- InChI
- InChI=1S/C10H20/c1-3-5-7-9-10-8-6-4-2/h3,5H,4,6-10H2,1-2H3/b5-3-
- InChI Key
- YKNMBTZOEVIJCM-HYXAFXHYSA-N
- Formula
- C10H20
- SMILES
- CC=CCCCCCCC
- Molecular Weight1
- 140.27
- CAS
- 20348-51-0
- Other Names
-
- (Z)-2-Decene
- (Z)-C10H20
- cis-2-Decene
- 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).
- 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).
- 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 | 0.4349 | Relay (1.0) Calculated Property | |
| ΔfG° | 113.54 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -162.99 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 21.86 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.25 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [8.90; 9.08] | eV |
|
| IE | 8.90 ± 0.01 | eV | NIST |
| IE | 9.08 ± 0.01 | eV | NIST |
| log10WS | -5.37 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.923 | Crippen Calculated Property | |
| McVol | 147.460 | ml/mol | McGowan Calculated Property |
| Pc | 2212.45 | kPa | Joback Calculated Property |
| Inp | [1001.00; 1013.00] |
|
|
| Inp | 1002.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 1009.70 | NIST | |
| Inp | 1011.30 | NIST | |
| Inp | 1002.20 | NIST | |
| Inp | 1001.20 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1011.30 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Ip | [1072.00; 1084.00] |
|
|
| Ip | 1081.00 | NIST | |
| Ip | 1082.00 | NIST | |
| Ip | 1084.00 | NIST | |
| Ip | 1074.00 | NIST | |
| Ip | 1078.00 | NIST | |
| Ip | 1075.00 | NIST | |
| Ip | 1076.00 | NIST | |
| Ip | 1074.00 | NIST | |
| Ip | 1080.70 | NIST | |
| Ip | 1084.00 | NIST | |
| Ip | 1073.70 | NIST | |
| Ip | 1077.90 | NIST | |
| Ip | 1080.70 | NIST | |
| Ip | 1084.00 | NIST | |
| Ip | 1073.70 | NIST | |
| Ip | 1077.90 | NIST | |
| Ip | 1072.00 | NIST | |
| Ip | 1072.00 | NIST | |
| Tboil | 443.47 | K | Relay (1.0) Calculated Property |
| Tc | 617.17 | K | Relay (1.0) Calculated Property |
| Tfus | 214.70 | K | Relay (1.0) Calculated Property |
| Vc | 0.572 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 43.60 | kJ/mol | 424.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [203.62; 504.66] | 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 | -2.03840e+01 | |||
| Coefficient B | 9.73840e-01 | |||
| Coefficient C | -6.04000e-04 | |||
| Coefficient D | 1.55200e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 203.62 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 255.42 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 301.48 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 342.30 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 378.38 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 410.19 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 438.23 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 463.00 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 484.98 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 504.66 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0057907; 0.0002110] | Pa×s | [197.38; 422.00] |
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 | -1.13744e+01 | |||
| Coefficient B | 1.22828e+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. | 197.38 | |||
| Temperature range, max. | 422.00 | |||
| η | 0.0057907 | Pa×s | 197.38 | Calculated Property |
| η | 0.0028798 | Pa×s | 222.34 | Calculated Property |
| η | 0.0016490 | Pa×s | 247.30 | Calculated Property |
| η | 0.0010459 | Pa×s | 272.25 | Calculated Property |
| η | 0.0007161 | Pa×s | 297.21 | Calculated Property |
| η | 0.0005199 | Pa×s | 322.17 | Calculated Property |
| η | 0.0003952 | Pa×s | 347.13 | Calculated Property |
| η | 0.0003117 | Pa×s | 372.08 | Calculated Property |
| η | 0.0002533 | Pa×s | 397.04 | Calculated Property |
| η | 0.0002110 | Pa×s | 422.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [346.20; 461.20] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.74478e+01 | |||
| Coefficient B | -4.76701e+03 | |||
| Coefficient C | -6.84040e+01 | |||
| Temperature range, min. | 346.20 | |||
| Temperature range, max. | 461.20 | |||
| Pvap | 1.33 | kPa | 346.20 | Calculated Property |
| Pvap | 2.84 | kPa | 358.98 | Calculated Property |
| Pvap | 5.66 | kPa | 371.76 | Calculated Property |
| Pvap | 10.68 | kPa | 384.53 | Calculated Property |
| Pvap | 19.19 | kPa | 397.31 | Calculated Property |
| Pvap | 32.99 | kPa | 410.09 | Calculated Property |
| Pvap | 54.55 | kPa | 422.87 | Calculated Property |
| Pvap | 87.11 | kPa | 435.64 | Calculated Property |
| Pvap | 134.77 | kPa | 448.42 | Calculated Property |
| Pvap | 202.68 | kPa | 461.20 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Decene, (Z)-.
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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