.00 | K | NIST |
| Tboil | 432.60 ± 0.20 | K | NIST |
| Tboil | 430.00 ± 5.00 | K | NIST |
| Tboil | 430.00 ± 6.00 | K | NIST |
| Tboil | 429.65 ± 2.00 | K | NIST |
| Tboil | 429.00 ± 4.00 | K | NIST |
| Tboil | 432.70 ± 0.20 | K | NIST |
| Tboil | 432.00 ± 2.00 | K | NIST |
| Tboil | 432.00 ± 3.00 | K | NIST |
| Tboil | 431.20 ± 1.00 | K | NIST |
| Tboil | 432.40 ± 0.50 | K | NIST |
| Tboil | 430.00 ± 2.00 | K | NIST |
| Tboil | 431.90 ± 1.50 | K | NIST |
| Tc | [638.24; 639.20] | K |
|
| Tc | 638.35 | K | ChemSep v8.3 pure component data |
| Tc | 638.35 | K | KDB |
| Tc | 638.40 ± 0.10 | K | NIST |
| Tc | 638.24 ± 0.10 | K | NIST |
| Tc | 638.36 ± 0.30 | K | NIST |
| Tc | Outlier 639.20 ± 0.40 | K | NIST |
| Tc | 638.80 ± 0.60 | K | NIST |
| Tfus | [171.28; 174.10] | K |
|
| Tfus | 174.10 | K | Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents |
| Tfus | 173.55 | K | ChemSep v8.3 pure component data |
| Tfus | 173.59 | K | KDB |
| Tfus | 173.53 | K | Aq. Solubility Prediction |
| Tfus | 171.50 ± 0.20 | K | NIST |
| Tfus | 173.08 ± 0.10 | K | NIST |
| Tfus | 173.95 ± 0.30 | K | NIST |
| Tfus | 173.56 ± 0.02 | K | NIST |
| Tfus | 173.58 ± 0.20 | K | NIST |
| Tfus | 171.28 ± 0.40 | K | NIST |
| Tfus | 171.64 ± 0.30 | K | NIST |
| Tfus | 173.40 ± 0.40 | K | NIST |
| Tfus | 173.69 ± 0.20 | K | NIST |
| Tfus | 171.60 ± 0.04 | K | NIST |
| Tfus | 173.57 ± 0.04 | K | NIST |
| Tfus | 173.59 ± 0.03 | K | NIST |
| Tfus | 173.65 ± 0.02 | K | NIST |
| Tfus | 173.06 ± 0.40 | K | NIST |
| Tfus | 174.00 ± 0.60 | K | NIST |
| Tfus | 171.60 ± 0.25 | K | NIST |
| Ttriple | [171.60; 173.59] | K |
|
| Ttriple | 173.55 | K | ChemSep v8.3 pure component data |
| Ttriple | 173.59 ± 0.01 | K | NIST |
| Ttriple | 171.60 ± 0.01 | K | NIST |
| Ttriple | 173.59 ± 0.01 | K | NIST |
| Ttriple | 171.60 ± 0.01 | K | NIST |
| UQi | 4.05 | ChemSep v8.3 pure component data | |
| URi | 5.27 | ChemSep v8.3 pure component data | |
| Vc | [0.440; 0.440] | m3/kmol |
|
| Vc | 0.440 | m3/kmol | ChemSep v8.3 pure component data |
| Vc | 0.440 | m3/kmol | KDB |
| Vc | 0.440 | m3/kmol | NIST |
| Zc | [0.2650000; 0.2652820] |
|
|
| Zc | 0.2650000 | ChemSep v8.3 pure component data | |
| Zc | 0.2652820 | KDB | |
| Zra | [0.26; 0.26] |
|
|
| Zra | 0.26 | ChemSep v8.3 pure component data | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [91.48; 416.51] | J/mol×K | [150.00; 1500.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 8.23700e+01 | |||
| Coefficient B | -6.22600e+02 | |||
| Coefficient C | 6.38124e+00 | |||
| Coefficient D | -1.43070e-04 | |||
| Coefficient E | 2.66580e-08 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 91.48 | J/mol×K | 150.00 | Calculated Property |
| Cp,gas | 153.56 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 221.96 | J/mol×K | 450.00 | Calculated Property |
| Cp,gas | 276.27 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | 317.19 | J/mol×K | 750.00 | Calculated Property |
| Cp,gas | 348.05 | J/mol×K | 900.00 | Calculated Property |
| Cp,gas | 371.67 | J/mol×K | 1050.00 | Calculated Property |
| Cp,gas | 390.07 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 404.68 | J/mol×K | 1350.00 | Calculated Property |
| Cp,gas | 416.51 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [181.30; 277.63] | J/mol×K | [173.55; 432.39] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 4.44290e+01 | |||
| Coefficient B | 6.58410e+01 | |||
| Coefficient C | 3.98924e+00 | |||
| Coefficient D | 3.26580e-03 | |||
| Coefficient E | -5.44020e-07 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 173.55 | |||
| Temperature range, max. | 432.39 | |||
| Cp,liquid | 181.30 | J/mol×K | 173.55 | Calculated Property |
| Cp,liquid | 186.05 | J/mol×K | 202.31 | Calculated Property |
| Cp,liquid | 192.81 | J/mol×K | 231.07 | Calculated Property |
| Cp,liquid | 201.15 | J/mol×K | 259.83 | Calculated Property |
| Cp,liquid | 210.86 | J/mol×K | 288.59 | Calculated Property |
| Cp,liquid | 221.82 | J/mol×K | 317.35 | Calculated Property |
| Cp,liquid | 233.98 | J/mol×K | 346.11 | Calculated Property |
| Cp,liquid | 247.32 | J/mol×K | 374.87 | Calculated Property |
| Cp,liquid | 261.87 | J/mol×K | 403.63 | Calculated Property |
| Cp,liquid | 277.63 | J/mol×K | 432.39 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0067720; 0.0001649] | Pa×s | [200.00; 510.68] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.56010e+01 | |||
| Coefficient B | 1.46790e+03 | |||
| Coefficient C | 6.10450e-01 | |||
| Coefficient D | 8.04420e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 510.68 | |||
| η | 0.0067720 | Pa×s | 200.00 | Calculated Property |
| η | 0.0025644 | Pa×s | 234.52 | Calculated Property |
| η | 0.0012667 | Pa×s | 269.04 | Calculated Property |
| η | 0.0007450 | Pa×s | 303.56 | Calculated Property |
| η | 0.0004943 | Pa×s | 338.08 | Calculated Property |
| η | 0.0003578 | Pa×s | 372.60 | Calculated Property |
| η | 0.0002764 | Pa×s | 407.12 | Calculated Property |
| η | 0.0002243 | Pa×s | 441.64 | Calculated Property |
| η | 0.0001893 | Pa×s | 476.16 | Calculated Property |
| η | 0.0001649 | Pa×s | 510.68 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [54.50; 0.00] | kJ/mol | [173.55; 638.35] |
ChemSep v8.3 pure component data
|
| 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 | 7.13120e+01 | |||
| Coefficient B | 1.04450e+00 | |||
| Coefficient C | -6.10760e-01 | |||
| Coefficient D | -5.95690e-01 | |||
| Coefficient E | 6.33320e-01 | |||
| Critical temperature, Tc (K) | 6.38350e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization, ChemSep Tmax 639.84 K | |||
| Temperature range, min. | 173.55 | |||
| Temperature range, max. | 638.35 | |||
| ΔvapH | 54.50 | kJ/mol | 173.55 | Calculated Property |
| ΔvapH | 50.73 | kJ/mol | 225.19 | Calculated Property |
| ΔvapH | 47.38 | kJ/mol | 276.84 | Calculated Property |
| ΔvapH | 44.30 | kJ/mol | 328.48 | Calculated Property |
| ΔvapH | 41.31 | kJ/mol | 380.13 | Calculated Property |
| ΔvapH | 38.13 | kJ/mol | 431.77 | Calculated Property |
| ΔvapH | 34.37 | kJ/mol | 483.42 | Calculated Property |
| ΔvapH | 29.37 | kJ/mol | 535.06 | Calculated Property |
| ΔvapH | 21.78 | kJ/mol | 586.71 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 638.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [315.30; 461.35] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.45214e+01 | |||
| Coefficient B | -3.81126e+03 | |||
| Coefficient C | -4.75350e+01 | |||
| Temperature range, min. | 315.30 | |||
| Temperature range, max. | 461.35 | |||
| Pvap | 1.33 | kPa | 315.30 | Calculated Property |
| Pvap | 3.01 | kPa | 331.53 | Calculated Property |
| Pvap | 6.21 | kPa | 347.76 | Calculated Property |
| Pvap | 11.91 | kPa | 363.98 | Calculated Property |
| Pvap | 21.44 | kPa | 380.21 | Calculated Property |
| Pvap | 36.52 | kPa | 396.44 | Calculated Property |
| Pvap | 59.35 | kPa | 412.67 | Calculated Property |
| Pvap | 92.53 | kPa | 428.89 | Calculated Property |
| Pvap | 139.14 | kPa | 445.12 | Calculated Property |
| Pvap | 202.63 | kPa | 461.35 | Calculated Property |
| Pvap | [1.85e-07; 3199.45] | kPa | [173.55; 638.35] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.39962e+01 | |||
| Coefficient B | -8.25450e+03 | |||
| Coefficient C | -1.01050e+01 | |||
| Coefficient D | 5.57690e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 173.55 | |||
| Temperature range, max. | 638.35 | |||
| Pvap | 1.85e-07 | kPa | 173.55 | Calculated Property |
| Pvap | 8.13e-04 | kPa | 225.19 | Calculated Property |
| Pvap | 0.11 | kPa | 276.84 | Calculated Property |
| Pvap | 2.50 | kPa | 328.48 | Calculated Property |
| Pvap | 21.29 | kPa | 380.13 | Calculated Property |
| Pvap | 99.69 | kPa | 431.77 | Calculated Property |
| Pvap | 319.39 | kPa | 483.42 | Calculated Property |
| Pvap | 798.06 | kPa | 535.06 | Calculated Property |
| Pvap | 1689.44 | kPa | 586.71 | Calculated Property |
| Pvap | 3199.45 | kPa | 638.35 | Calculated Property |
| Pvap | [1.53e-07; 3180.46] | kPa | [173.67; 638.38] |
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 | 8.95794e+01 | |||
| Coefficient B | -8.51249e+03 | |||
| Coefficient C | -1.09449e+01 | |||
| Coefficient D | 6.16532e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 173.67 | |||
| Temperature range, max. | 638.38 | |||
| Pvap | 1.53e-07 | kPa | 173.67 | Calculated Property |
| Pvap | 7.59e-04 | kPa | 225.30 | Calculated Property |
| Pvap | 0.11 | kPa | 276.94 | Calculated Property |
| Pvap | 2.49 | kPa | 328.57 | Calculated Property |
| Pvap | 21.34 | kPa | 380.21 | Calculated Property |
| Pvap | 99.74 | kPa | 431.84 | Calculated Property |
| Pvap | 318.30 | kPa | 483.48 | Calculated Property |
| Pvap | 792.82 | kPa | 535.11 | Calculated Property |
| Pvap | 1676.46 | kPa | 586.75 | Calculated Property |
| Pvap | 3180.46 | kPa | 638.38 | Calculated Property |
| Pvap | [6.41; 104.13] | kPa | [348.97; 433.39] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39901e+01 | |||
| Coefficient B | -3.43307e+03 | |||
| Coefficient C | -6.60000e+01 | |||
| Reference | Forziati, Norris, et al., 1949, 2 | |||
| Temperature range, min. | 348.97 | |||
| Temperature range, max. | 433.39 | |||
| Pvap | 6.41 | kPa | 348.97 | Calculated Property |
| Pvap | 9.46 | kPa | 358.35 | Calculated Property |
| Pvap | 13.63 | kPa | 367.73 | Calculated Property |
| Pvap | 19.21 | kPa | 377.11 | Calculated Property |
| Pvap | 26.53 | kPa | 386.49 | Calculated Property |
| Pvap | 35.97 | kPa | 395.87 | Calculated Property |
| Pvap | 47.97 | kPa | 405.25 | Calculated Property |
| Pvap | 62.98 | kPa | 414.63 | Calculated Property |
| Pvap | 81.52 | kPa | 424.01 | Calculated Property |
| Pvap | 104.13 | kPa | 433.39 | Calculated Property |
| Pvap | [6.41; 104.13] | kPa | [348.97; 433.39] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39901e+01 | |||
| Coefficient B | -3.43307e+03 | |||
| Coefficient C | -6.60000e+01 | |||
| Reference | Forziati, Norris, et al., 1949 | |||
| Temperature range, min. | 348.97 | |||
| Temperature range, max. | 433.39 | |||
| Pvap | 6.41 | kPa | 348.97 | Calculated Property |
| Pvap | 9.46 | kPa | 358.35 | Calculated Property |
| Pvap | 13.63 | kPa | 367.73 | Calculated Property |
| Pvap | 19.21 | kPa | 377.11 | Calculated Property |
| Pvap | 26.53 | kPa | 386.49 | Calculated Property |
| Pvap | 35.97 | kPa | 395.87 | Calculated Property |
| Pvap | 47.97 | kPa | 405.25 | Calculated Property |
| Pvap | 62.98 | kPa | 414.63 | Calculated Property |
| Pvap | 81.52 | kPa | 424.01 | Calculated Property |
| Pvap | 104.13 | kPa | 433.39 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [959.27; 272.25] | kg/m3 | [173.15; 638.35] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 6.83554e+01 | |||
| Coefficient B | 2.51080e-01 | |||
| Coefficient C | 6.38350e+02 | |||
| Coefficient D | 2.93370e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 173.15 | |||
| Temperature range, max. | 638.35 | |||
| ρl | 959.27 | kg/m3 | 173.15 | Calculated Property |
| ρl | 919.10 | kg/m3 | 224.84 | Calculated Property |
| ρl | 877.13 | kg/m3 | 276.53 | Calculated Property |
| ρl | 832.91 | kg/m3 | 328.22 | Calculated Property |
| ρl | 785.79 | kg/m3 | 379.91 | Calculated Property |
| ρl | 734.74 | kg/m3 | 431.59 | Calculated Property |
| ρl | 678.01 | kg/m3 | 483.28 | Calculated Property |
| ρl | 612.06 | kg/m3 | 534.97 | Calculated Property |
| ρl | 527.30 | kg/m3 | 586.66 | Calculated Property |
| ρl | 272.25 | kg/m3 | 638.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 1.95e-05] | N/m | [173.55; 633.24] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.01790e-02 | |||
| Coefficient B | 3.15650e+01 | |||
| Coefficient C | -3.02340e+00 | |||
| Coefficient D | 1.39090e-04 | |||
| Coefficient E | -4.23960e-06 | |||
| Comment | ChemSep eq 16, SurfaceTension, ChemSep Tmax 638.35 K | |||
| Temperature range, min. | 173.55 | |||
| Temperature range, max. | 633.24 | |||
| γ | 0.04 | N/m | 173.55 | Calculated Property |
| γ | 0.04 | N/m | 224.63 | Calculated Property |
| γ | 0.03 | N/m | 275.70 | Calculated Property |
| γ | 0.03 | N/m | 326.78 | Calculated Property |
| γ | 0.02 | N/m | 377.86 | Calculated Property |
| γ | 0.02 | N/m | 428.93 | Calculated Property |
| γ | 0.01 | N/m | 480.01 | Calculated Property |
| γ | 0.01 | N/m | 531.08 | Calculated Property |
| γ | 0.00 | N/m | 582.16 | Calculated Property |
| γ | 1.95e-05 | N/m | 633.24 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.00; 0.08] | W/m×K | [173.55; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 2.50180e-02 | |||
| Coefficient B | 2.67280e-01 | |||
| Coefficient C | 1.00660e+02 | |||
| Coefficient D | 9.71170e+05 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 173.55 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.00 | W/m×K | 173.55 | Calculated Property |
| λ | 0.01 | W/m×K | 265.38 | Calculated Property |
| λ | 0.01 | W/m×K | 357.21 | Calculated Property |
| λ | 0.02 | W/m×K | 449.03 | Calculated Property |
| λ | 0.03 | W/m×K | 540.86 | Calculated Property |
| λ | 0.04 | W/m×K | 632.69 | Calculated Property |
| λ | 0.05 | W/m×K | 724.52 | Calculated Property |
| λ | 0.06 | W/m×K | 816.34 | Calculated Property |
| λ | 0.07 | W/m×K | 908.17 | Calculated Property |
| λ | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.15; 0.07] | W/m×K | [173.55; 583.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | -8.13910e-02 | |||
| Coefficient B | 2.87000e+00 | |||
| Coefficient C | -1.34550e+00 | |||
| Coefficient D | -6.18350e-04 | |||
| Coefficient E | -5.16640e-07 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 173.55 | |||
| Temperature range, max. | 583.15 | |||
| λ | 0.15 | W/m×K | 173.55 | Calculated Property |
| λ | 0.14 | W/m×K | 219.06 | Calculated Property |
| λ | 0.13 | W/m×K | 264.57 | Calculated Property |
| λ | 0.13 | W/m×K | 310.08 | Calculated Property |
| λ | 0.12 | W/m×K | 355.59 | Calculated Property |
| λ | 0.11 | W/m×K | 401.11 | Calculated Property |
| λ | 0.10 | W/m×K | 446.62 | Calculated Property |
| λ | 0.09 | W/m×K | 492.13 | Calculated Property |
| λ | 0.08 | W/m×K | 537.64 | Calculated Property |
| λ | 0.07 | W/m×K | 583.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, propyl-.
Mixtures
- Dodecane + 2-Pyrrolidinone, 1-methyl- + Benzene, propyl-
- 2-Pyrrolidinone, 1-methyl- + Benzene, propyl- + Tetradecane
- Heptadecane + 2-Pyrrolidinone, 1-methyl- + Benzene, propyl-
- Hexadecane + Benzene, propyl-
- Benzene, propyl- + Ethane, 1,1,2,2-tetrachloro-
- Acetic acid, pentyl ester + Benzene, propyl-
- Octane + Benzene, propyl- + Benzene, ethyl-
- Benzene, propyl- + Water
- Propanamide, N,N-bis(2-ethylhexyl)-2-methyl- + Benzene, propyl-
- Benzene, propyl- + Cyclohexylamine + Water
- Benzene, chloro- + Benzene, propyl-
- Benzene, propyl- + Benzene, (chloromethyl)-
- Benzene, (2-chloroethyl)- + Benzene, propyl-
- Benzene, (3-chloropropyl)- + Benzene, propyl-
- Benzene, propyl- + Anisole
Sources
- KDB Vapor Pressure Data
- 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
- Liquid liquid equilibria for n-alkanes (C12, C14, C17) + propylbenzene +NMP mixtures at temperatures between 298 and 328K
- 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
- (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
- Separation of propylbenzene and n-alkanes from their mixtures using 4-methyl-N-butylpyridinium tetrafluoroborate as an ionic solvent at several temperatures
- Extraction of propylbenzene from its mixtures with heptadecane using 4-methyl-N-butylpyridinium tetrafluoroborate
- Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- 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
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
- 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
- Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
- Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
- Evaluation of [bmim][PF6] as an ionic solvent for the extraction of propylbenzene from aliphatic compounds
- Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
- The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- 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
- Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
- Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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