- InChI
- InChI=1S/C7H16O/c1-2-3-4-5-6-7-8/h8H,2-7H2,1H3
- InChI Key
- BBMCTIGTTCKYKF-UHFFFAOYSA-N
- Formula
- C7H16O
- SMILES
- CCCCCCCO
- Molecular Weight1
- 116.20
- CAS
- 111-70-6
- Other Names
-
- 1-HeptanoI
- 1-Heptyl alcohol
- 1-Hydroxyheptane
- Alcohol C7
- Enanthic alcohol
- Enanthyl alcohol
- Gentanol
- Heptan-1-ol
- Heptane-1-ol
- Heptanol-1
- Heptyl alcohol
- Heptyl alcohol, n-
- NSC 3703
- l'Alcool n-heptylique primaire
- n-C7H15OH
- n-Heptan-1-ol
- n-Heptanol
- n-Heptanol-1
- n-Heptyl alcohol
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- 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).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 | 0.5600 | KDB | |
| PAff | 799.00 | kJ/mol | NIST |
| Tig | 255.37 | K | KDB |
| ΔcH°liquid | [-4642.52; -4631.90] | kJ/mol |
|
| ΔcH°liquid | -4637.80 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | -4638.01 ± 0.79 | kJ/mol | NIST |
| ΔcH°liquid | -4642.52 ± 0.71 | kJ/mol | NIST |
| ΔcH°liquid | -4631.90 ± 2.30 | kJ/mol | NIST |
| ΔcH°liquid | -4631.90 | kJ/mol | NIST |
| μ | 1.70 | debye | KDB |
| Tflash,cc | 349.82 | K | KDB |
| ΔfG° | -121.00 | kJ/mol | KDB |
| ΔfH°gas | [-393.60; -329.10] | kJ/mol |
|
| ΔfH°gas | -332.00 | kJ/mol | KDB |
| ΔfH°gas | -333.70 | kJ/mol | NIST |
| ΔfH°gas | -336.60 ± 0.50 | kJ/mol | NIST |
| ΔfH°gas | -336.40 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -329.10 | kJ/mol | NIST |
| ΔfH°gas | -332.00 ± 0.90 | kJ/mol | NIST |
| ΔfH°gas | -339.70 ± 1.60 | kJ/mol | NIST |
| ΔfH°gas | Outlier -393.60 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | [-460.40; -398.80] | kJ/mol |
|
| ΔfH°liquid | -403.40 ± 0.50 | kJ/mol | NIST |
| ΔfH°liquid | -403.20 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -398.80 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | -409.40 ± 2.30 | kJ/mol | NIST |
| ΔfH°liquid | -460.40 ± 3.00 | kJ/mol | NIST |
| ΔfusH° | 17.97 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [66.40; 69.70] | kJ/mol |
|
| ΔvapH° | 66.81 | kJ/mol | NIST |
| ΔvapH° | 67.10 | kJ/mol | NIST |
| ΔvapH° | 66.90 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 66.50 | kJ/mol | NIST |
| ΔvapH° | 66.40 | kJ/mol | NIST |
| ΔvapH° | 66.81 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 66.80 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 67.80 ± 1.50 | kJ/mol | NIST |
| ΔvapH° | Outlier 69.70 | kJ/mol | NIST |
| IE | [9.84; 10.40] | eV |
|
| IE | 10.40 ± 0.10 | eV | NIST |
| IE | 9.84 | eV | NIST |
| IE | 10.35 | eV | NIST |
| log10WS | [-1.81; -1.81] |
|
|
| log10WS | -1.81 | Aq. Solubility Prediction | |
| log10WS | -1.81 | Estimated Solubility | |
| logPoct/wat | 1.949 | Crippen Calculated Property | |
| McVol | 115.360 | ml/mol | McGowan Calculated Property |
| Pc | [3058.00; 3160.00] | kPa |
|
| Pc | 3058.00 | kPa | KDB |
| Pc | 3060.00 ± 20.00 | kPa | NIST |
| Pc | 3160.00 ± 50.00 | kPa | NIST |
| Pc | 3058.00 ± 20.00 | kPa | NIST |
| Pc | 3058.00 ± 20.00 | kPa | NIST |
| ρc | [266.10; 267.26] | kg/m3 |
|
| ρc | 267.26 ± 2.32 | kg/m3 | NIST |
| ρc | 267.26 | kg/m3 | NIST |
| ρc | 266.10 ± 27.89 | kg/m3 | NIST |
| ρc | 267.26 ± 3.49 | kg/m3 | NIST |
| Inp | [154.52; 989.00] |
|
|
| Inp | 942.00 | NIST | |
| Inp | 951.60 | NIST | |
| Inp | 933.20 | NIST | |
| Inp | 939.60 | NIST | |
| Inp | 954.90 | NIST | |
| Inp | 952.80 | NIST | |
| Inp | 971.10 | NIST | |
| Inp | 969.20 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 951.80 | NIST | |
| Inp | 966.70 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 952.20 | NIST | |
| Inp | 953.30 | NIST | |
| Inp | 970.60 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 953.20 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 977.20 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 952.20 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 952.40 | NIST | |
| Inp | 952.90 | NIST | |
| Inp | 956.40 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 968.40 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | Outlier 154.52 | NIST | |
| Inp | Outlier 157.77 | NIST | |
| Inp | Outlier 155.86 | NIST | |
| Inp | 977.20 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 972.00 | NIST | |
| I | [1405.00; 1471.00] |
|
|
| I | 1456.00 | NIST | |
| I | Outlier 1405.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1453.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1444.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1431.00 | NIST | |
| I | 1425.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1423.00 | NIST | |
| I | 1437.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1463.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1446.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1457.00 | NIST | |
| I | Outlier 1421.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1463.00 | NIST | |
| I | 1445.70 | NIST | |
| I | 1452.90 | NIST | |
| I | 1450.30 | NIST | |
| I | 1447.40 | NIST | |
| I | 1449.80 | NIST | |
| I | 1449.30 | NIST | |
| I | 1449.20 | NIST | |
| I | 1448.40 | NIST | |
| I | 1424.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1444.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1464.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1453.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1463.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1467.00 | NIST | |
| I | Outlier 1419.00 | NIST | |
| I | Outlier 1419.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1436.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1453.00 | NIST | |
| I | 1429.00 | NIST | |
| I | 1463.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1467.00 | NIST | |
| I | Outlier 1419.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1455.00 | NIST | |
| I | Outlier 1419.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1430.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1423.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1436.00 | NIST | |
| I | 1429.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1441.00 | NIST | |
| S°gas | 485.80 ± 4.20 | J/mol×K | NIST |
| S°liquid | 325.90 | J/mol×K | NIST |
| Tboil | [445.90; 450.15] | K |
|
| Tboil | 449.60 | K | KDB |
| Tboil | 449.50 | K | NIST |
| Tboil | 447.30 ± 0.15 | K | NIST |
| Tboil | 449.55 ± 0.40 | K | NIST |
| Tboil | Outlier 446.15 ± 2.00 | K | NIST |
| Tboil | 448.15 ± 2.00 | K | NIST |
| Tboil | 449.55 ± 1.00 | K | NIST |
| Tboil | 449.15 ± 2.00 | K | NIST |
| Tboil | 449.25 ± 0.50 | K | NIST |
| Tboil | 449.05 ± 0.50 | K | NIST |
| Tboil | 449.15 ± 0.50 | K | NIST |
| Tboil | 449.30 ± 0.50 | K | NIST |
| Tboil | 448.55 ± 0.30 | K | NIST |
| Tboil | 447.20 ± 0.60 | K | NIST |
| Tboil | 449.65 ± 2.00 | K | NIST |
| Tboil | 448.70 ± 0.60 | K | NIST |
| Tboil | 449.30 ± 0.20 | K | NIST |
| Tboil | 447.15 ± 2.00 | K | NIST |
| Tboil | 447.90 ± 2.00 | K | NIST |
| Tboil | 447.65 ± 3.00 | K | NIST |
| Tboil | 449.96 ± 0.40 | K | NIST |
| Tboil | 448.75 ± 0.35 | K | NIST |
| Tboil | 449.45 ± 0.50 | K | NIST |
| Tboil | 449.50 ± 0.20 | K | NIST |
| Tboil | 449.30 ± 0.30 | K | NIST |
| Tboil | 448.55 ± 2.00 | K | NIST |
| Tboil | 448.15 ± 2.00 | K | NIST |
| Tboil | 449.15 ± 0.50 | K | NIST |
| Tboil | 448.15 ± 2.00 | K | NIST |
| Tboil | 447.20 ± 0.40 | K | NIST |
| Tboil | 449.15 ± 3.00 | K | NIST |
| Tboil | 447.90 ± 1.00 | K | NIST |
| Tboil | 449.15 ± 2.00 | K | NIST |
| Tboil | 447.65 ± 2.00 | K | NIST |
| Tboil | Outlier 446.15 ± 1.00 | K | NIST |
| Tboil | 448.15 ± 2.00 | K | NIST |
| Tboil | 448.15 ± 2.00 | K | NIST |
| Tboil | 450.15 ± 2.00 | K | NIST |
| Tboil | Outlier 445.90 ± 1.00 | K | NIST |
| Tboil | Outlier 445.90 ± 1.00 | K | NIST |
| Tboil | 448.15 ± 2.00 | K | NIST |
| Tboil | 447.65 ± 3.00 | K | NIST |
| Tboil | 448.70 ± 2.00 | K | NIST |
| Tboil | 449.15 ± 2.00 | K | NIST |
| Tboil | 448.95 ± 1.00 | K | NIST |
| Tc | [632.00; 638.50] | K |
|
| Tc | 632.60 | K | KDB |
| Tc | 632.60 ± 0.50 | K | NIST |
| Tc | 632.00 ± 0.80 | K | NIST |
| Tc | 632.00 ± 0.60 | K | NIST |
| Tc | 632.90 ± 0.60 | K | NIST |
| Tc | 632.50 | K | NIST |
| Tc | 632.30 ± 0.15 | K | NIST |
| Tc | 633.00 ± 2.00 | K | NIST |
| Tc | Outlier 638.50 | K | NIST |
| Tfus | [238.25; 239.40] | K |
|
| Tfus | 239.00 | K | KDB |
| Tfus | 238.65 | K | Aq. Solubility Prediction |
| Tfus | 238.25 ± 0.50 | K | NIST |
| Tfus | 239.40 ± 0.50 | K | NIST |
| Tfus | 238.60 ± 0.40 | K | NIST |
| Ttriple | [240.00; 240.00] | K |
|
| Ttriple | 240.00 ± 0.20 | K | NIST |
| Ttriple | 240.00 ± 0.20 | K | NIST |
| Vc | [0.435; 0.435] | m3/kmol |
|
| Vc | 0.435 | m3/kmol | KDB |
| Vc | 0.435 | m3/kmol | NIST |
| Zc | 0.2529070 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [247.80; 305.68] | J/mol×K | [451.74; 612.20] |
|
| Cp,gas | 247.80 | J/mol×K | 451.74 | Joback Calculated Property |
| Cp,gas | 258.38 | J/mol×K | 478.48 | Joback Calculated Property |
| Cp,gas | 268.58 | J/mol×K | 505.23 | Joback Calculated Property |
| Cp,gas | 278.39 | J/mol×K | 531.97 | Joback Calculated Property |
| Cp,gas | 287.84 | J/mol×K | 558.71 | Joback Calculated Property |
| Cp,gas | 296.94 | J/mol×K | 585.45 | Joback Calculated Property |
| Cp,gas | 305.68 | J/mol×K | 612.20 | Joback Calculated Property |
| Cp,liquid | [270.80; 297.00] | J/mol×K | [298.00; 303.35] |
|
| Cp,liquid | 274.10 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 270.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 272.29 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 273.67 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 278.57 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 278.90 | J/mol×K | 302.97 | NIST |
| Cp,liquid | 297.00 | J/mol×K | 303.35 | NIST |
| η | [0.0002110; 0.0673608] | Pa×s | [229.47; 451.74] |
|
| η | 0.0673608 | Pa×s | 229.47 | Joback Calculated Property |
| η | 0.0132124 | Pa×s | 266.51 | Joback Calculated Property |
| η | 0.0038567 | Pa×s | 303.56 | Joback Calculated Property |
| η | 0.0014716 | Pa×s | 340.61 | Joback Calculated Property |
| η | 0.0006783 | Pa×s | 377.65 | Joback Calculated Property |
| η | 0.0003591 | Pa×s | 414.70 | Joback Calculated Property |
| η | 0.0002110 | Pa×s | 451.74 | Joback Calculated Property |
| ΔfusH | [18.16; 18.35] | kJ/mol | [239.90; 240.40] |
|
| ΔfusH | 18.35 | kJ/mol | 239.90 | NIST |
| ΔfusH | 18.16 | kJ/mol | 240.40 | NIST |
| ΔfusH | 18.16 | kJ/mol | 240.40 | NIST |
| ΔfusH | 18.18 | kJ/mol | 240.40 | NIST |
| ΔfusH | 18.18 | kJ/mol | 240.40 | NIST |
| ΔvapH | [48.12; 65.20] | kJ/mol | [310.50; 449.10] |
|
| ΔvapH | 65.20 | kJ/mol | 310.50 | NIST |
| ΔvapH | 62.90 | kJ/mol | 379.00 | NIST |
| ΔvapH | 65.20 | kJ/mol | 391.00 | NIST |
| ΔvapH | 62.50 | kJ/mol | 392.50 | NIST |
| ΔvapH | 62.60 | kJ/mol | 393.00 | NIST |
| ΔvapH | 48.12 | kJ/mol | 449.10 | KDB |
| ρl | 822.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | [75.60; 75.60] | J/mol×K | [240.40; 240.40] |
|
| ΔfusS | 75.60 | J/mol×K | 240.40 | NIST |
| ΔfusS | 75.60 | J/mol×K | 240.40 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 351.70 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [344.87; 473.36] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.46759e+01 | |||
| Coefficient B | -3.44597e+03 | |||
| Coefficient C | -1.05377e+02 | |||
| Temperature range, min. | 344.87 | |||
| Temperature range, max. | 473.36 | |||
| Pvap | 1.33 | kPa | 344.87 | Calculated Property |
| Pvap | 2.99 | kPa | 359.15 | Calculated Property |
| Pvap | 6.17 | kPa | 373.42 | Calculated Property |
| Pvap | 11.82 | kPa | 387.70 | Calculated Property |
| Pvap | 21.28 | kPa | 401.98 | Calculated Property |
| Pvap | 36.28 | kPa | 416.25 | Calculated Property |
| Pvap | 59.02 | kPa | 430.53 | Calculated Property |
| Pvap | 92.18 | kPa | 444.81 | Calculated Property |
| Pvap | 138.86 | kPa | 459.08 | Calculated Property |
| Pvap | 202.64 | kPa | 473.36 | Calculated Property |
| Pvap | [1.63e-05; 2969.62] | kPa | [239.15; 631.90] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.98081e+02 | |||
| Coefficient B | -1.56272e+04 | |||
| Coefficient C | -2.63701e+01 | |||
| Coefficient D | 1.17680e-05 | |||
| Temperature range, min. | 239.15 | |||
| Temperature range, max. | 631.90 | |||
| Pvap | 1.63e-05 | kPa | 239.15 | Calculated Property |
| Pvap | 6.16e-03 | kPa | 282.79 | Calculated Property |
| Pvap | 0.31 | kPa | 326.43 | Calculated Property |
| Pvap | 4.57 | kPa | 370.07 | Calculated Property |
| Pvap | 31.12 | kPa | 413.71 | Calculated Property |
| Pvap | 127.11 | kPa | 457.34 | Calculated Property |
| Pvap | 368.82 | kPa | 500.98 | Calculated Property |
| Pvap | 849.17 | kPa | 544.62 | Calculated Property |
| Pvap | 1672.47 | kPa | 588.26 | Calculated Property |
| Pvap | 2969.62 | kPa | 631.90 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Heptanol.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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