- InChI
- InChI=1S/C3H6O/c1-2-3-4/h2,4H,1,3H2
- InChI Key
- XXROGKLTLUQVRX-UHFFFAOYSA-N
- Formula
- C3H6O
- SMILES
- C=CCO
- Molecular Weight1
- 58.08
- CAS
- 107-18-6
- Other Names
-
- 1-Hydroxy-2-propene
- 1-Propen-3-ol
- 1-Propenol-3
- 1-Propenol-3-ol
- 2-Propene-1-ol
- 2-Propenol
- 2-Propenyl alcohol
- 2-propen-1-ol (allyl alcohol)
- 3-HYDROXYPROPENE
- 3-Hydroxy-1-propene
- AA
- Alcool allilco
- Alcool allylique
- Allilowy alkohol
- Allyl al
- Allyl alcohol
- Allylalkohol
- Allylic alcohol
- CH2=CHCH2OH
- NSC 6526
- PROPENYLALCOHOL
- Propen-1-ol-3
- Propenol-3
- Propenyl alcohol
- Rcra waste number P005
- Shell Unkrauttod A
- Shell unkrautted A
- UN 1098
- VINYLCARBINOL
- Weed drench
- prop-2-en-1-ol
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- 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,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (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
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5540 | KDB | |
| Tig | 715.93 | K | KDB |
| LFL | 2.50 | % in Air | KDB |
| UFL | 18.00 | % in Air | KDB |
| Tflash,cc | 305.37 | K | KDB |
| Tflash,oc | 295.37 | K | KDB |
| ΔfG° | -71.30 | kJ/mol | KDB |
| ΔfH°gas | [-132.10; -123.60] | kJ/mol |
|
| ΔfH°gas | -132.10 | kJ/mol | KDB |
| ΔfH°gas | -123.60 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 6.33 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [44.80; 47.30] | kJ/mol |
|
| ΔvapH° | 44.80 | kJ/mol | NIST |
| ΔvapH° | 46.10 | kJ/mol | NIST |
| ΔvapH° | 47.30 | kJ/mol | NIST |
| ΔvapH° | 47.00 ± 1.00 | kJ/mol | NIST |
| IE | [9.63; 10.22] | eV |
|
| IE | 9.67 ± 0.03 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.63 | eV | NIST |
| IE | 9.67 ± 0.05 | eV | NIST |
| IE | 10.22 | eV | NIST |
| log10WS | -0.20 | Crippen Calculated Property | |
| logPoct/wat | 0.165 | Crippen Calculated Property | |
| McVol | 54.700 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 3 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | [5310.00; 5640.00] | kPa |
|
| Pc | 5310.00 | kPa | KDB |
| Pc | 5640.00 | kPa | Critica... |
| Inp | [498.00; 576.00] |
|
|
| Inp | 576.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 546.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 546.00 | NIST | |
| Inp | 539.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 526.00 | NIST | |
| Inp | 549.00 | NIST | |
| Inp | 532.00 | NIST | |
| Inp | 546.00 | NIST | |
| Inp | Outlier 498.00 | NIST | |
| Inp | Outlier 501.00 | NIST | |
| Inp | 519.00 | NIST | |
| Inp | 550.00 | NIST | |
| Inp | 543.00 | NIST | |
| Inp | 545.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 555.00 | NIST | |
| Inp | 555.00 | NIST | |
| Inp | 555.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 534.00 | NIST | |
| Inp | 555.00 | NIST | |
| Inp | 546.00 | NIST | |
| Inp | Outlier 498.00 | NIST | |
| I | [1097.00; 1167.00] |
|
|
| I | 1130.00 | NIST | |
| I | Outlier 1167.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1130.00 | NIST | |
| I | Outlier 1167.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1145.00 | NIST | |
| I | 1098.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1097.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1104.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1138.00 | NIST | |
| Tboil | [369.60; 370.30] | K |
|
| Tboil | 370.23 | K | KDB |
| Tboil | 369.95 | K | Separat... |
| Tboil | 369.75 | K | Vapor-L... |
| Tboil | 369.90 | K | Measure... |
| Tboil | 369.94 | K | Isobari... |
| Tboil | 370.30 | K | NIST |
| Tboil | 370.00 | K | NIST |
| Tboil | 370.25 ± 0.30 | K | NIST |
| Tboil | 369.62 ± 0.50 | K | NIST |
| Tboil | 370.23 ± 0.30 | K | NIST |
| Tboil | 370.07 ± 0.20 | K | NIST |
| Tboil | 370.00 ± 0.50 | K | NIST |
| Tboil | 370.00 ± 0.40 | K | NIST |
| Tboil | 370.10 ± 0.30 | K | NIST |
| Tboil | 370.10 ± 0.50 | K | NIST |
| Tboil | 369.60 ± 2.00 | K | NIST |
| Tc | [545.00; 545.10] | K |
|
| Tc | 545.00 | K | KDB |
| Tc | 545.10 | K | NIST |
| Tc | 545.10 | K | NIST |
| Tfus | 144.00 | K | KDB |
| Vc | 0.203 | m3/kmol | KDB |
| Zc | 0.2384660 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [88.33; 115.41] | J/mol×K | [356.90; 522.27] |
|
| Cp,gas | 88.33 | J/mol×K | 356.90 | Joback Calculated Property |
| Cp,gas | 93.33 | J/mol×K | 384.46 | Joback Calculated Property |
| Cp,gas | 98.12 | J/mol×K | 412.02 | Joback Calculated Property |
| Cp,gas | 102.72 | J/mol×K | 439.59 | Joback Calculated Property |
| Cp,gas | 107.13 | J/mol×K | 467.15 | Joback Calculated Property |
| Cp,gas | 111.36 | J/mol×K | 494.71 | Joback Calculated Property |
| Cp,gas | 115.41 | J/mol×K | 522.27 | Joback Calculated Property |
| Cp,liquid | [134.61; 160.30] | J/mol×K | [273.41; 324.46] |
|
| Cp,liquid | 134.94 | J/mol×K | 273.41 | Heat Ca... |
| Cp,liquid | 134.61 | J/mol×K | 273.41 | Heat Ca... |
| Cp,liquid | 137.19 | J/mol×K | 278.52 | Heat Ca... |
| Cp,liquid | 137.35 | J/mol×K | 278.52 | Heat Ca... |
| Cp,liquid | 139.43 | J/mol×K | 283.62 | Heat Ca... |
| Cp,liquid | 139.18 | J/mol×K | 283.62 | Heat Ca... |
| Cp,liquid | 141.93 | J/mol×K | 288.72 | Heat Ca... |
| Cp,liquid | 141.68 | J/mol×K | 288.72 | Heat Ca... |
| Cp,liquid | 144.34 | J/mol×K | 293.83 | Heat Ca... |
| Cp,liquid | 144.17 | J/mol×K | 293.83 | Heat Ca... |
| Cp,liquid | 138.90 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 146.67 | J/mol×K | 298.93 | Heat Ca... |
| Cp,liquid | 146.50 | J/mol×K | 298.93 | Heat Ca... |
| Cp,liquid | 149.16 | J/mol×K | 304.04 | Heat Ca... |
| Cp,liquid | 149.08 | J/mol×K | 304.04 | Heat Ca... |
| Cp,liquid | 152.32 | J/mol×K | 309.14 | Heat Ca... |
| Cp,liquid | 151.82 | J/mol×K | 309.14 | Heat Ca... |
| Cp,liquid | 154.40 | J/mol×K | 314.25 | Heat Ca... |
| Cp,liquid | 154.82 | J/mol×K | 314.25 | Heat Ca... |
| Cp,liquid | 157.23 | J/mol×K | 319.35 | Heat Ca... |
| Cp,liquid | 157.06 | J/mol×K | 319.35 | Heat Ca... |
| Cp,liquid | 160.14 | J/mol×K | 324.46 | Heat Ca... |
| Cp,liquid | 160.30 | J/mol×K | 324.46 | Heat Ca... |
| η | [0.0003781; 0.1538622] | Pa×s | [182.63; 356.90] |
|
| η | 0.1538622 | Pa×s | 182.63 | Joback Calculated Property |
| η | 0.0284333 | Pa×s | 211.67 | Joback Calculated Property |
| η | 0.0078973 | Pa×s | 240.72 | Joback Calculated Property |
| η | 0.0028903 | Pa×s | 269.76 | Joback Calculated Property |
| η | 0.0012861 | Pa×s | 298.81 | Joback Calculated Property |
| η | 0.0006605 | Pa×s | 327.86 | Joback Calculated Property |
| η | 0.0003781 | Pa×s | 356.90 | Joback Calculated Property |
| ΔvapH | [39.96; 46.70] | kJ/mol | [311.50; 369.70] |
|
| ΔvapH | 46.70 | kJ/mol | 311.50 | NIST |
| ΔvapH | 44.60 | kJ/mol | 325.00 | NIST |
| ΔvapH | 39.96 | kJ/mol | 369.70 | KDB |
| Pvap | [6.95; 520.67] | kPa | [311.42; 423.15] |
|
| Pvap | 6.95 | kPa | 311.42 | Vapor-L... |
| Pvap | 7.67 | kPa | 313.15 | Vapor-L... |
| Pvap | 8.87 | kPa | 315.81 | Vapor-L... |
| Pvap | 11.08 | kPa | 319.97 | Vapor-L... |
| Pvap | 15.67 | kPa | 326.70 | Vapor-L... |
| Pvap | 20.19 | kPa | 331.84 | Vapor-L... |
| Pvap | 21.51 | kPa | 333.15 | Vapor-L... |
| Pvap | 22.60 | kPa | 334.20 | Vapor-L... |
| Pvap | 26.94 | kPa | 337.96 | Vapor-L... |
| Pvap | 31.72 | kPa | 341.54 | Vapor-L... |
| Pvap | 35.82 | kPa | 344.27 | Vapor-L... |
| Pvap | 40.30 | kPa | 346.97 | Vapor-L... |
| Pvap | 48.61 | kPa | 351.37 | Vapor-L... |
| Pvap | 52.34 | kPa | 353.15 | Vapor-L... |
| Pvap | 52.33 | kPa | 353.15 | Vapor-L... |
| Pvap | 53.30 | kPa | 353.59 | Vapor-L... |
| Pvap | 58.11 | kPa | 355.70 | Vapor-L... |
| Pvap | 101.30 | kPa | 369.75 | Vapor-L... |
| Pvap | 101.30 | kPa | 369.94 | Isobari... |
| Pvap | 113.10 | kPa | 373.15 | Vapor L... |
| Pvap | 109.94 | kPa | 373.15 | Vapor L... |
| Pvap | 109.95 | kPa | 373.15 | Vapor L... |
| Pvap | 520.67 | kPa | 423.15 | Vapor L... |
| Pvap | 518.64 | kPa | 423.15 | Vapor L... |
| Pvap | 518.11 | kPa | 423.15 | Vapor L... |
| n0 | 1.41280 | 293.15 | Solubil... | |
| ρl | [832.63; 855.00] | kg/m3 | [288.00; 318.15] |
|
| ρl | 855.00 | kg/m3 | 288.00 | KDB |
| ρl | 855.00 | kg/m3 | 293.15 | Salts e... |
| ρl | 854.00 | kg/m3 | 293.15 | Isobari... |
| ρl | 850.40 | kg/m3 | 298.15 | Volumet... |
| ρl | 846.02 | kg/m3 | 303.15 | Volumet... |
| ρl | 841.59 | kg/m3 | 308.15 | Volumet... |
| ρl | 837.13 | kg/m3 | 313.15 | Volumet... |
| ρl | 832.63 | kg/m3 | 318.15 | Volumet... |
| γ | 0.03 | N/m | 293.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 5709.21] | kPa | [282.38; 545.10] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.59415e+01 | |||
| Coefficient B | -3.58605e+03 | |||
| Coefficient C | -5.33010e+01 | |||
| Temperature range, min. | 282.38 | |||
| Temperature range, max. | 545.10 | |||
| Pvap | 1.33 | kPa | 282.38 | Calculated Property |
| Pvap | 7.82 | kPa | 311.57 | Calculated Property |
| Pvap | 32.03 | kPa | 340.76 | Calculated Property |
| Pvap | 101.15 | kPa | 369.95 | Calculated Property |
| Pvap | 263.10 | kPa | 399.14 | Calculated Property |
| Pvap | 589.70 | kPa | 428.34 | Calculated Property |
| Pvap | 1176.30 | kPa | 457.53 | Calculated Property |
| Pvap | 2138.00 | kPa | 486.72 | Calculated Property |
| Pvap | 3603.71 | kPa | 515.91 | Calculated Property |
| Pvap | 5709.21 | kPa | 545.10 | Calculated Property |
| Pvap | [2.91e-09; 5618.34] | kPa | [144.15; 545.05] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.40943e+01 | |||
| Coefficient B | -6.87755e+03 | |||
| Coefficient C | -5.24079e+00 | |||
| Coefficient D | 6.03381e-07 | |||
| Temperature range, min. | 144.15 | |||
| Temperature range, max. | 545.05 | |||
| Pvap | 2.91e-09 | kPa | 144.15 | Calculated Property |
| Pvap | 5.57e-05 | kPa | 188.69 | Calculated Property |
| Pvap | 0.02 | kPa | 233.24 | Calculated Property |
| Pvap | 0.90 | kPa | 277.78 | Calculated Property |
| Pvap | 12.82 | kPa | 322.33 | Calculated Property |
| Pvap | 88.42 | kPa | 366.87 | Calculated Property |
| Pvap | 376.98 | kPa | 411.42 | Calculated Property |
| Pvap | 1152.71 | kPa | 455.96 | Calculated Property |
| Pvap | 2778.06 | kPa | 500.51 | Calculated Property |
| Pvap | 5618.34 | kPa | 545.05 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Propen-1-ol.
Mixtures
- 2-Propen-1-ol + Water
- Hydrogen + 2-Propen-1-ol
- 2-Propen-1-ol + 2-Pyrrolidinone, 1-methyl-
- 2-Propen-1-ol + Formamide, N-methyl-
- 1,2-Ethanediol + 2-Propen-1-ol
- 2-Propanol, 1,3-dichloro- + 2-Propen-1-ol
- 2-Propen-1-ol + Methyl Alcohol
- 2-Propen-1-ol + Ethanol
- Benzene + 2-Propen-1-ol
- Isobutyl acetate + 2-Propen-1-ol
- 2-Propen-1-ol + Acetic acid, butyl ester
- Propanoic acid, butyl ester + 2-Propen-1-ol
- Trichloromethane + 2-Propen-1-ol
- 2-Propen-1-ol + Ethyl Acetate
- 2-Propen-1-ol + Methyl propionate
- 1-Propanol + 2-Propen-1-ol
- Monoethanolamine + 2-Propen-1-ol
- Furfural + 2-Propen-1-ol
- Propane + 2-Propen-1-ol
- Propene + 2-Propen-1-ol
Find more mixtures with 2-Propen-1-ol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Salts effect on isobaric vapor-liquid equilibrium for separation of the azeotropic mixture allyl alcohol + water
- Solubility of hydrogen in bio-oil compounds
- Separation of azeotrope (allyl alcohol + water): Isobaric vapour-liquid phase equilibrium measurements and extractive distillation
- Heat Capacities of 2-Propenol and Selected Cyclohexylalcohols
- Volumetric properties for binary and ternary mixtures of allyl alcohol, 1,3-dichloro-2-propanol and 1-ethyl-3-methyl imidazolium ethyl sulfate [Emim][EtSO4] from T = 298.15 to 318.15 K at ambient pressure
- Isobaric Vapor Liquid Equilibrium for Binary Systems of Allyl Alcohol with Water, Methanol, and Ethanol at 101.3 kPa
- Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol + Water and Allyl Alcohol + Benzene at 101.3 kPa
- Measurement and Correlation of Isobaric Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol with Isobutyl Acetate, Butyl Acetate, and Butyl Propionate at 101.3 kPa
- Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
- Vapor-Liquid Equilibrium for Benzene + 2-Methylpentane and Allyl Alcohol + 1-Propanol
- Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Propen-1-ol
- Critical Point and Vapor Pressure Measurements for Seven Compounds by a Low Residence Time Flow Method
- Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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that the value is more than 2 standard deviations away from the
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