- InChI
- InChI=1S/C12H24/c1-3-5-7-9-11-12-10-8-6-4-2/h3,5H,4,6-12H2,1-2H3/b5-3+
- InChI Key
- ADOQBZAVKYCFOI-HWKANZROSA-N
- Formula
- C12H24
- SMILES
- CC=CCCCCCCCCC
- Molecular Weight1
- 168.32
- CAS
- 7206-13-5
- Other Names
-
- (2E)-2-Dodecene
- (E)-2-Dodecene
- 2-Dodecene, trans-
- trans-2-Dodecene
- ω : Acentric Factor.
- Cp,gas : Ideal gas 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).
- 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.
- Ip : 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 | 0.5206 | Relay (1.0) Calculated Property | |
| ΔfG° | 130.38 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -207.63 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 27.04 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 62.05 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.91 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.02 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.703 | Crippen Calculated Property | |
| McVol | 175.640 | ml/mol | McGowan Calculated Property |
| Pc | 1861.11 | kPa | Joback Calculated Property |
| Inp | [1196.80; 1205.00] |
|
|
| Inp | 1197.00 | NIST | |
| Inp | 1202.00 | NIST | |
| Inp | 1202.00 | NIST | |
| Inp | 1202.00 | NIST | |
| Inp | 1203.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1202.90 | NIST | |
| Inp | 1196.90 | NIST | |
| Inp | 1196.90 | NIST | |
| Inp | 1196.80 | NIST | |
| Inp | 1196.90 | NIST | |
| Inp | Outlier 1205.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1196.90 | NIST | |
| Ip | [1251.80; 1267.50] |
|
|
| Ip | Outlier 1251.80 | NIST | |
| Ip | 1254.40 | NIST | |
| Ip | 1255.70 | NIST | |
| Ip | 1265.00 | NIST | |
| Ip | 1266.00 | NIST | |
| Ip | 1266.00 | NIST | |
| Ip | 1266.00 | NIST | |
| Ip | 1267.00 | NIST | |
| Ip | 1260.00 | NIST | |
| Ip | 1260.00 | NIST | |
| Ip | 1260.00 | NIST | |
| Ip | 1261.00 | NIST | |
| Ip | 1261.00 | NIST | |
| Ip | 1260.00 | NIST | |
| Ip | 1265.00 | NIST | |
| Ip | 1266.00 | NIST | |
| Ip | 1266.00 | NIST | |
| Ip | 1267.00 | NIST | |
| Ip | 1266.50 | NIST | |
| Ip | 1267.50 | NIST | |
| Ip | 1266.50 | NIST | |
| Ip | 1267.50 | NIST | |
| Ip | 1261.00 | NIST | |
| Ip | 1263.00 | NIST | |
| Ip | Outlier 1251.80 | NIST | |
| Ip | 1266.00 | NIST | |
| Ip | 1260.00 | NIST | |
| Ip | 1266.50 | NIST | |
| Tboil | 481.96 | K | Relay (1.0) Calculated Property |
| Tc | 654.86 | K | Relay (1.0) Calculated Property |
| Tfus | 240.41 | K | Relay (1.0) Calculated Property |
| Vc | 0.686 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [246.04; 607.84] | 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 | -2.22020e+01 | |||
| Coefficient B | 1.16384e+00 | |||
| Coefficient C | -7.12800e-04 | |||
| Coefficient D | 1.79000e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 246.04 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 308.25 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 363.64 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 412.76 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 456.20 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 494.51 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 528.27 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 558.03 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 584.36 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 607.84 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0058071; 0.0002118] | Pa×s | [219.92; 452.52] |
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 | -1.15901e+01 | |||
| Coefficient B | 1.41660e+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. | 219.92 | |||
| Temperature range, max. | 452.52 | |||
| η | 0.0058071 | Pa×s | 219.92 | Calculated Property |
| η | 0.0029497 | Pa×s | 245.76 | Calculated Property |
| η | 0.0017044 | Pa×s | 271.61 | Calculated Property |
| η | 0.0010834 | Pa×s | 297.45 | Calculated Property |
| η | 0.0007404 | Pa×s | 323.30 | Calculated Property |
| η | 0.0005353 | Pa×s | 349.14 | Calculated Property |
| η | 0.0004047 | Pa×s | 374.99 | Calculated Property |
| η | 0.0003172 | Pa×s | 400.83 | Calculated Property |
| η | 0.0002561 | Pa×s | 426.67 | Calculated Property |
| η | 0.0002118 | Pa×s | 452.52 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [365.54; 508.49] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.48867e+01 | |||
| Coefficient B | -3.97767e+03 | |||
| Coefficient C | -9.30800e+01 | |||
| Temperature range, min. | 365.54 | |||
| Temperature range, max. | 508.49 | |||
| Pvap | 1.33 | kPa | 365.54 | Calculated Property |
| Pvap | 2.98 | kPa | 381.42 | Calculated Property |
| Pvap | 6.12 | kPa | 397.31 | Calculated Property |
| Pvap | 11.71 | kPa | 413.19 | Calculated Property |
| Pvap | 21.08 | kPa | 429.07 | Calculated Property |
| Pvap | 35.97 | kPa | 444.96 | Calculated Property |
| Pvap | 58.60 | kPa | 460.84 | Calculated Property |
| Pvap | 91.71 | kPa | 476.72 | Calculated Property |
| Pvap | 138.49 | kPa | 492.61 | Calculated Property |
| Pvap | 202.64 | kPa | 508.49 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Dodecene, (E)-.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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