- InChI
- InChI=1S/C5H10O/c1-3-5(6)4-2/h3,5-6H,1,4H2,2H3
- InChI Key
- VHVMXWZXFBOANQ-UHFFFAOYSA-N
- Formula
- C5H10O
- SMILES
- C=CC(O)CC
- Molecular Weight1
- 86.13
- CAS
- 616-25-1
- Other Names
-
- 1-Pentene-3-ol
- Ethyl vinyl carbinol
- Pent-1-en-3-ol
- ethylvinylcarbinol
- penten-3-ol
- «alpha»-Ethylallyl alcohol
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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.
- 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 |
|---|---|---|---|
| ω | 0.5048 | Relay (1.0) Calculated Property | |
| ΔfusH° | 7.99 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 51.30 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [9.40; 9.60] | eV |
|
| IE | 9.60 | eV | NIST |
| IE | 9.40 ± 0.05 | eV | NIST |
| log10WS | -0.03 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.943 | Crippen Calculated Property | |
| McVol | 82.880 | ml/mol | McGowan Calculated Property |
| Pc | 4130.29 | kPa | Joback Calculated Property |
| Inp | [649.00; 725.00] |
|
|
| Inp | 650.00 | NIST | |
| Inp | 654.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 670.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 656.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | Outlier 725.00 | NIST | |
| Inp | Outlier 722.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | Outlier 719.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 688.80 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | Outlier 716.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 659.00 | NIST | |
| Inp | Outlier 710.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 656.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | Outlier 721.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 659.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 649.00 | NIST | |
| I | [1112.00; 1207.00] |
|
|
| I | 1157.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1160.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1158.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1148.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1153.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1168.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1151.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1151.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1141.00 | NIST | |
| I | Outlier 1207.00 | NIST | |
| I | 1160.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1155.00 | NIST | |
| I | 1160.00 | NIST | |
| I | 1160.00 | NIST | |
| I | Outlier 1192.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1159.00 | NIST | |
| I | Outlier 1112.00 | NIST | |
| I | 1149.00 | NIST | |
| I | 1148.00 | NIST | |
| I | 1149.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1146.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1169.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1145.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1154.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1167.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1155.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1158.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1146.00 | NIST | |
| I | 1152.00 | NIST | |
| I | Outlier 1204.00 | NIST | |
| I | Outlier 1112.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1152.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1158.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1158.00 | NIST | |
| I | 1152.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1160.00 | NIST | |
| I | 1153.00 | NIST | |
| I | 1148.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1145.00 | NIST | |
| I | 1147.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1169.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1149.00 | NIST | |
| I | 1155.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1169.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1163.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1155.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1147.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1158.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1155.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1145.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1160.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1158.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1149.00 | NIST | |
| I | 1162.00 | NIST | |
| I | 1167.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1164.00 | NIST | |
| I | Outlier 1204.00 | NIST | |
| I | 1148.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1140.00 | NIST | |
| Tboil | 388.20 | K | NIST |
| Tc | 541.20 | K | Relay (1.0) Calculated Property |
| Tfus | 187.67 | K | Relay (1.0) Calculated Property |
| Vc | 0.304 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Enthalpy of formation at standard conditions, Standard Gibbs free energy of formation 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 |
|---|---|---|---|---|
| ΔvapH | [46.80; 49.90] | kJ/mol | [313.00; 343.00] |
|
| ΔvapH | 49.90 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 48.40 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 46.80 ± 0.10 | kJ/mol | 343.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [113.93; 267.98] | 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 | -1.03900e+00 | |||
| Coefficient B | 4.98720e-01 | |||
| Coefficient C | -3.04700e-04 | |||
| Coefficient D | 7.50000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 113.93 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 140.58 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 164.30 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 185.31 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 203.87 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 220.19 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 234.53 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 247.12 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 258.19 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 267.98 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.2702616; 0.0002954] | Pa×s | [190.17; 399.73] |
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 | -1.43151e+01 | |||
| Coefficient B | 2.47349e+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. | 190.17 | |||
| Temperature range, max. | 399.73 | |||
| η | 0.2702616 | Pa×s | 190.17 | Calculated Property |
| η | 0.0654038 | Pa×s | 213.45 | Calculated Property |
| η | 0.0209233 | Pa×s | 236.74 | Calculated Property |
| η | 0.0082092 | Pa×s | 260.02 | Calculated Property |
| η | 0.0037563 | Pa×s | 283.31 | Calculated Property |
| η | 0.0019355 | Pa×s | 306.59 | Calculated Property |
| η | 0.0010952 | Pa×s | 329.87 | Calculated Property |
| η | 0.0006680 | Pa×s | 353.16 | Calculated Property |
| η | 0.0004332 | Pa×s | 376.44 | Calculated Property |
| η | 0.0002954 | Pa×s | 399.73 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.88; 202.66] | kPa | [287.34; 410.54] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.58395e+01 | |||
| Coefficient B | -3.80716e+03 | |||
| Coefficient C | -4.89170e+01 | |||
| Temperature range, min. | 287.34 | |||
| Temperature range, max. | 410.54 | |||
| Pvap | 0.88 | kPa | 287.34 | Calculated Property |
| Pvap | 2.09 | kPa | 301.03 | Calculated Property |
| Pvap | 4.55 | kPa | 314.72 | Calculated Property |
| Pvap | 9.19 | kPa | 328.41 | Calculated Property |
| Pvap | 17.35 | kPa | 342.10 | Calculated Property |
| Pvap | 30.97 | kPa | 355.78 | Calculated Property |
| Pvap | 52.60 | kPa | 369.47 | Calculated Property |
| Pvap | 85.56 | kPa | 383.16 | Calculated Property |
| Pvap | 133.93 | kPa | 396.85 | Calculated Property |
| Pvap | 202.66 | kPa | 410.54 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Penten-3-ol.
Mixtures
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Activity Coefficients at Infinite Dilution of Volatile Compounds in Water: Effect of Temperature and Salt Concentration
- Joback Method
- 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.
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