- InChI
- InChI=1S/C15H24O/c1-10-8-11(14(2,3)4)13(16)12(9-10)15(5,6)7/h8-9,16H,1-7H3
- InChI Key
- NLZUEZXRPGMBCV-UHFFFAOYSA-N
- Formula
- C15H24O
- SMILES
-
Cc1cc(C(C)(C)C)c(O)c(C(C)(C)C)
c1 - Molecular Weight1
- 220.35
- CAS
- 128-37-0
- Other Names
-
- 1-Hydroxy-4-methyl-2,6-di-tert-butylbenzene
- 2,6-BIS(1,1-DIMETHYLETHYL)-4METHYLPHENOL
- 2,6-Bis(1,1-dimethylethyl)-4-methylphenol
- 2,6-Bis(tert-butyl)-4-methylphenol
- 2,6-Di(tert-butyl)hydroxytoluene
- 2,6-Di-t-butyl-4-methylphenol
- 2,6-Di-t-butyl-p-cresol
- 2,6-Di-terc.butyl-p-kresol
- 2,6-Di-tert-butyl-1-hydroxy-4-methyl benzene
- 2,6-Di-tert-butyl-4-cresol
- 2,6-Di-tert-butyl-4-methylphenol
- 2,6-Di-tert-butyl-p-cresol
- 2,6-Di-tert-butyl-p-methylphenol
- 2,6-Di-tert-butyl-para-methylphenol
- 2,6-di-Butyl-para-cresol
- 2,6-di-ter-butul-4-methyl-phenol
- 2,6-di-ter-butyl-4-methyl-phenol
- 2,6-di-tert-Butyl-methylphenol
- 2,6-di-tert-butyl-p-cresol (BHT)
- 3,5-Di-tert-butyl-4-hydroxytoluene
- 4-Hydroxy-3,5-di-tert-butyltoluene
- 4-Methyl-2,6-di-t-butyl-phenol
- 4-Methyl-2,6-di-terc. butylfenol
- 4-Methyl-2,6-di-tert-butylphenol
- 4-Methyl-2,6-di-tert.-butylphenol
- 4-Methyl-2,6-tert-butylphenol
- AO 29
- AO 4K
- Advastab 401
- Agidol
- Annulex BHT
- Antioxidant 29
- Antioxidant 30
- Antioxidant 4K
- Antioxidant DBPC
- Antioxidant KB
- Antrancine 8
- BHT
- BHT (butylated hydroxytoluene)
- BHT Swanox
- BUKS
- Bht(food grade)
- Butylated hydroxyl toluene (BHT)
- Butylated hydroxytoluol
- Butylhydroxytoluene
- CAO 1
- CAO 3
- Catalin Antioxydant 1
- Catalin CAO-3
- Chemanox 11
- DBMP
- DBPC
- Dalpac
- Dbpc(technical grade)
- Deenax
- Di-ter-butyl p-cresol
- Di-tert-Butyl-4-methylphenol
- Di-tert-Butylparamethylphenol
- Di-tert-butyl-p-cresol
- Di-tert-butyl-p-methylphenol
- Di-tert-butylcresol
- Dibunol
- Dibutyl-p-cresol
- Dibutylated hydroxytoluene
- Dibutylcresol
- Dibutylhydroxytoluene
- Ergotamine, dihydro-, monomethanesulfonate (salt)
- Impruvol
- Ionol
- Ionol (Antioxidant)
- Ionol 1
- Ionol BHT
- Ionol CP
- Ionole
- Lowinox BHT
- NCI-C03598
- Nipanox BHT
- Nonox TBC
- P 21
- Parabar 441
- Paranox 441
- Phenol, 2,6-bis(1,1-dimethylethyl)-4-methyl-
- Phenol, 2,6-di-tert-butyl-4-methyl-
- Ralox BHT
- Stavox
- Sumilizer BHT
- Sustane
- Sustane BHT
- Tenamene 3
- Tenox BHT
- Topanol
- Topanol O
- Topanol OC
- Vanlube PC
- Vanlube PCX
- Vianol
- Vulkanox KB
- butylated OH tolueno
- o-Di-tert-butyl-p-methylphenol
- p-Cresol, 2,6-di-tert-butyl-
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid 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).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation 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).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (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°solid | -8916.00 | kJ/mol | NIST |
| ΔfG° | 19.63 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -296.90 | kJ/mol | NIST |
| ΔfH°solid | -410.00 | kJ/mol | NIST |
| ΔfusH° | 18.82 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [88.00; 117.30] | kJ/mol |
|
| ΔsubH° | 91.90 ± 3.20 | kJ/mol | NIST |
| ΔsubH° | 88.00 ± 0.80 | kJ/mol | NIST |
| ΔsubH° | 117.30 | kJ/mol | NIST |
| ΔsubH° | 113.10 | kJ/mol | NIST |
| ΔvapH° | 63.01 | kJ/mol | Joback Calculated Property |
| IE | 7.80 | eV | NIST |
| log10WS | -4.12 | Crippen Calculated Property | |
| logPoct/wat | 4.296 | Crippen Calculated Property | |
| McVol | 204.320 | ml/mol | McGowan Calculated Property |
| Pc | 2123.64 | kPa | Joback Calculated Property |
| Inp | [1471.00; 1555.00] |
|
|
| Inp | 1514.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Inp | 1500.00 | NIST | |
| Inp | 1501.00 | NIST | |
| Inp | 1499.00 | NIST | |
| Inp | 1497.00 | NIST | |
| Inp | 1494.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1533.30 | NIST | |
| Inp | 1517.50 | NIST | |
| Inp | 1514.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Inp | 1503.90 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1515.00 | NIST | |
| Inp | 1494.50 | NIST | |
| Inp | 1489.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | Outlier 1471.00 | NIST | |
| Inp | 1508.00 | NIST | |
| Inp | 1483.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | 1519.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1511.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Inp | 1519.00 | NIST | |
| Inp | 1492.00 | NIST | |
| Inp | 1509.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1508.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1516.00 | NIST | |
| Inp | 1508.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1516.00 | NIST | |
| Inp | Outlier 1545.00 | NIST | |
| Inp | 1524.00 | NIST | |
| Inp | 1496.00 | NIST | |
| Inp | 1501.00 | NIST | |
| Inp | 1538.00 | NIST | |
| Inp | 1525.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | Outlier 1474.00 | NIST | |
| Inp | 1499.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | Outlier 1555.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1514.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1515.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1493.00 | NIST | |
| Inp | 1497.00 | NIST | |
| Inp | 1526.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1494.00 | NIST | |
| Inp | 1534.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1514.00 | NIST | |
| I | [1867.00; 1927.00] |
|
|
| I | Outlier 1870.00 | NIST | |
| I | Outlier 1873.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1898.00 | NIST | |
| I | 1898.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1927.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1914.00 | NIST | |
| I | 1911.00 | NIST | |
| I | Outlier 1867.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1927.00 | NIST | |
| I | 1927.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1916.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1910.00 | NIST | |
| I | Outlier 1870.00 | NIST | |
| Tboil | 538.20 | K | NIST |
| Tc | 880.13 | K | Joback Calculated Property |
| Tfus | [342.86; 344.00] | K |
|
| Tfus | 344.00 ± 0.20 | K | NIST |
| Tfus | 342.86 ± 0.25 | K | NIST |
| Tfus | 343.00 ± 0.15 | K | NIST |
| Vc | 0.712 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [562.55; 654.63] | J/mol×K | [653.40; 880.13] |
|
| Cp,gas | 562.55 | J/mol×K | 653.40 | Joback Calculated Property |
| Cp,gas | 580.43 | J/mol×K | 691.19 | Joback Calculated Property |
| Cp,gas | 597.12 | J/mol×K | 728.98 | Joback Calculated Property |
| Cp,gas | 612.75 | J/mol×K | 766.77 | Joback Calculated Property |
| Cp,gas | 627.45 | J/mol×K | 804.56 | Joback Calculated Property |
| Cp,gas | 641.37 | J/mol×K | 842.35 | Joback Calculated Property |
| Cp,gas | 654.63 | J/mol×K | 880.13 | Joback Calculated Property |
| η | [0.0000139; 0.0006069] | Pa×s | [426.83; 653.40] |
|
| η | 0.0006069 | Pa×s | 426.83 | Joback Calculated Property |
| η | 0.0002505 | Pa×s | 464.59 | Joback Calculated Property |
| η | 0.0001181 | Pa×s | 502.35 | Joback Calculated Property |
| η | 0.0000618 | Pa×s | 540.12 | Joback Calculated Property |
| η | 0.0000352 | Pa×s | 577.88 | Joback Calculated Property |
| η | 0.0000215 | Pa×s | 615.64 | Joback Calculated Property |
| η | 0.0000139 | Pa×s | 653.40 | Joback Calculated Property |
| ΔfusH | [19.85; 23.85] | kJ/mol | [341.70; 343.70] |
|
| ΔfusH | 19.85 | kJ/mol | 341.70 | NIST |
| ΔfusH | 23.85 | kJ/mol | 343.70 | NIST |
| ΔsubH | [86.80; 87.80] | kJ/mol | [318.00; 323.00] |
|
| ΔsubH | 86.80 ± 0.80 | kJ/mol | 318.00 | NIST |
| ΔsubH | 87.80 | kJ/mol | 323.00 | NIST |
| ΔvapH | [61.50; 87.80] | kJ/mol | [323.00; 447.00] |
|
| ΔvapH | 87.80 | kJ/mol | 323.00 | NIST |
| ΔvapH | 61.50 | kJ/mol | 447.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [412.92; 567.92] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.57262e+01 | |||
| Coefficient B | -4.96090e+03 | |||
| Coefficient C | -9.15900e+01 | |||
| Temperature range, min. | 412.92 | |||
| Temperature range, max. | 567.92 | |||
| Pvap | 1.33 | kPa | 412.92 | Calculated Property |
| Pvap | 2.92 | kPa | 430.14 | Calculated Property |
| Pvap | 5.94 | kPa | 447.36 | Calculated Property |
| Pvap | 11.31 | kPa | 464.59 | Calculated Property |
| Pvap | 20.35 | kPa | 481.81 | Calculated Property |
| Pvap | 34.83 | kPa | 499.03 | Calculated Property |
| Pvap | 57.07 | kPa | 516.25 | Calculated Property |
| Pvap | 89.98 | kPa | 533.48 | Calculated Property |
| Pvap | 137.10 | kPa | 550.70 | Calculated Property |
| Pvap | 202.63 | kPa | 567.92 | Calculated Property |
| Pvap | [0.04; 2131.09] | kPa | [344.00; 720.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.61940e+02 | |||
| Coefficient B | -1.50684e+04 | |||
| Coefficient C | -2.09800e+01 | |||
| Coefficient D | 9.03774e-06 | |||
| Temperature range, min. | 344.00 | |||
| Temperature range, max. | 720.00 | |||
| Pvap | 0.04 | kPa | 344.00 | Calculated Property |
| Pvap | 0.49 | kPa | 385.78 | Calculated Property |
| Pvap | 3.49 | kPa | 427.56 | Calculated Property |
| Pvap | 15.97 | kPa | 469.33 | Calculated Property |
| Pvap | 53.30 | kPa | 511.11 | Calculated Property |
| Pvap | 142.17 | kPa | 552.89 | Calculated Property |
| Pvap | 322.71 | kPa | 594.67 | Calculated Property |
| Pvap | 652.27 | kPa | 636.44 | Calculated Property |
| Pvap | 1213.66 | kPa | 678.22 | Calculated Property |
| Pvap | 2131.09 | kPa | 720.00 | Calculated Property |
Similar Compounds
![Phenol, 4,4'-[thiobis(methylene)]bis[2,6-bis(1,1-dimethylethyl)-.](data:image/png;base64,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)
Find more compounds similar to Butylated Hydroxytoluene.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.