- InChI
- InChI=1S/C9H12/c1-8(2)9-6-4-3-5-7-9/h3-8H,1-2H3
- InChI Key
- RWGFKTVRMDUZSP-UHFFFAOYSA-N
- Formula
- C9H12
- SMILES
- CC(C)c1ccccc1
- Molecular Weight1
- 120.19
- CAS
- 98-82-8
- Other Names
-
- (1-METHYLETHYL)BENZENE
- (1-methylethyl)benzene (cumene)
- (Methylethyl)benzene
- 1-methylethylbenzene
- 2-Fenilpropano
- 2-Fenyl-propaan
- 2-PHENYLPROPANE
- Benzene, i-propyl-
- Benzene, isopropyl-
- Cumeen
- Cumene
- Cumol
- ISOPROPYLBENZENE
- Isopropilbenzene
- Isopropylbenzeen
- Isopropylbenzol
- NSC 8776
- Propane, 2-phenyl-
- Rcra waste number U055
- UN 1918
- i-Propylbenzene
- iso-propylbenzene
- iso-propylbenzene (cumene)
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- 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).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- 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.
- 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3260 | KDB | |
| PAff | 791.60 | kJ/mol | NIST |
| Tig | 698.15 | K | KDB |
| BasG | 763.90 | kJ/mol | NIST |
| ΔcH°liquid | [-5218.60; -5215.44] | kJ/mol |
|
| ΔcH°liquid | -5215.44 ± 0.96 | kJ/mol | NIST |
| ΔcH°liquid | -5218.60 | kJ/mol | NIST |
| Cp,liquid | 214.75 | J/mol×K | Thermod... |
| η | [0.0007390; 0.0007390] | Pa×s |
|
| η | 0.0007390 | Pa×s | Viscosi... |
| η | 0.0007390 | Pa×s | Viscosi... |
| LFL | 0.90 | % in Air | KDB |
| UFL | 6.50 | % in Air | KDB |
| Tflash,oc | 317.04 | K | KDB |
| ΔfG° | 137.10 | kJ/mol | KDB |
| Δc,grossH | 5215.44 | kJ/mol | KDB |
| Δc,netH | 4951.346 | kJ/mol | KDB |
| ΔfH°gas | [3.90; 3.94] | kJ/mol |
|
| ΔfH°gas | 3.94 | kJ/mol | KDB |
| ΔfH°gas | 3.90 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -41.20 ± 1.10 | kJ/mol | NIST |
| ΔfusH° | 9.58 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [37.00; 45.15] | kJ/mol |
|
| ΔvapH° | 45.15 | kJ/mol | NIST |
| ΔvapH° | 45.10 | kJ/mol | NIST |
| ΔvapH° | 45.10 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 44.00 | kJ/mol | NIST |
| ΔvapH° | 45.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 37.00 | kJ/mol | NIST |
| ΔvapH° | 45.10 | kJ/mol | NIST |
| ΔvapH° | 45.14 | kJ/mol | NIST |
| ΔvapH° | 45.10 | kJ/mol | NIST |
| IE | [8.69; 8.98] | eV |
|
| IE | 8.73 ± 0.02 | eV | NIST |
| IE | 8.72 | eV | NIST |
| IE | 8.72 ± 0.01 | eV | NIST |
| IE | 8.69 ± 0.01 | eV | NIST |
| IE | 8.76 | eV | NIST |
| IE | 8.71 | eV | NIST |
| IE | 8.75 | eV | NIST |
| IE | Outlier 8.98 | eV | NIST |
| log10WS | [-3.27; -3.27] |
|
|
| log10WS | -3.27 | Aq. Sol... | |
| log10WS | -3.27 | Estimat... | |
| logPoct/wat | 2.810 | Crippen Calculated Property | |
| McVol | 113.910 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| Pc | [2786.44; 3210.00] | kPa |
|
| Pc | 3209.00 | kPa | KDB |
| Pc | 3210.00 ± 40.00 | kPa | NIST |
| Pc | 3209.00 ± 6.00 | kPa | NIST |
| Pc | 2786.44 ± 151.99 | kPa | NIST |
| Pc | 3160.00 ± 5.88 | kPa | NIST |
| ρc | 278.84 ± 0.96 | kg/m3 | NIST |
| Inp | [134.00; 961.00] |
|
|
| Inp | 909.10 | NIST | |
| Inp | 909.82 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 935.10 | NIST | |
| Inp | 942.50 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.50 | NIST | |
| Inp | 919.20 | NIST | |
| Inp | 920.10 | NIST | |
| Inp | 920.70 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 892.90 | NIST | |
| Inp | 898.20 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 909.30 | NIST | |
| Inp | 909.80 | NIST | |
| Inp | 911.30 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 904.10 | NIST | |
| Inp | 906.70 | NIST | |
| Inp | 920.40 | NIST | |
| Inp | 925.60 | NIST | |
| Inp | 931.80 | NIST | |
| Inp | 915.50 | NIST | |
| Inp | 900.30 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 903.40 | NIST | |
| Inp | 903.90 | NIST | |
| Inp | 904.10 | NIST | |
| Inp | 904.10 | NIST | |
| Inp | 906.70 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 910.10 | NIST | |
| Inp | 910.10 | NIST | |
| Inp | 910.10 | NIST | |
| Inp | 910.10 | NIST | |
| Inp | 910.10 | NIST | |
| Inp | 910.10 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 903.10 | NIST | |
| Inp | 910.80 | NIST | |
| Inp | 903.50 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 925.10 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 912.20 | NIST | |
| Inp | 912.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 914.30 | NIST | |
| Inp | 919.40 | NIST | |
| Inp | 922.20 | NIST | |
| Inp | 923.60 | NIST | |
| Inp | 906.90 | NIST | |
| Inp | 930.30 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 910.80 | NIST | |
| Inp | 928.70 | NIST | |
| Inp | 907.20 | NIST | |
| Inp | 907.90 | NIST | |
| Inp | 919.40 | NIST | |
| Inp | 922.20 | NIST | |
| Inp | 923.60 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 909.43 | NIST | |
| Inp | 909.62 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 934.30 | NIST | |
| Inp | 929.20 | NIST | |
| Inp | 931.60 | NIST | |
| Inp | 946.50 | NIST | |
| Inp | 941.60 | NIST | |
| Inp | 944.90 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 914.90 | NIST | |
| Inp | 909.07 | NIST | |
| Inp | 910.70 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 905.10 | NIST | |
| Inp | 911.30 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 936.10 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 912.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 912.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 930.70 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 912.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 907.50 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | Outlier 134.00 | NIST | |
| I | [1150.00; 1236.00] |
|
|
| I | 1158.00 | NIST | |
| I | 1176.90 | NIST | |
| I | 1202.10 | NIST | |
| I | 1203.60 | NIST | |
| I | 1169.80 | NIST | |
| I | 1154.90 | NIST | |
| I | Outlier 1232.00 | NIST | |
| I | Outlier 1236.00 | NIST | |
| I | 1198.00 | NIST | |
| I | 1205.00 | NIST | |
| I | 1213.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1192.30 | NIST | |
| I | 1177.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1211.00 | NIST | |
| I | Outlier 1225.00 | NIST | |
| I | 1169.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1155.00 | NIST | |
| I | 1168.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1168.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1171.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1155.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1169.00 | NIST | |
| S°gas | 386.53 | J/mol×K | NIST |
| S°liquid | 277.57 | J/mol×K | NIST |
| Tboil | [425.44; 425.63] | K |
|
| Tboil | 425.56 | K | KDB |
| Tboil | 425.55 | K | Isobari... |
| Tboil | 425.55 | K | Isobari... |
| Tboil | 425.44 | K | Isobari... |
| Tboil | 425.63 | K | Experim... |
| Tboil | 425.44 | K | Vapor-L... |
| Tc | [624.55; 635.90] | K |
|
| Tc | 631.00 | K | KDB |
| Tc | 631.00 ± 0.50 | K | NIST |
| Tc | 631.10 ± 0.15 | K | NIST |
| Tc | 624.55 ± 2.00 | K | NIST |
| Tc | 635.90 ± 4.00 | K | NIST |
| Tfus | 177.14 | K | KDB |
| Ttriple | 177.13 ± 0.01 | K | NIST |
| Vc | 0.435 | m3/kmol | KDB |
| Zc | 0.2658850 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [214.82; 289.96] | J/mol×K | [431.56; 643.71] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 220 240 260 280 450 500 550 600 | ||||
| Cp,gas | 214.82 | J/mol×K | 431.56 | Joback Calculated Property |
| Cp,gas | 229.30 | J/mol×K | 466.92 | Joback Calculated Property |
| Cp,gas | 242.96 | J/mol×K | 502.28 | Joback Calculated Property |
| Cp,gas | 255.82 | J/mol×K | 537.64 | Joback Calculated Property |
| Cp,gas | 267.92 | J/mol×K | 573.00 | Joback Calculated Property |
| Cp,gas | 279.29 | J/mol×K | 608.35 | Joback Calculated Property |
| Cp,gas | 289.96 | J/mol×K | 643.71 | Joback Calculated Property |
| Cp,liquid | [198.70; 215.40] | J/mol×K | [295.96; 302.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 200 205 210 215 296 298 300 302 | ||||
| Cp,liquid | 214.40 | J/mol×K | 295.96 | NIST |
| Cp,liquid | 213.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 215.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 209.41 | J/mol×K | 299.80 | NIST |
| Cp,liquid | 198.70 | J/mol×K | 302.00 | NIST |
| Cp,liquid | 198.70 | J/mol×K | 302.00 | NIST |
| η | [0.0006110; 0.0006900] | Pa×s | [303.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 6.20e-4 6.40e-4 6.60e-4 6.80e-4 305 310 | ||||
| η | 0.0006900 | Pa×s | 303.15 | Physica... |
| η | 0.0006900 | Pa×s | 303.15 | Density... |
| η | 0.0006510 | Pa×s | 308.15 | Physica... |
| η | 0.0006510 | Pa×s | 308.15 | Density... |
| η | 0.0006110 | Pa×s | 313.15 | Physica... |
| η | 0.0006110 | Pa×s | 313.15 | Density... |
| ΔfusH | [7.32; 7.33] | kJ/mol | [177.10; 177.13] |
|
| ΔfusH | 7.32 | kJ/mol | 177.10 | NIST |
| ΔfusH | 7.32 | kJ/mol | 177.10 | NIST |
| ΔfusH | 7.33 | kJ/mol | 177.13 | NIST |
| ΔvapH | [41.20; 42.10] | kJ/mol | [384.50; 387.50] |
|
| ΔvapH | 41.90 | kJ/mol | 384.50 | NIST |
| ΔvapH | 42.10 | kJ/mol | 386.00 | NIST |
| ΔvapH | 41.20 | kJ/mol | 387.50 | NIST |
| n0 | [1.48869; 1.49130] | [293.15; 298.20] |
|
|
|
T(K) Refractive Index 1.49 1.49 1.49 1.49 1.49 1.49 1.49 294 296 298 | ||||
| n0 | 1.49130 | 293.15 | Liquid ... | |
| n0 | 1.49120 | 293.15 | Experim... | |
| n0 | 1.48890 | 298.15 | KDB | |
| n0 | 1.48869 | 298.15 | Effect ... | |
| n0 | 1.49005 | 298.20 | Salt Ef... | |
| ρl | [857.51; 864.12] | kg/m3 | [293.00; 298.20] |
|
| ρl | 862.00 | kg/m3 | 293.00 | KDB |
| ρl | 857.51 | kg/m3 | 298.15 | Thermod... |
| ρl | 864.12 | kg/m3 | 298.15 | Liquid-... |
| ρl | 857.54 | kg/m3 | 298.20 | Liquid-... |
| ΔfusS | [41.36; 41.37] | J/mol×K | [177.10; 177.13] |
|
| ΔfusS | 41.37 | J/mol×K | 177.10 | NIST |
| ΔfusS | 41.36 | J/mol×K | 177.13 | NIST |
| γ | 0.03 | N/m | 293.20 | KDB |
| λ | [0.11; 0.13] | W/m×K | [261.13; 329.83] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.11 0.11 0.12 0.12 0.12 0.12 0.12 0.13 260 280 300 320 | ||||
| λ | 0.13 | W/m×K | 261.13 | Thermal... |
| λ | 0.13 | W/m×K | 261.33 | Thermal... |
| λ | 0.13 | W/m×K | 261.48 | Thermal... |
| λ | 0.12 | W/m×K | 275.03 | Thermal... |
| λ | 0.12 | W/m×K | 275.24 | Thermal... |
| λ | 0.12 | W/m×K | 275.40 | Thermal... |
| λ | 0.12 | W/m×K | 294.11 | Thermal... |
| λ | 0.12 | W/m×K | 294.32 | Thermal... |
| λ | 0.12 | W/m×K | 294.47 | Thermal... |
| λ | 0.12 | W/m×K | 312.46 | Thermal... |
| λ | 0.12 | W/m×K | 312.68 | Thermal... |
| λ | 0.12 | W/m×K | 312.84 | Thermal... |
| λ | 0.11 | W/m×K | 329.45 | Thermal... |
| λ | 0.11 | W/m×K | 329.68 | Thermal... |
| λ | 0.11 | W/m×K | 329.83 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 857.94 |
| 313.15 | 100.00 | 845.05 |
| 333.15 | 100.00 | 827.73 |
| 353.15 | 100.00 | 810.17 |
| 373.15 | 100.00 | 792.31 |
| 393.15 | 100.00 | 773.98 |
| 413.15 | 100.00 | 755.04 |
| 433.15 | 10100.00 | 752.29 |
| 298.15 | 20100.00 | 871.79 |
| 313.15 | 20100.00 | 859.97 |
| 333.15 | 20100.00 | 844.44 |
| 353.15 | 20100.00 | 828.86 |
| 373.15 | 20100.00 | 813.36 |
| 393.15 | 20100.00 | 797.74 |
| 413.15 | 20100.00 | 781.98 |
| 433.15 | 20100.00 | 766.12 |
| 298.15 | 40100.00 | 883.81 |
| 313.15 | 40100.00 | 872.84 |
| 333.15 | 40100.00 | 858.51 |
| 353.15 | 40100.00 | 844.27 |
| 373.15 | 40100.00 | 830.23 |
| 393.15 | 40100.00 | 816.2 |
| 413.15 | 40100.00 | 802.25 |
| 433.15 | 40100.00 | 788.34 |
| 298.15 | 60100.00 | 894.47 |
| 313.15 | 60100.00 | 884.19 |
| 333.15 | 60100.00 | 870.78 |
| 353.15 | 60100.00 | 857.52 |
| 373.15 | 60100.00 | 844.51 |
| 393.15 | 60100.00 | 831.6 |
| 413.15 | 60100.00 | 818.85 |
| 433.15 | 60100.00 | 806.14 |
| 298.15 | 80100.00 | 904.16 |
| 313.15 | 80100.00 | 894.38 |
| 333.15 | 80100.00 | 881.68 |
| 353.15 | 80100.00 | 869.22 |
| 373.15 | 80100.00 | 857.0 |
| 393.15 | 80100.00 | 844.92 |
| 413.15 | 80100.00 | 833.04 |
| 433.15 | 80100.00 | 821.27 |
| 298.15 | 100100.00 | 913.02 |
| 313.15 | 100100.00 | 903.69 |
| 333.15 | 100100.00 | 891.56 |
| 353.15 | 100100.00 | 879.74 |
| 373.15 | 100100.00 | 868.11 |
| 393.15 | 100100.00 | 856.72 |
| 413.15 | 100100.00 | 845.53 |
| 433.15 | 100100.00 | 834.45 |
| Reference | ||
Speed of sound, m/s
Operational condition: Frequency, MHz = 3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 100.00 | 1309.1 |
| 313.15 | 100.00 | 1247.6 |
| 333.15 | 100.00 | 1168.5 |
| 353.15 | 100.00 | 1091.8 |
| 373.15 | 100.00 | 1017.8 |
| 393.15 | 100.00 | 945.6 |
| 413.15 | 100.00 | 875.0 |
| 433.15 | 10100.00 | 897.7 |
| 298.15 | 20100.00 | 1406.9 |
| 313.15 | 20100.00 | 1351.3 |
| 333.15 | 20100.00 | 1280.5 |
| 353.15 | 20100.00 | 1213.2 |
| 373.15 | 20100.00 | 1149.2 |
| 393.15 | 20100.00 | 1088.1 |
| 413.15 | 20100.00 | 1029.6 |
| 433.15 | 20100.00 | 974.0 |
| 298.15 | 40100.00 | 1491.7 |
| 313.15 | 40100.00 | 1440.0 |
| 333.15 | 40100.00 | 1374.7 |
| 353.15 | 40100.00 | 1313.2 |
| 373.15 | 40100.00 | 1255.1 |
| 393.15 | 40100.00 | 1200.1 |
| 413.15 | 40100.00 | 1147.8 |
| 433.15 | 40100.00 | 1098.9 |
| 298.15 | 60100.00 | 1566.8 |
| 313.15 | 60100.00 | 1518.3 |
| 333.15 | 60100.00 | 1457.2 |
| 353.15 | 60100.00 | 1399.6 |
| 373.15 | 60100.00 | 1345.6 |
| 393.15 | 60100.00 | 1294.7 |
| 413.15 | 60100.00 | 1246.5 |
| 433.15 | 60100.00 | 1201.3 |
| 298.15 | 80100.00 | 1634.8 |
| 313.15 | 80100.00 | 1588.9 |
| 333.15 | 80100.00 | 1530.9 |
| 353.15 | 80100.00 | 1476.5 |
| 373.15 | 80100.00 | 1425.6 |
| 393.15 | 80100.00 | 1377.6 |
| 413.15 | 80100.00 | 1332.1 |
| 433.15 | 80100.00 | 1289.9 |
| 298.15 | 100100.00 | 1697.4 |
| 313.15 | 100100.00 | 1653.3 |
| 333.15 | 100100.00 | 1598.0 |
| 353.15 | 100100.00 | 1546.0 |
| 373.15 | 100100.00 | 1497.4 |
| 393.15 | 100100.00 | 1451.6 |
| 413.15 | 100100.00 | 1408.6 |
| 433.15 | 100100.00 | 1368.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [310.56; 454.20] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.43493e+01 | |||
| Coefficient B | -3.63341e+03 | |||
| Coefficient C | -5.21730e+01 | |||
| Temperature range, min. | 310.56 | |||
| Temperature range, max. | 454.20 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 310.56 | Calculated Property |
| Pvap | 3.02 | kPa | 326.52 | Calculated Property |
| Pvap | 6.26 | kPa | 342.48 | Calculated Property |
| Pvap | 12.01 | kPa | 358.44 | Calculated Property |
| Pvap | 21.61 | kPa | 374.40 | Calculated Property |
| Pvap | 36.80 | kPa | 390.36 | Calculated Property |
| Pvap | 59.72 | kPa | 406.32 | Calculated Property |
| Pvap | 92.95 | kPa | 422.28 | Calculated Property |
| Pvap | 139.48 | kPa | 438.24 | Calculated Property |
| Pvap | 202.66 | kPa | 454.20 | Calculated Property |
| Pvap | [3.82e-07; 3143.15] | kPa | [177.14; 631.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.02480e+02 | |||
| Coefficient B | -8.96989e+03 | |||
| Coefficient C | -1.29151e+01 | |||
| Coefficient D | 7.67090e-06 | |||
| Temperature range, min. | 177.14 | |||
| Temperature range, max. | 631.15 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 400 600 | ||||
| Pvap | 3.82e-07 | kPa | 177.14 | Calculated Property |
| Pvap | 1.32e-03 | kPa | 227.59 | Calculated Property |
| Pvap | 0.15 | kPa | 278.03 | Calculated Property |
| Pvap | 3.20 | kPa | 328.48 | Calculated Property |
| Pvap | 25.23 | kPa | 378.92 | Calculated Property |
| Pvap | 110.81 | kPa | 429.37 | Calculated Property |
| Pvap | 337.42 | kPa | 479.81 | Calculated Property |
| Pvap | 812.07 | kPa | 530.26 | Calculated Property |
| Pvap | 1677.90 | kPa | 580.70 | Calculated Property |
| Pvap | 3143.15 | kPa | 631.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, (1-methylethyl)-.
Mixtures
- Benzene, (1-methylethyl)- + Acetic acid, butyl ester
- Benzene, (1-methylethyl)- + Formic acid + Water
- Benzene, (1-methylethyl)- + Acetic acid + Water
- Benzene, (1-methylethyl)- + Propanoic acid + Water
- Benzene, (1-methylethyl)- + Ethane, 1,1,2,2-tetrachloro-
- Benzene, (1-methylethyl)- + Benzonitrile
- Benzene, (1-methylethyl)- + Thiophene, tetrahydro-, 1,1-dioxide
- Benzene, (1-methylethyl)- + N-Formylmorpholine
- Benzene, (1-methylethyl)- + Water
- Benzene, (1-methylethyl)- + Phenol + Water
- Benzene, (1-methylethyl)- + sodium chloride + Water
- Benzene, (1-methylethyl)- + Sodium sulfate + Water
- 2-Butanone + Benzene, (1-methylethyl)-
- Methyl Isobutyl Ketone + Benzene, (1-methylethyl)-
- Benzene, (1-methylethyl)- + Benzaldehyde
- Ethyl formate + Benzene, (1-methylethyl)-
- Benzene, (1-methylethyl)- + Acetic acid ethenyl ester
- Benzene, (1-methylethyl)- + Tetrahydrofuran
- Benzene, (1-methylethyl)- + Tetrahydropyran
- Benzene, (1-methylethyl)- + Acetamide, N-methyl-
Find more mixtures with Benzene, (1-methylethyl)-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
- Liquid liquid equilibria of ternary systems (water + carboxylic acid + cumene) at 298.15K
- Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
- Thermodynamics of risperidone and solubility in pure organic solvents
- Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
- 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
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Liquid density measurements of cumene, tert-butylbenzene, and hexadecane over wide ranges of temperature and pressure
- 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
- Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
- LLE data for the ionic liquid 3-methyl-N-butyl pyridinium dicyanamide with several aromatic and aliphatic hydrocarbons
- Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
- Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Experimental and correlational study of phase equilibria in aqueous mixtures of phosphoric acid with aromatic hydrocarbons at various temperatures
- 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
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamic properties of cumene, tert-butylbenzene, and n-hexadecane under elevated pressures
- Liquid-Liquid Equilibrium of the Ternary System of Water + Phenol + (Propan-2-yl) Benzene at Several Temperatures
- Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
- Salt Effects on Liquid-Liquid Equilibria of Water + Phenol + (Propan-2-yl) Benzene + Salts Systems
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K
- Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
- Liquid-Liquid Equilibrium of (Water + Acetone) with Cumene or r-Methylstyrene or Phenol at Temperatures of (323.15 and 333.15) K
- Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
- Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
- Salting-Out Effect of NaCl and KCl on the Liquid Liquid Equilibrium of Water + 2-Methylpropanoic Acid + (1-Methylethyl)-benzene System at Several Temperatures
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Isobaric Vapor Liquid Equilibrium of Binary Mixtures of Vinyl Acetate and Ethyl Formate with Cumene at 97.3 kPa
- Experimental Isobaric Vapor-Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene
- Vapor-Liquid Equilibrium Data for N-Methylacetamide and N,N-Dimethylacetamide with Cumene at 97.3 kPa
- 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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