- InChI
- InChI=1S/C5H12O/c1-3-5(6)4-2/h5-6H,3-4H2,1-2H3
- InChI Key
- AQIXEPGDORPWBJ-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- CCC(O)CC
- Molecular Weight1
- 88.15
- CAS
- 584-02-1
- Other Names
-
- (C2H5)2CHOH
- 1-Ethyl-1-propanol
- 3-PENTYL ALCOHOL
- DIETHYL CARBINOL
- ISOAMYL ALCOHOL
- NSC 8654
- Pentan-3-ol
- Pentanol-3
- UN 2706
- sec-Amyl alcohol
- sec-Pentanol
- sec-Pentyl alcohol
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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°liquid : Liquid 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).
- 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).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- S°gas : Molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- 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 |
|---|---|---|---|
| ΔcH°liquid | -3312.30 ± 0.46 | kJ/mol | NIST |
| ΔfG° | -148.04 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-318.60; -314.70] | kJ/mol |
|
| ΔfH°gas | -317.20 | kJ/mol | NIST |
| ΔfH°gas | -314.70 ± 1.10 | kJ/mol | NIST |
| ΔfH°gas | -318.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | [-370.30; -368.90] | kJ/mol |
|
| ΔfH°liquid | -368.90 ± 0.79 | kJ/mol | NIST |
| ΔfH°liquid | -370.30 ± 0.59 | kJ/mol | NIST |
| ΔfusH° | 1.66 | kJ/mol | Heat Ca... |
| ΔvapH° | [51.70; 54.03] | kJ/mol |
|
| ΔvapH° | 54.03 | kJ/mol | NIST |
| ΔvapH° | 53.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 51.70 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 52.90 | kJ/mol | NIST |
| IE | [9.73; 10.25] | eV |
|
| IE | 9.76 ± 0.02 | eV | NIST |
| IE | 9.78 ± 0.07 | eV | NIST |
| IE | 9.78 | eV | NIST |
| IE | 9.78 | eV | NIST |
| IE | 9.73 | eV | NIST |
| IE | Outlier 10.25 | eV | NIST |
| log10WS | [-0.24; -0.24] |
|
|
| log10WS | -0.24 | Aq. Sol... | |
| log10WS | -0.24 | Estimat... | |
| logPoct/wat | 1.167 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| Pc | 3916.03 | kPa | Joback Calculated Property |
| ρc | [270.61; 270.61] | kg/m3 |
|
| ρc | 270.61 | kg/m3 | NIST |
| ρc | 270.61 ± 20.27 | kg/m3 | NIST |
| Inp | [661.00; 712.00] |
|
|
| Inp | 669.20 | NIST | |
| Inp | 676.50 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | Outlier 661.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | Outlier 710.00 | NIST | |
| Inp | Outlier 712.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 669.20 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | Outlier 712.00 | NIST | |
| I | [1087.00; 1128.00] |
|
|
| I | 1097.00 | NIST | |
| I | 1102.00 | NIST | |
| I | 1111.00 | NIST | |
| I | Outlier 1124.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1096.00 | NIST | |
| I | 1100.00 | NIST | |
| I | Outlier 1087.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1098.00 | NIST | |
| I | 1103.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1116.00 | NIST | |
| I | Outlier 1093.00 | NIST | |
| I | 1101.00 | NIST | |
| I | 1110.00 | NIST | |
| I | Outlier 1128.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1106.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1104.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1104.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1104.00 | NIST | |
| I | 1103.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1106.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1107.00 | NIST | |
| S°gas | 382.21 | J/mol×K | NIST |
| Tboil | [361.90; 391.10] | K |
|
| Tboil | 389.40 | K | KDB |
| Tboil | 389.30 | K | NIST |
| Tboil | Outlier 361.90 ± 1.50 | K | NIST |
| Tboil | 388.75 ± 2.00 | K | NIST |
| Tboil | 386.65 ± 2.00 | K | NIST |
| Tboil | 388.15 ± 3.00 | K | NIST |
| Tboil | 385.15 ± 3.00 | K | NIST |
| Tboil | 387.65 ± 1.50 | K | NIST |
| Tboil | 388.65 ± 0.30 | K | NIST |
| Tboil | 389.35 ± 0.50 | K | NIST |
| Tboil | 389.40 ± 1.00 | K | NIST |
| Tboil | 388.85 ± 0.50 | K | NIST |
| Tboil | 387.15 ± 2.00 | K | NIST |
| Tboil | 387.65 ± 2.00 | K | NIST |
| Tboil | 388.45 ± 1.00 | K | NIST |
| Tboil | 389.15 ± 1.00 | K | NIST |
| Tboil | 385.65 ± 3.00 | K | NIST |
| Tboil | 389.15 ± 0.70 | K | NIST |
| Tboil | 387.95 ± 2.00 | K | NIST |
| Tboil | 391.10 ± 2.00 | K | NIST |
| Tboil | 388.15 ± 2.00 | K | NIST |
| Tboil | 387.15 ± 2.00 | K | NIST |
| Tboil | 388.80 ± 0.50 | K | NIST |
| Tboil | 388.80 ± 0.20 | K | NIST |
| Tboil | 386.15 ± 3.00 | K | NIST |
| Tboil | 387.90 ± 2.00 | K | NIST |
| Tboil | 390.15 ± 2.00 | K | NIST |
| Tboil | 388.65 ± 1.00 | K | NIST |
| Tboil | 389.25 ± 0.30 | K | NIST |
| Tboil | 390.15 ± 2.00 | K | NIST |
| Tboil | 389.15 ± 2.00 | K | NIST |
| Tboil | 389.05 ± 0.50 | K | NIST |
| Tboil | 388.15 ± 0.50 | K | NIST |
| Tboil | 388.50 ± 0.30 | K | NIST |
| Tboil | 387.65 ± 2.00 | K | NIST |
| Tboil | 388.50 ± 0.50 | K | NIST |
| Tboil | 389.15 ± 2.00 | K | NIST |
| Tboil | 386.70 ± 2.00 | K | NIST |
| Tc | [559.60; 559.60] | K |
|
| Tc | 559.60 | K | KDB |
| Tc | 559.60 ± 0.50 | K | NIST |
| Tc | 559.60 | K | NIST |
| Tc | 559.60 ± 0.25 | K | NIST |
| Tfus | [202.10; 204.00] | K |
|
| Tfus | 204.00 | K | KDB |
| Tfus | 202.10 | K | Aq. Sol... |
| Vc | [0.325; 0.325] | m3/kmol |
|
| Vc | 0.325 | m3/kmol | KDB |
| Vc | 0.325 | m3/kmol | NIST |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [169.82; 216.94] | J/mol×K | [405.54; 570.76] |
|
| Cp,gas | 169.82 | J/mol×K | 405.54 | Joback Calculated Property |
| Cp,gas | 178.43 | J/mol×K | 433.08 | Joback Calculated Property |
| Cp,gas | 186.73 | J/mol×K | 460.61 | Joback Calculated Property |
| Cp,gas | 194.72 | J/mol×K | 488.15 | Joback Calculated Property |
| Cp,gas | 202.42 | J/mol×K | 515.68 | Joback Calculated Property |
| Cp,gas | 209.82 | J/mol×K | 543.22 | Joback Calculated Property |
| Cp,gas | 216.94 | J/mol×K | 570.76 | Joback Calculated Property |
| Cp,liquid | 239.70 | J/mol×K | 298.00 | NIST |
| η | [0.0002833; 0.3005917] | Pa×s | [191.93; 405.54] |
|
| η | 0.3005917 | Pa×s | 191.93 | Joback Calculated Property |
| η | 0.0379452 | Pa×s | 227.53 | Joback Calculated Property |
| η | 0.0083860 | Pa×s | 263.13 | Joback Calculated Property |
| η | 0.0026559 | Pa×s | 298.74 | Joback Calculated Property |
| η | 0.0010745 | Pa×s | 334.34 | Joback Calculated Property |
| η | 0.0005174 | Pa×s | 369.94 | Joback Calculated Property |
| η | 0.0002833 | Pa×s | 405.54 | Joback Calculated Property |
| ΔfusH | [9.08; 9.08] | kJ/mol | [204.20; 204.20] |
|
| ΔfusH | 9.08 | kJ/mol | 204.20 | NIST |
| ΔfusH | 9.08 | kJ/mol | 204.20 | NIST |
| ΔvapH | [49.60; 59.90] | kJ/mol | [298.50; 353.00] |
|
| ΔvapH | 53.60 | kJ/mol | 298.50 | NIST |
| ΔvapH | 59.90 | kJ/mol | 317.50 | NIST |
| ΔvapH | 50.20 | kJ/mol | 341.50 | NIST |
| ΔvapH | 49.60 | kJ/mol | 353.00 | NIST |
| Pvap | [0.23; 97.99] | kPa | [279.05; 387.65] |
|
| Pvap | 0.23 | kPa | 279.05 | Vapor P... |
| Pvap | 0.32 | kPa | 282.62 | Vapor P... |
| Pvap | 0.47 | kPa | 287.46 | Vapor P... |
| Pvap | 0.74 | kPa | 293.45 | Vapor P... |
| Pvap | 0.77 | kPa | 293.92 | Vapor P... |
| Pvap | 1.04 | kPa | 298.17 | Vapor P... |
| Pvap | 1.40 | kPa | 302.31 | Vapor P... |
| Pvap | 2.05 | kPa | 307.87 | Vapor P... |
| Pvap | 2.83 | kPa | 312.86 | Vapor P... |
| Pvap | 4.01 | kPa | 318.42 | Vapor P... |
| Pvap | 14.66 | kPa | 342.02 | Vapor p... |
| Pvap | 17.33 | kPa | 345.41 | Vapor p... |
| Pvap | 20.00 | kPa | 348.40 | Vapor p... |
| Pvap | 22.66 | kPa | 351.07 | Vapor p... |
| Pvap | 26.00 | kPa | 354.07 | Vapor p... |
| Pvap | 29.33 | kPa | 356.77 | Vapor p... |
| Pvap | 32.66 | kPa | 359.24 | Vapor p... |
| Pvap | 34.66 | kPa | 360.62 | Vapor p... |
| Pvap | 38.00 | kPa | 362.79 | Vapor p... |
| Pvap | 41.33 | kPa | 364.81 | Vapor p... |
| Pvap | 45.33 | kPa | 367.06 | Vapor p... |
| Pvap | 49.33 | kPa | 369.16 | Vapor p... |
| Pvap | 53.33 | kPa | 371.13 | Vapor p... |
| Pvap | 57.33 | kPa | 372.99 | Vapor p... |
| Pvap | 61.33 | kPa | 374.75 | Vapor p... |
| Pvap | 66.66 | kPa | 376.95 | Vapor p... |
| Pvap | 71.99 | kPa | 379.02 | Vapor p... |
| Pvap | 77.33 | kPa | 380.97 | Vapor p... |
| Pvap | 82.66 | kPa | 382.82 | Vapor p... |
| Pvap | 89.33 | kPa | 385.00 | Vapor p... |
| Pvap | 95.99 | kPa | 387.06 | Vapor p... |
| Pvap | 97.99 | kPa | 387.65 | Vapor p... |
| n0 | [1.39810; 1.40870] | [298.15; 318.15] |
|
|
| n0 | 1.40870 | 298.15 | Phase E... | |
| n0 | 1.40470 | 298.15 | Densiti... | |
| n0 | 1.40290 | 308.15 | Densiti... | |
| n0 | 1.39810 | 318.15 | Densiti... | |
| ρl | [806.90; 835.70] | kg/m3 | [273.65; 308.15] |
|
| ρl | 835.70 | kg/m3 | 273.65 | Tempera... |
| ρl | 835.30 | kg/m3 | 274.15 | Tempera... |
| ρl | 834.90 | kg/m3 | 274.65 | Tempera... |
| ρl | 834.50 | kg/m3 | 275.15 | Tempera... |
| ρl | 834.10 | kg/m3 | 275.65 | Tempera... |
| ρl | 833.70 | kg/m3 | 276.15 | Tempera... |
| ρl | 833.30 | kg/m3 | 276.65 | Tempera... |
| ρl | 832.90 | kg/m3 | 277.15 | Tempera... |
| ρl | 832.50 | kg/m3 | 277.65 | Tempera... |
| ρl | 832.10 | kg/m3 | 278.15 | Tempera... |
| ρl | 831.70 | kg/m3 | 278.65 | Tempera... |
| ρl | 831.30 | kg/m3 | 279.15 | Tempera... |
| ρl | 830.90 | kg/m3 | 279.65 | Tempera... |
| ρl | 830.50 | kg/m3 | 280.15 | Tempera... |
| ρl | 830.10 | kg/m3 | 280.65 | Tempera... |
| ρl | 829.70 | kg/m3 | 281.15 | Tempera... |
| ρl | 829.30 | kg/m3 | 281.65 | Tempera... |
| ρl | 828.90 | kg/m3 | 282.15 | Tempera... |
| ρl | 815.62 | kg/m3 | 298.15 | Excess ... |
| ρl | 815.80 | kg/m3 | 298.15 | Asymmet... |
| ρl | 806.90 | kg/m3 | 308.15 | Excess ... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 387.70 | K | 99.90 | NIST |
Datasets
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 100.00 | 1234.7 |
| 303.15 | 10000.00 | 1294.0 |
| 303.15 | 20000.00 | 1348.2 |
| 303.15 | 30000.00 | 1397.7 |
| 303.15 | 40000.00 | 1443.6 |
| 303.15 | 50000.00 | 1486.9 |
| 303.15 | 60000.00 | 1526.0 |
| 303.15 | 70000.00 | 1564.7 |
| 303.15 | 80000.00 | 1600.5 |
| 303.15 | 90000.00 | 1636.4 |
| 303.15 | 100000.00 | 1668.2 |
| 313.15 | 100.00 | 1194.7 |
| 313.15 | 10000.00 | 1257.0 |
| 313.15 | 20000.00 | 1313.0 |
| 313.15 | 30000.00 | 1364.7 |
| 313.15 | 40000.00 | 1411.9 |
| 313.15 | 50000.00 | 1456.0 |
| 313.15 | 60000.00 | 1498.1 |
| 313.15 | 70000.00 | 1537.4 |
| 313.15 | 80000.00 | 1574.5 |
| 313.15 | 90000.00 | 1610.2 |
| 313.15 | 100000.00 | 1644.1 |
| 323.15 | 100.00 | 1155.2 |
| 323.15 | 10000.00 | 1219.2 |
| 323.15 | 20000.00 | 1277.9 |
| 323.15 | 30000.00 | 1331.0 |
| 323.15 | 40000.00 | 1380.2 |
| 323.15 | 50000.00 | 1425.8 |
| 323.15 | 60000.00 | 1468.5 |
| 323.15 | 70000.00 | 1508.9 |
| 323.15 | 80000.00 | 1547.2 |
| 323.15 | 90000.00 | 1583.6 |
| 323.15 | 100000.00 | 1618.6 |
| 333.15 | 100.00 | 1115.9 |
| 333.15 | 10000.00 | 1182.2 |
| 333.15 | 20000.00 | 1243.1 |
| 333.15 | 30000.00 | 1298.2 |
| 333.15 | 40000.00 | 1348.6 |
| 333.15 | 50000.00 | 1395.9 |
| 333.15 | 60000.00 | 1439.4 |
| 333.15 | 70000.00 | 1480.7 |
| 333.15 | 80000.00 | 1519.8 |
| 333.15 | 90000.00 | 1556.9 |
| 333.15 | 100000.00 | 1592.2 |
| 343.15 | 100.00 | 1076.8 |
| 343.15 | 10000.00 | 1146.9 |
| 343.15 | 20000.00 | 1209.7 |
| 343.15 | 30000.00 | 1266.6 |
| 343.15 | 40000.00 | 1318.2 |
| 343.15 | 50000.00 | 1366.4 |
| 343.15 | 60000.00 | 1411.1 |
| 343.15 | 70000.00 | 1453.1 |
| 343.15 | 80000.00 | 1492.9 |
| 343.15 | 90000.00 | 1530.7 |
| 343.15 | 100000.00 | 1566.6 |
| 353.15 | 100.00 | 1036.7 |
| 353.15 | 10000.00 | 1110.4 |
| 353.15 | 20000.00 | 1176.2 |
| 353.15 | 30000.00 | 1234.1 |
| 353.15 | 40000.00 | 1287.8 |
| 353.15 | 50000.00 | 1337.3 |
| 353.15 | 60000.00 | 1383.1 |
| 353.15 | 70000.00 | 1425.8 |
| 353.15 | 80000.00 | 1466.6 |
| 353.15 | 90000.00 | 1505.0 |
| 353.15 | 100000.00 | 1541.4 |
| 363.15 | 100.00 | 997.3 |
| 363.15 | 10000.00 | 1075.3 |
| 363.15 | 20000.00 | 1143.2 |
| 363.15 | 30000.00 | 1203.5 |
| 363.15 | 40000.00 | 1258.2 |
| 363.15 | 50000.00 | 1308.3 |
| 363.15 | 60000.00 | 1355.1 |
| 363.15 | 70000.00 | 1399.6 |
| 363.15 | 80000.00 | 1440.8 |
| 363.15 | 90000.00 | 1479.7 |
| 363.15 | 100000.00 | 1516.9 |
| 373.15 | 100.00 | 957.2 |
| 373.15 | 10000.00 | 1038.9 |
| 373.15 | 20000.00 | 1109.6 |
| 373.15 | 30000.00 | 1171.5 |
| 373.15 | 40000.00 | 1228.3 |
| 373.15 | 50000.00 | 1280.1 |
| 373.15 | 60000.00 | 1328.2 |
| 373.15 | 70000.00 | 1373.1 |
| 373.15 | 80000.00 | 1415.0 |
| 373.15 | 90000.00 | 1454.6 |
| 373.15 | 100000.00 | 1492.5 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [299.83; 409.85] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44746e+01 | |||
| Coefficient B | -2.84676e+03 | |||
| Coefficient C | -9.91730e+01 | |||
| Temperature range, min. | 299.83 | |||
| Temperature range, max. | 409.85 | |||
| Pvap | 1.33 | kPa | 299.83 | Calculated Property |
| Pvap | 3.01 | kPa | 312.05 | Calculated Property |
| Pvap | 6.22 | kPa | 324.28 | Calculated Property |
| Pvap | 11.94 | kPa | 336.50 | Calculated Property |
| Pvap | 21.48 | kPa | 348.73 | Calculated Property |
| Pvap | 36.60 | kPa | 360.95 | Calculated Property |
| Pvap | 59.45 | kPa | 373.18 | Calculated Property |
| Pvap | 92.65 | kPa | 385.40 | Calculated Property |
| Pvap | 139.24 | kPa | 397.63 | Calculated Property |
| Pvap | 202.66 | kPa | 409.85 | Calculated Property |
| Pvap | [4.93e-05; 3720.52] | kPa | [204.15; 547.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.10919e+01 | |||
| Coefficient B | -9.04205e+03 | |||
| Coefficient C | -1.06916e+01 | |||
| Coefficient D | 3.55838e-06 | |||
| Temperature range, min. | 204.15 | |||
| Temperature range, max. | 547.00 | |||
| Pvap | 4.93e-05 | kPa | 204.15 | Calculated Property |
| Pvap | 8.90e-03 | kPa | 242.24 | Calculated Property |
| Pvap | 0.32 | kPa | 280.34 | Calculated Property |
| Pvap | 4.21 | kPa | 318.43 | Calculated Property |
| Pvap | 28.63 | kPa | 356.53 | Calculated Property |
| Pvap | 123.86 | kPa | 394.62 | Calculated Property |
| Pvap | 388.85 | kPa | 432.72 | Calculated Property |
| Pvap | 967.13 | kPa | 470.81 | Calculated Property |
| Pvap | 2024.12 | kPa | 508.91 | Calculated Property |
| Pvap | 3720.52 | kPa | 547.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 3-Pentanol.
Mixtures
- n-Butyl ether + 3-Pentanol
- 3-Pentanol + Water
- Methane, nitro- + 3-Pentanol
- 3-Pentanone + 3-Pentanol
- 2-Pentanone + 3-Pentanol
- 2-Pentanone + 3-Pentanone + 3-Pentanol
- 2-Butanone + 3-Pentanol
- Propane + 3-Pentanol
- Propene + 3-Pentanol
- Butane + 3-Pentanol
- 3-Pentanol + Isobutane
- 1-Butene + 3-Pentanol
- 1-Propene, 2-methyl- + 3-Pentanol
- 2-Butene, (E)- + 3-Pentanol
- 1,3-Butadiene + 3-Pentanol
- 2-Butene, (Z)- + 3-Pentanol
- Dimethyl ether + 3-Pentanol
- Ethyl Chloride + 3-Pentanol
- Ethane, 1,1-difluoro- + 3-Pentanol
- Carbon dioxide + 3-Pentanol
Find more mixtures with 3-Pentanol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
- The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
- Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
- Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
- Study of the volumetric properties of weakly associated alcohols by means of high-pressure speed of sound measurements
- Measurement and modeling of high-pressure (vapor + liquid) equilibria of (CO2 + alkanol) binary systems
- Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
- Temperature of maximum density for aqueous mixtures of three pentanol isomers
- Asymmetric liquid-liquid criticality in the ideal volumetric mixing approximation
- Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
- Phase Equilibria in the Binary and Ternary Systems Composed of Diethyl ketone, 2-Pentanone and 3-Pentanol at 101.3 kPa
- Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
- Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
- Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched Pentanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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