- InChI
- InChI=1S/C18H36O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19/h9-10,19H,2-8,11-18H2,1H3/b10-9-
- InChI Key
- ALSTYHKOOCGGFT-KTKRTIGZSA-N
- Formula
- C18H36O
- SMILES
- CCCCCCCCC=CCCCCCCCCO
- Molecular Weight1
- 268.48
- CAS
- 143-28-2
- Other Names
-
- ( Z)-9-octadecenol
- (9Z)-9-Octadecen-1-ol
- (Z)-9-octadecen-1-ol
- (Z)-octadec-9-enol
- 9-Octadecen-1-ol
- 9-Octadecen-1-ol, (9Z)-
- 9-Octadecen-1-ol, cis-
- Adol 320
- Adol 330
- Adol 34
- Adol 340
- Adol 80
- Adol 85
- Adol 90
- Anjecol 90N
- Anjecol 90NR
- Atalco O
- Cachalot O-1
- Cachalot O-15
- Cachalot O-3
- Cachalot O-8
- Conditioner 1
- Crodacol A.10
- Crodacol-O
- Dermaffine
- Emery 3312
- Emery 3317
- Fancol OA-95
- H.D. eutanol
- HD oleyl alcohol 70/75
- HD oleyl alcohol 80/85
- HD oleyl alcohol 90/95
- HD oleyl alcohol CG
- HD-Echelon 90/95
- HD-Eutanol
- HD-Ocenol 90/95
- HD-Ocenol K
- Lancol
- Lipocol O
- Loxanol 95
- Loxanol M
- Novol
- Ocenol
- Oceol
- Octadec-9-en-1-ol
- Octadec-9-en-1-ol, (Z)-
- Octadec-9Z-enol
- Octadeca-9-cis-en-1-ol
- Oleic alcohol
- Oleo alcohol
- Oleol
- Olive alcohol
- Satol
- Sipol O
- Siponol OC
- Unjecol 110
- Unjecol 50
- Unjecol 70
- Unjecol 90
- Unjecol 90N
- Unjecol 90NR
- cis-9-Octadecenyl Alcohol
- cis-9-octadecen-1-ol
- cis-«DELTA»9-Octadecenol
- oleyl 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).
- 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).
- n0 : Refractive Index.
- 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 |
|---|---|---|---|
| ω | 0.9797 | Relay (1.0) Calculated Property | |
| ΔfG° | 44.08 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -507.38 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 46.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 119.30 | kJ/mol | NIST |
| IE | 9.15 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.50 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.016 | Crippen Calculated Property | |
| McVol | 266.050 | ml/mol | McGowan Calculated Property |
| Pc | 1273.69 | kPa | Joback Calculated Property |
| Inp | [2060.00; 2068.80] |
|
|
| Inp | 2068.80 | NIST | |
| Inp | 2060.00 | NIST | |
| Inp | 2060.00 | NIST | |
| Inp | 2066.00 | NIST | |
| Ip | [2116.00; 2116.00] |
|
|
| Ip | 2116.00 | NIST | |
| Ip | 2116.00 | NIST | |
| Tboil | 605.26 | K | Relay (1.0) Calculated Property |
| Tc | 783.44 | K | Relay (1.0) Calculated Property |
| Tfus | [272.15; 309.00] | K |
|
| Tfus | 272.15 | K | The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect |
| Tfus | 279.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 309.00 ± 2.00 | K | NIST |
| Tfus | 273.15 ± 3.00 | K | NIST |
| Vc | 1.012 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | 2.00 | kPa | 480.05 | Phase equilibria of liquid (water + butyric acid + oleyl alcohol) ternary system |
| n0 | [1.46010; 1.46030] | [293.15; 293.15] |
|
|
| n0 | 1.46030 | 293.15 | Liquid phase equilibria of (water + propionic acid + oleyl alcohol) ternary system at several temperatures | |
| n0 | 1.46010 | 293.15 | Distribution of Butyric Acid between Water and Several Solvents |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [480.00; 480.70] | K | [1.70; 2.00] |
|
| Tboilr | 480.20 | K | 1.70 | NIST |
| Tboilr | 480.00 | K | 1.70 | NIST |
| Tboilr | 480.70 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [385.83; 936.06] | 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 | -2.23650e+01 | |||
| Coefficient B | 1.76782e+00 | |||
| Coefficient C | -1.06960e-03 | |||
| Coefficient D | 2.60200e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 385.83 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 480.70 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 565.22 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 640.21 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 706.49 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 764.88 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 816.21 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 861.30 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 900.98 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 936.06 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0612576; 0.0000551] | Pa×s | [283.36; 611.98] |
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 | -1.58542e+01 | |||
| Coefficient B | 3.70115e+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. | 283.36 | |||
| Temperature range, max. | 611.98 | |||
| η | 0.0612576 | Pa×s | 283.36 | Calculated Property |
| η | 0.0137929 | Pa×s | 319.88 | Calculated Property |
| η | 0.0042153 | Pa×s | 356.39 | Calculated Property |
| η | 0.0016058 | Pa×s | 392.90 | Calculated Property |
| η | 0.0007208 | Pa×s | 429.41 | Calculated Property |
| η | 0.0003668 | Pa×s | 465.93 | Calculated Property |
| η | 0.0002060 | Pa×s | 502.44 | Calculated Property |
| η | 0.0001250 | Pa×s | 538.95 | Calculated Property |
| η | 0.0000809 | Pa×s | 575.47 | Calculated Property |
| η | 0.0000551 | Pa×s | 611.98 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [493.72; 687.67] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50364e+01 | |||
| Coefficient B | -5.53733e+03 | |||
| Coefficient C | -1.18278e+02 | |||
| Temperature range, min. | 493.72 | |||
| Temperature range, max. | 687.67 | |||
| Pvap | 1.33 | kPa | 493.72 | Calculated Property |
| Pvap | 2.97 | kPa | 515.27 | Calculated Property |
| Pvap | 6.09 | kPa | 536.82 | Calculated Property |
| Pvap | 11.64 | kPa | 558.37 | Calculated Property |
| Pvap | 20.94 | kPa | 579.92 | Calculated Property |
| Pvap | 35.75 | kPa | 601.47 | Calculated Property |
| Pvap | 58.31 | kPa | 623.02 | Calculated Property |
| Pvap | 91.38 | kPa | 644.57 | Calculated Property |
| Pvap | 138.22 | kPa | 666.12 | Calculated Property |
| Pvap | 202.64 | kPa | 687.67 | Calculated Property |
Similar Compounds
Find more compounds similar to 9-Octadecen-1-ol, (Z)-.
Mixtures
- 9-Octadecen-1-ol, (Z)- + 2,3-Butanediol + Water
- Butanoic acid + 9-Octadecen-1-ol, (Z)- + Water
- 9-Octadecen-1-ol, (Z)- + Propanoic acid + Water
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
- Liquid phase equilibria of (water + propionic acid + oleyl alcohol) ternary system at several temperatures
- Phase equilibria of liquid (water + butyric acid + oleyl alcohol) ternary system
- (Liquid + liquid) phase equilibria for (water + 2,3-butanediol + oleyl alcohol) at T = (300.2, 307.2, and 314.2) K
- The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
- Distribution of Butyric Acid between Water and Several Solvents
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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