- InChI
- InChI=1S/C12H18O/c1-8(2)10-6-5-7-11(9(3)4)12(10)13/h5-9,13H,1-4H3
- InChI Key
- OLBCVFGFOZPWHH-UHFFFAOYSA-N
- Formula
- C12H18O
- SMILES
- CC(C)c1cccc(C(C)C)c1O
- Molecular Weight1
- 178.27
- CAS
- 2078-54-8
- Other Names
-
- 2,6-Bis(1-methylethyl)phenol
- 2,6-Diisopropylphenol
- 2,6-bis(Isopropyl)phenol
- Ampofol
- Aquafol
- Diprifusor
- Diprivan
- Diprivan 10
- Diprofol
- Disoprivan
- Disoprofol
- Fresofol
- ICI 35868
- Ivofol
- NSC 5105
- Phenol, 2,6-bis(1-methylethyl)-
- Phenol, 2,6-diisopropyl-
- Pofol
- Propofol-lipuro
- Propovan
- Rapinovet
- Recofol
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- Pc : Critical Pressure (kPa).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -6962.00 | kJ/mol | NIST |
| ΔfH°gas | [-254.10; -244.40] | kJ/mol |
|
| ΔfH°gas | -254.10 ± 2.80 | kJ/mol | NIST |
| ΔfH°gas | -244.40 | kJ/mol | NIST |
| ΔfH°liquid | -330.00 | kJ/mol | NIST |
| ΔfusH° | 19.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [68.70; 86.11] | kJ/mol |
|
| ΔvapH° | 68.70 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 86.11 | kJ/mol | NIST |
| ΔvapH° | 85.60 | kJ/mol | NIST |
| IE | 8.01 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.41 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.639 | Crippen Calculated Property | |
| McVol | 162.050 | ml/mol | McGowan Calculated Property |
| Pc | 2802.44 | kPa | Joback Calculated Property |
| Inp | [235.30; 1365.60] |
|
|
| Inp | 1364.80 | NIST | |
| Inp | 1334.60 | NIST | |
| Inp | 1361.10 | NIST | |
| Inp | 1362.70 | NIST | |
| Inp | 1365.60 | NIST | |
| Inp | 1346.00 | NIST | |
| Inp | 1335.00 | NIST | |
| Inp | Outlier 235.30 | NIST | |
| Inp | 1364.80 | NIST | |
| Inp | 1346.00 | NIST | |
| Ip | 1992.00 | NIST | |
| Tboil | 508.81 | K | Relay (1.0) Calculated Property |
| Tc | 736.93 | K | Relay (1.0) Calculated Property |
| Tfus | 291.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.573 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [14.64; 14.64] | kJ/mol | [292.80; 292.80] |
|
| ΔfusH | 14.64 | kJ/mol | 292.80 | NIST |
| ΔfusH | 14.64 | kJ/mol | 292.80 | NIST |
| ΔvapH | 67.90 ± 0.30 | kJ/mol | 310.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 529.20 | K | 102.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [221.60; 540.35] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -3.99100e+01 | |||
| Coefficient B | 1.17188e+00 | |||
| Coefficient C | -8.55920e-04 | |||
| Coefficient D | 2.64300e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 221.60 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 279.25 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 329.39 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 372.86 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 410.50 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 443.13 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 471.59 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 496.73 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 519.37 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 540.35 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0324364; 0.0000409] | Pa×s | [291.15; 564.81] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.72047e+01 | |||
| Coefficient B | 4.01094e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 291.15 | |||
| Temperature range, max. | 564.81 | |||
| η | 0.0324364 | Pa×s | 291.15 | Calculated Property |
| η | 0.0088164 | Pa×s | 321.56 | Calculated Property |
| η | 0.0030012 | Pa×s | 351.96 | Calculated Property |
| η | 0.0012127 | Pa×s | 382.37 | Calculated Property |
| η | 0.0005600 | Pa×s | 412.77 | Calculated Property |
| η | 0.0002875 | Pa×s | 443.18 | Calculated Property |
| η | 0.0001608 | Pa×s | 473.59 | Calculated Property |
| η | 0.0000965 | Pa×s | 503.99 | Calculated Property |
| η | 0.0000613 | Pa×s | 534.40 | Calculated Property |
| η | 0.0000409 | Pa×s | 564.81 | Calculated Property |
Similar Compounds
Find more compounds similar to Propofol.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
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