- InChI
- InChI=1S/C16H34O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17/h17H,2-16H2,1H3
- InChI Key
- BXWNKGSJHAJOGX-UHFFFAOYSA-N
- Formula
- C16H34O
- SMILES
- CCCCCCCCCCCCCCCCO
- Molecular Weight1
- 242.44
- CAS
- 124-29-8
- Other Names
-
- 1-Cetanol
- 1-Hexadecyl alcohol
- 1-Hexanedecanol
- 1-Hydroxyhexadecane
- 19141-82-3
- Adol 52
- Adol 52 NF
- Adol 520
- Adol 54
- Alcohol c-16
- Aldol 54
- Alfol 16
- Alfol 16RD
- Atalco C
- CO-1670
- CO-1695
- Cachalot C-50
- Cachalot C-50 NF
- Cachalot C-51
- Cachalot C-52
- Cetaffine
- Cetal
- Cetalol CA
- Cetyl alcohol NF
- Cetylic alcohol
- Cetylol
- Crodacol C
- Crodacol C70
- Crodacol C95 NF
- Crodacol-CAS
- Crodacol-CAT
- Dytol F-11
- Elfacos C
- Epal 16
- Epal 16NF
- Ethal
- Ethol
- Fancol CA
- Hexadecan-1-ol
- Hyfatol 16
- Hyfatol 16-95
- Kalcol 6098
- Lanette 16
- Lanol C
- Laurex 16
- Lipocol C
- Lorol 24
- Lorol C16
- LorolL 24
- Loxanol K
- Loxanol K extra
- Loxanwachs SK
- Palmitic alcohol
- Palmityl alcohol
- Philcohol 1600
- Product 308
- Rita CA
- Siponol CC
- Siponol wax-A
- cetanol
- cetyl alcohol
- hexadecanol
- hexadecyl alcohol
- n-1-Hexadecanol
- n-Hexadecan-1-ol
- n-Hexadecanol
- n-Hexadecyl alcohol
- n-cetyl alcohol
- ω : Acentric Factor.
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (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.
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 73.35 | kJ/mol | 617.20 | KDB |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 465.70 | K | 2.02 | Vapor-liquid equilibria of monoacylglicerol + monoacylglicerol or alcohol or fatty acid at subatmospheric pressures |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [357.40; 863.46] | 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 | -6.36500e+00 | |||
| Coefficient B | 1.55782e+00 | |||
| Coefficient C | -8.77000e-04 | |||
| Coefficient D | 1.89000e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 357.40 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 443.36 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 520.49 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 589.39 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 650.66 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 704.90 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 752.70 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 794.66 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 831.38 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 863.45 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0110364; 0.0001349] | Pa×s | [322.51; 539.00] |
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 | -1.54722e+01 | |||
| Coefficient B | 3.53659e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 322.51 | |||
| Temperature range, max. | 539.00 | |||
| η | 0.0110364 | Pa×s | 322.51 | Calculated Property |
| η | 0.0051558 | Pa×s | 346.57 | Calculated Property |
| η | 0.0026587 | Pa×s | 370.62 | Calculated Property |
| η | 0.0014863 | Pa×s | 394.68 | Calculated Property |
| η | 0.0008883 | Pa×s | 418.73 | Calculated Property |
| η | 0.0005614 | Pa×s | 442.78 | Calculated Property |
| η | 0.0003720 | Pa×s | 466.84 | Calculated Property |
| η | 0.0002566 | Pa×s | 490.89 | Calculated Property |
| η | 0.0001833 | Pa×s | 514.95 | Calculated Property |
| η | 0.0001349 | Pa×s | 539.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [464.78; 649.14] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50566e+01 | |||
| Coefficient B | -5.28146e+03 | |||
| Coefficient C | -1.07180e+02 | |||
| Temperature range, min. | 464.78 | |||
| Temperature range, max. | 649.14 | |||
| Pvap | 1.33 | kPa | 464.78 | Calculated Property |
| Pvap | 2.97 | kPa | 485.26 | Calculated Property |
| Pvap | 6.08 | kPa | 505.75 | Calculated Property |
| Pvap | 11.63 | kPa | 526.23 | Calculated Property |
| Pvap | 20.92 | kPa | 546.72 | Calculated Property |
| Pvap | 35.72 | kPa | 567.20 | Calculated Property |
| Pvap | 58.28 | kPa | 587.69 | Calculated Property |
| Pvap | 91.34 | kPa | 608.17 | Calculated Property |
| Pvap | 138.20 | kPa | 628.66 | Calculated Property |
| Pvap | 202.66 | kPa | 649.14 | Calculated Property |
| Pvap | [5.25e-05; 1689.08] | kPa | [322.35; 761.00] |
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 | 3.18319e+02 | |||
| Coefficient B | -2.59164e+04 | |||
| Coefficient C | -4.32052e+01 | |||
| Coefficient D | 1.69556e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 322.35 | |||
| Temperature range, max. | 761.00 | |||
| Pvap | 5.25e-05 | kPa | 322.35 | Calculated Property |
| Pvap | 8.18e-03 | kPa | 371.09 | Calculated Property |
| Pvap | 0.25 | kPa | 419.83 | Calculated Property |
| Pvap | 2.81 | kPa | 468.57 | Calculated Property |
| Pvap | 16.19 | kPa | 517.31 | Calculated Property |
| Pvap | 60.52 | kPa | 566.04 | Calculated Property |
| Pvap | 170.70 | kPa | 614.78 | Calculated Property |
| Pvap | 402.05 | kPa | 663.52 | Calculated Property |
| Pvap | 848.75 | kPa | 712.26 | Calculated Property |
| Pvap | 1689.08 | kPa | 761.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Hexadecanol.
Mixtures
- Quinoline + 1-Hexadecanol
- Propane + 1-Hexadecanol
- 1-Hexadecanol + 2,3-Pentadione
- 1-Hexadecanol + 1-Decanol
- 1-Hexadecanol + 1-Octadecanol
- 1-Hexadecanol + Methyl tetradecanoate
- 1-Dodecanol + 1-Hexadecanol
- 1-Hexadecanol + 1-Tetradecanol
- Carbon dioxide + 1-Hexadecanol
- Octadecanoic acid + 1-Hexadecanol
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
- Phase equilibria of high molecular mass 1-alcohols in supercritical propane
- The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
- Vapor-liquid equilibria of monoacylglicerol + monoacylglicerol or alcohol or fatty acid at subatmospheric pressures
- Thermodynamics of organic mixtures containing amines. VIII. Systems with quinoline
- The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
- High Pressure Solid-Liquid Equilibrium of Fatty Alcohols Binary Systems from 1-Dodecanol, 1-Tetradecanol, 1-Hexadecanol, and 1-Octadecanol
- High Pressure Phase Behavior of the Homologous Series CO2 + 1-Alcohols
- Vapor-Liquid Equilibria of Binary Systems with Long-Chain Organic Compounds (Fatty Alcohol, Fatty Ester, Acylglycerol, and n-Paraffin) at Subatmospheric Pressures
- Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography
- Liquid-Liquid Phase Behavior of Solutions of 1-Dodecyl-3-methylimidazolium Bis(trifluoromethylsulphonyl)imide (C12mimNTf2) in n- Alkyl Alcohols
- Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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