- InChI
- InChI=1S/C10H18/c1-3-5-7-9-10-8-6-4-2/h3,5,7-10H2,1-2H3
- InChI Key
- RWDDSTHSVISBEA-UHFFFAOYSA-N
- Formula
- C10H18
- SMILES
- CC#CCCCCCCC
- Molecular Weight1
- 138.25
- CAS
- 2384-70-5
- Other Names
-
- 2-C10H18
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×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).
- 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).
- 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 |
|---|---|---|---|
| ω | 0.3878 | Relay (1.0) Calculated Property | |
| ΔfG° | 236.12 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 23.60 ± 3.40 | kJ/mol | NIST |
| ΔfusH° | 24.78 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 54.01 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.30 ± 0.02 | eV | NIST |
| log10WS | -4.58 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.370 | Crippen Calculated Property | |
| McVol | 143.160 | ml/mol | McGowan Calculated Property |
| Pc | 2455.60 | kPa | Joback Calculated Property |
| Inp | [1040.00; 1064.00] |
|
|
| Inp | 1041.00 | NIST | |
| Inp | Outlier 1064.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1040.00 | NIST | |
| I | [1234.50; 1265.00] |
|
|
| I | 1240.70 | NIST | |
| I | 1248.00 | NIST | |
| I | 1251.70 | NIST | |
| I | 1263.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1234.50 | NIST | |
| I | 1253.20 | NIST | |
| I | 1237.10 | NIST | |
| I | 1255.50 | NIST | |
| I | 1256.90 | NIST | |
| Tboil | 442.75 | K | Relay (1.0) Calculated Property |
| Tc | 646.07 | K | Relay (1.0) Calculated Property |
| Tfus | 235.91 | K | Relay (1.0) Calculated Property |
| Vc | 0.546 | m3/kmol | Relay (1.0) Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 357.00 | K | 3.10 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [200.72; 474.12] | 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 | 1.13560e+01 | |||
| Coefficient B | 8.04040e-01 | |||
| Coefficient C | -4.28060e-04 | |||
| Coefficient D | 8.67800e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 200.72 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 246.07 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 287.04 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 323.90 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 356.93 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 386.39 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 412.56 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 435.73 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 456.15 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 474.12 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [346.20; 484.49] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54033e+01 | |||
| Coefficient B | -4.19906e+03 | |||
| Coefficient C | -6.84040e+01 | |||
| Temperature range, min. | 346.20 | |||
| Temperature range, max. | 484.49 | |||
| Pvap | 1.33 | kPa | 346.20 | Calculated Property |
| Pvap | 2.94 | kPa | 361.57 | Calculated Property |
| Pvap | 6.01 | kPa | 376.93 | Calculated Property |
| Pvap | 11.46 | kPa | 392.30 | Calculated Property |
| Pvap | 20.62 | kPa | 407.66 | Calculated Property |
| Pvap | 35.25 | kPa | 423.03 | Calculated Property |
| Pvap | 57.63 | kPa | 438.39 | Calculated Property |
| Pvap | 90.62 | kPa | 453.76 | Calculated Property |
| Pvap | 137.62 | kPa | 469.12 | Calculated Property |
| Pvap | 202.64 | kPa | 484.49 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Decyne.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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