- InChI
- InChI=1S/C7H16O/c1-3-4-5-6-7(2)8/h7-8H,3-6H2,1-2H3
- InChI Key
- CETWDUZRCINIHU-UHFFFAOYSA-N
- Formula
- C7H16O
- SMILES
- CCCCCC(C)O
- Molecular Weight1
- 116.20
- CAS
- 543-49-7
- Other Names
-
- 1-Methylhexanol
- 2-Heptyl alcohol
- 2-Hydroxyheptane
- Amyl methyl carbinol
- CH3(CH2)4CHOHCH3
- Heptan-2-ol
- Heptanol-2
- Methyl amyl carbinol
- NSC 2220
- amylmethylcarbinol
- methylpentylcarbinol
- n-Heptan-2-ol
- s-Heptyl alcohol
- 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).
- 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.
- 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 |
|---|---|---|---|
| Cp,liquid | 298.64 | J/mol×K | Vapour ... |
| η | 0.0053460 | Pa×s | Speeds ... |
| ΔfG° | -131.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -355.40 ± 2.10 | kJ/mol | NIST |
| ΔfH°liquid | -416.90 ± 0.67 | kJ/mol | NIST |
| ΔfusH° | 14.45 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 62.10 ± 0.40 | kJ/mol | NIST |
| IE | [9.70; 10.24] | eV |
|
| IE | 9.70 ± 0.03 | eV | NIST |
| IE | 10.24 | eV | NIST |
| log10WS | [-1.55; -1.55] |
|
|
| log10WS | -1.55 | Aq. Sol... | |
| log10WS | -1.55 | Estimat... | |
| logPoct/wat | 1.948 | Crippen Calculated Property | |
| McVol | 115.360 | ml/mol | McGowan Calculated Property |
| Pc | [3020.00; 3021.00] | kPa |
|
| Pc | 3021.00 | kPa | KDB |
| Pc | 3020.00 ± 20.00 | kPa | NIST |
| Pc | 3021.00 ± 20.00 | kPa | NIST |
| Pc | 3021.00 ± 20.00 | kPa | NIST |
| ρc | [262.61; 262.61] | kg/m3 |
|
| ρc | 262.61 ± 2.32 | kg/m3 | NIST |
| ρc | 262.61 ± 19.75 | kg/m3 | NIST |
| Inp | [142.33; 924.00] |
|
|
| Inp | 882.30 | NIST | |
| Inp | 888.40 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 882.50 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 901.40 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 905.10 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | Outlier 142.33 | NIST | |
| Inp | 882.30 | NIST | |
| Inp | 889.00 | NIST | |
| I | [1280.00; 1344.00] |
|
|
| I | 1294.00 | NIST | |
| I | 1307.00 | NIST | |
| I | 1319.00 | NIST | |
| I | 1319.00 | NIST | |
| I | 1325.00 | NIST | |
| I | Outlier 1285.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1335.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1298.00 | NIST | |
| I | 1301.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1322.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1296.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1303.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1308.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1323.00 | NIST | |
| I | 1290.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1326.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1333.00 | NIST | |
| I | 1335.00 | NIST | |
| I | 1312.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1328.00 | NIST | |
| I | 1315.00 | NIST | |
| I | 1313.00 | NIST | |
| I | 1312.00 | NIST | |
| I | 1316.00 | NIST | |
| I | 1316.00 | NIST | |
| I | Outlier 1286.00 | NIST | |
| I | 1328.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1319.00 | NIST | |
| I | 1320.00 | NIST | |
| I | 1320.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1326.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1322.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1326.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1332.00 | NIST | |
| I | Outlier 1280.00 | NIST | |
| I | 1304.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1311.00 | NIST | |
| I | Outlier 1284.00 | NIST | |
| I | 1322.00 | NIST | |
| I | 1315.00 | NIST | |
| I | 1290.00 | NIST | |
| I | 1290.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1326.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1300.00 | NIST | |
| I | 1312.00 | NIST | |
| I | 1335.00 | NIST | |
| I | 1326.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1304.00 | NIST | |
| I | 1322.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1320.00 | NIST | |
| I | Outlier 1284.00 | NIST | |
| I | 1293.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1320.00 | NIST | |
| I | Outlier 1286.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1298.00 | NIST | |
| I | 1296.00 | NIST | |
| I | 1318.00 | NIST | |
| I | 1290.00 | NIST | |
| Tboil | [429.40; 434.20] | K |
|
| Tboil | 432.00 | K | KDB |
| Tboil | 434.20 | K | NIST |
| Tboil | 431.15 ± 3.00 | K | NIST |
| Tboil | 432.65 ± 2.00 | K | NIST |
| Tboil | 433.55 ± 0.50 | K | NIST |
| Tboil | 432.85 ± 0.50 | K | NIST |
| Tboil | 432.55 ± 1.00 | K | NIST |
| Tboil | 434.15 ± 1.00 | K | NIST |
| Tboil | 429.65 ± 3.00 | K | NIST |
| Tboil | 431.85 ± 0.50 | K | NIST |
| Tboil | 429.40 ± 3.00 | K | NIST |
| Tboil | 432.15 ± 2.00 | K | NIST |
| Tboil | 430.65 ± 3.00 | K | NIST |
| Tboil | 434.15 ± 3.00 | K | NIST |
| Tc | [608.30; 611.40] | K |
|
| Tc | 608.30 | K | KDB |
| Tc | 608.30 ± 0.60 | K | NIST |
| Tc | 608.60 ± 0.60 | K | NIST |
| Tc | 608.30 ± 0.60 | K | NIST |
| Tc | 608.38 | K | NIST |
| Tc | Outlier 611.40 ± 0.25 | K | NIST |
| Tfus | 243.00 | K | KDB |
| Vc | [0.442; 0.442] | m3/kmol |
|
| Vc | 0.442 | m3/kmol | KDB |
| Vc | 0.442 | m3/kmol | NIST |
| Zc | 0.2640090 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [247.92; 307.23] | J/mol×K | [451.30; 615.06] |
|
| Cp,gas | 247.92 | J/mol×K | 451.30 | Joback Calculated Property |
| Cp,gas | 258.79 | J/mol×K | 478.59 | Joback Calculated Property |
| Cp,gas | 269.25 | J/mol×K | 505.89 | Joback Calculated Property |
| Cp,gas | 279.32 | J/mol×K | 533.18 | Joback Calculated Property |
| Cp,gas | 289.00 | J/mol×K | 560.47 | Joback Calculated Property |
| Cp,gas | 298.30 | J/mol×K | 587.77 | Joback Calculated Property |
| Cp,gas | 307.23 | J/mol×K | 615.06 | Joback Calculated Property |
| η | [0.0028520; 0.0050230] | Pa×s | [298.15; 313.15] |
|
| η | 0.0050030 | Pa×s | 298.15 | Densiti... |
| η | 0.0050230 | Pa×s | 298.15 | Densiti... |
| η | 0.0041520 | Pa×s | 303.15 | Densiti... |
| η | 0.0041510 | Pa×s | 303.15 | Densiti... |
| η | 0.0034780 | Pa×s | 308.15 | Densiti... |
| η | 0.0034780 | Pa×s | 308.15 | Densiti... |
| η | 0.0028530 | Pa×s | 313.15 | Densiti... |
| η | 0.0028520 | Pa×s | 313.15 | Densiti... |
| ΔvapH | [51.60; 66.10] | kJ/mol | [291.00; 394.00] |
|
| ΔvapH | 66.10 | kJ/mol | 291.00 | NIST |
| ΔvapH | 59.80 | kJ/mol | 378.00 | NIST |
| ΔvapH | 54.40 | kJ/mol | 392.00 | NIST |
| ΔvapH | 51.60 | kJ/mol | 394.00 | NIST |
| n0 | [1.41430; 1.42060] | [293.15; 308.15] |
|
|
| n0 | 1.42060 | 293.15 | Densiti... | |
| n0 | 1.41880 | 298.15 | Densiti... | |
| n0 | 1.41880 | 298.15 | Densiti... | |
| n0 | 1.41650 | 303.15 | Densiti... | |
| n0 | 1.41430 | 308.15 | Densiti... | |
| ρl | [789.38; 813.74] | kg/m3 | [298.15; 328.15] |
|
| ρl | 813.36 | kg/m3 | 298.15 | The stu... |
| ρl | 813.20 | kg/m3 | 298.15 | Thermod... |
| ρl | 813.74 | kg/m3 | 298.15 | Study o... |
| ρl | 813.38 | kg/m3 | 298.15 | Densiti... |
| ρl | 813.74 | kg/m3 | 298.15 | Densiti... |
| ρl | 809.50 | kg/m3 | 303.15 | Thermod... |
| ρl | 809.50 | kg/m3 | 303.15 | Densiti... |
| ρl | 805.72 | kg/m3 | 308.15 | Densiti... |
| ρl | 805.72 | kg/m3 | 308.15 | The stu... |
| ρl | 804.88 | kg/m3 | 308.15 | Densiti... |
| ρl | 805.70 | kg/m3 | 308.15 | Thermod... |
| ρl | 801.46 | kg/m3 | 313.15 | Densiti... |
| ρl | 801.50 | kg/m3 | 313.15 | Thermod... |
| ρl | 797.65 | kg/m3 | 318.15 | The stu... |
| ρl | 789.38 | kg/m3 | 328.15 | The stu... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.16 | 1003.00 | 802.5 |
| 313.16 | 2005.00 | 803.3 |
| 313.16 | 3002.00 | 804.0 |
| 313.16 | 4013.00 | 804.8 |
| 313.16 | 5001.00 | 805.5 |
| 313.16 | 5991.00 | 806.2 |
| 313.16 | 6993.00 | 806.9 |
| 313.16 | 7994.00 | 807.7 |
| 313.16 | 9011.00 | 808.4 |
| 313.16 | 9995.00 | 809.1 |
| 313.16 | 10990.00 | 809.8 |
| 313.16 | 11988.00 | 810.5 |
| 313.16 | 13003.00 | 811.2 |
| 313.16 | 13988.00 | 811.9 |
| 313.16 | 14992.00 | 812.6 |
| 313.16 | 15990.00 | 813.2 |
| 313.16 | 17012.00 | 813.9 |
| 313.16 | 17987.00 | 814.5 |
| 313.16 | 18982.00 | 815.2 |
| 313.16 | 20004.00 | 815.9 |
| 313.16 | 20996.00 | 816.5 |
| 313.16 | 21989.00 | 817.2 |
| 323.09 | 1026.00 | 794.4 |
| 323.09 | 2006.00 | 795.2 |
| 323.09 | 3018.00 | 796.0 |
| 323.09 | 4017.00 | 796.8 |
| 323.09 | 5005.00 | 797.5 |
| 323.09 | 6018.00 | 798.3 |
| 323.09 | 7002.00 | 799.1 |
| 323.09 | 8003.00 | 799.8 |
| 323.09 | 9017.00 | 800.6 |
| 323.09 | 10017.00 | 801.3 |
| 323.09 | 10994.00 | 802.0 |
| 323.09 | 11998.00 | 802.8 |
| 323.09 | 13028.00 | 803.5 |
| 323.09 | 13997.00 | 804.2 |
| 323.09 | 15005.00 | 804.9 |
| 323.09 | 16003.00 | 805.6 |
| 323.09 | 17013.00 | 806.3 |
| 323.09 | 18009.00 | 807.0 |
| 323.09 | 19003.00 | 807.6 |
| 323.09 | 20006.00 | 808.3 |
| 323.09 | 20998.00 | 808.9 |
| 323.09 | 22011.00 | 809.6 |
| 333.05 | 1047.00 | 786.1 |
| 333.05 | 2009.00 | 787.0 |
| 333.05 | 3005.00 | 787.8 |
| 333.05 | 4010.00 | 788.7 |
| 333.05 | 5015.00 | 789.5 |
| 333.05 | 6018.00 | 790.3 |
| 333.05 | 7022.00 | 791.1 |
| 333.05 | 8012.00 | 791.9 |
| 333.05 | 9031.00 | 792.8 |
| 333.05 | 10017.00 | 793.5 |
| 333.05 | 11080.00 | 794.3 |
| 333.05 | 12039.00 | 795.1 |
| 333.05 | 13026.00 | 795.8 |
| 333.05 | 14017.00 | 796.6 |
| 333.05 | 15024.00 | 797.3 |
| 333.05 | 16018.00 | 798.1 |
| 333.05 | 17020.00 | 798.8 |
| 333.05 | 18019.00 | 799.5 |
| 333.05 | 19029.00 | 800.2 |
| 333.05 | 20016.00 | 800.9 |
| 333.05 | 21037.00 | 801.7 |
| 333.05 | 22015.00 | 802.4 |
| 342.96 | 971.00 | 777.4 |
| 342.96 | 2038.00 | 778.5 |
| 342.96 | 3013.00 | 779.3 |
| 342.96 | 4034.00 | 780.2 |
| 342.96 | 5024.00 | 781.1 |
| 342.96 | 6033.00 | 782.0 |
| 342.96 | 7015.00 | 782.9 |
| 342.96 | 8023.00 | 783.8 |
| 342.96 | 9025.00 | 784.7 |
| 342.96 | 10020.00 | 785.4 |
| 342.96 | 11029.00 | 786.3 |
| 342.96 | 12020.00 | 787.1 |
| 342.96 | 13030.00 | 787.9 |
| 342.96 | 14039.00 | 788.7 |
| 342.96 | 15023.00 | 789.5 |
| 342.96 | 16026.00 | 790.3 |
| 342.96 | 17026.00 | 791.1 |
| 342.96 | 18034.00 | 791.9 |
| 342.96 | 19026.00 | 792.7 |
| 342.96 | 20040.00 | 793.5 |
| 342.96 | 21031.00 | 794.2 |
| 342.96 | 22028.00 | 795.0 |
| 352.85 | 1038.00 | 769.0 |
| 352.85 | 2045.00 | 770.0 |
| 352.85 | 3019.00 | 770.9 |
| 352.85 | 4058.00 | 771.9 |
| 352.85 | 5028.00 | 772.8 |
| 352.85 | 6028.00 | 773.7 |
| 352.85 | 7037.00 | 774.7 |
| 352.85 | 8022.00 | 775.5 |
| 352.85 | 9078.00 | 776.5 |
| 352.85 | 10037.00 | 777.3 |
| 352.85 | 11042.00 | 778.2 |
| 352.85 | 12042.00 | 779.0 |
| 352.85 | 13042.00 | 779.9 |
| 352.85 | 14040.00 | 780.8 |
| 352.85 | 15042.00 | 781.6 |
| 352.85 | 16053.00 | 782.5 |
| 352.85 | 17058.00 | 783.3 |
| 352.85 | 18042.00 | 784.1 |
| 352.85 | 19040.00 | 784.9 |
| 352.85 | 20070.00 | 785.7 |
| 352.85 | 21055.00 | 786.5 |
| 352.85 | 22050.00 | 787.3 |
| 362.72 | 1043.00 | 760.1 |
| 362.72 | 2049.00 | 761.2 |
| 362.72 | 3066.00 | 762.2 |
| 362.72 | 4062.00 | 763.2 |
| 362.72 | 5041.00 | 764.2 |
| 362.72 | 6045.00 | 765.2 |
| 362.72 | 7046.00 | 766.2 |
| 362.72 | 8042.00 | 767.2 |
| 362.72 | 9058.00 | 768.1 |
| 362.72 | 10038.00 | 769.0 |
| 362.72 | 11054.00 | 770.0 |
| 362.72 | 12046.00 | 770.9 |
| 362.72 | 13054.00 | 771.8 |
| 362.72 | 14048.00 | 772.7 |
| 362.72 | 15049.00 | 773.6 |
| 362.72 | 16050.00 | 774.5 |
| 362.72 | 17070.00 | 775.4 |
| 362.72 | 18065.00 | 776.2 |
| 362.72 | 19060.00 | 777.1 |
| 362.72 | 20081.00 | 777.9 |
| 362.72 | 21068.00 | 778.8 |
| 362.72 | 22063.00 | 779.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [335.65; 456.45] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.38938e+01 | |||
| Coefficient B | -2.80782e+03 | |||
| Coefficient C | -1.29285e+02 | |||
| Temperature range, min. | 335.65 | |||
| Temperature range, max. | 456.45 | |||
| Pvap | 1.33 | kPa | 335.65 | Calculated Property |
| Pvap | 3.06 | kPa | 349.07 | Calculated Property |
| Pvap | 6.38 | kPa | 362.49 | Calculated Property |
| Pvap | 12.29 | kPa | 375.92 | Calculated Property |
| Pvap | 22.12 | kPa | 389.34 | Calculated Property |
| Pvap | 37.59 | kPa | 402.76 | Calculated Property |
| Pvap | 60.76 | kPa | 416.18 | Calculated Property |
| Pvap | 94.10 | kPa | 429.61 | Calculated Property |
| Pvap | 140.38 | kPa | 443.03 | Calculated Property |
| Pvap | 202.65 | kPa | 456.45 | Calculated Property |
| Pvap | [8.06e-04; 2994.69] | kPa | [243.00; 588.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.14758e+02 | |||
| Coefficient B | -1.04894e+04 | |||
| Coefficient C | -1.44255e+01 | |||
| Coefficient D | 8.88948e-06 | |||
| Temperature range, min. | 243.00 | |||
| Temperature range, max. | 588.00 | |||
| Pvap | 8.06e-04 | kPa | 243.00 | Calculated Property |
| Pvap | 0.04 | kPa | 281.33 | Calculated Property |
| Pvap | 0.71 | kPa | 319.67 | Calculated Property |
| Pvap | 5.86 | kPa | 358.00 | Calculated Property |
| Pvap | 29.69 | kPa | 396.33 | Calculated Property |
| Pvap | 107.38 | kPa | 434.67 | Calculated Property |
| Pvap | 305.58 | kPa | 473.00 | Calculated Property |
| Pvap | 732.16 | kPa | 511.33 | Calculated Property |
| Pvap | 1548.95 | kPa | 549.67 | Calculated Property |
| Pvap | 2994.69 | kPa | 588.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Heptanol.
Mixtures
- Toluene + 2-Heptanol
- 2-Heptanol + Cyclohexane, methyl-
- 2-Heptanol + Decane
- 2-Heptanol + Formamide
- 2-Heptanol + Cyclohexanamine, N-methyl-
- Acetonitrile + 2-Heptanol
- 2-Butanone + 2-Heptanol
- 2-Heptanol + Cyclohexanone
- 2-Heptanol + N,N-Dimethylacetamide
- 2-Heptanol + Acetophenone
- Nitrogen + 2-Heptanol
- 2-Heptanol + Ethanol, 2,2'-oxybis-
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Vapor liquid equilibria for nitrogen with 2-hexanol, 2-heptanol, or 2-octanol binary systems
- Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
- A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
- Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
- Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols
- Densities and derived thermodynamic properties of 1-heptanol and 2-heptanol at temperatures from 313 K to 363 K and pressures up to 22 MPa
- Study of thermodynamic and transport properties of binary liquid mixtures of n-decane with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 K. Experimental results and application of the Prigogine-Flory-Patterson theory
- Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
- The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
- Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
- Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
- Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
- Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
- Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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