- InChI
- InChI=1S/C10H20/c1-2-4-6-8-10-9-7-5-3-1/h1-10H2
- InChI Key
- LMGZGXSXHCMSAA-UHFFFAOYSA-N
- Formula
- C10H20
- SMILES
- C1CCCCCCCCC1
- Molecular Weight1
- 140.27
- CAS
- 293-96-9
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- 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).
- 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).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-6600.30; -6586.20] | kJ/mol |
|
| ΔcH°liquid | -6586.20 ± 0.90 | kJ/mol | NIST |
| ΔcH°liquid | -6600.30 ± 6.30 | kJ/mol | NIST |
| ΔfG° | 17.08 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -199.71 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 4.02 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 39.28 | kJ/mol | Joback Calculated Property |
| IE | [9.60; 10.00] | eV |
|
| IE | 9.60 | eV | NIST |
| IE | 10.00 ± 0.05 | eV | NIST |
| log10WS | -3.90 | Crippen Calculated Property | |
| logPoct/wat | 3.901 | Crippen Calculated Property | |
| McVol | 140.900 | ml/mol | McGowan Calculated Property |
| Pc | 2953.69 | kPa | Joback Calculated Property |
| Inp | [1127.00; 1198.00] |
|
|
| Inp | 1179.00 | NIST | |
| Inp | 1177.40 | NIST | |
| Inp | 1133.90 | NIST | |
| Inp | 1128.70 | NIST | |
| Inp | 1131.20 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1198.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1128.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1198.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1128.00 | NIST | |
| I | [1261.00; 1271.00] |
|
|
| I | 1271.00 | NIST | |
| I | 1261.00 | NIST | |
| I | 1261.00 | NIST | |
| Tboil | [474.00; 475.20] | K |
|
| Tboil | 474.00 | K | NIST |
| Tboil | 475.20 | K | NIST |
| Tboil | 474.00 ± 5.00 | K | NIST |
| Tc | 700.22 | K | Joback Calculated Property |
| Tfus | 285.00 ± 1.00 | K | NIST |
| Vc | 0.497 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [300.19; 424.80] | J/mol×K | [469.50; 700.22] |
|
| Cp,gas | 300.19 | J/mol×K | 469.50 | Joback Calculated Property |
| Cp,gas | 324.11 | J/mol×K | 507.95 | Joback Calculated Property |
| Cp,gas | 346.77 | J/mol×K | 546.41 | Joback Calculated Property |
| Cp,gas | 368.15 | J/mol×K | 584.86 | Joback Calculated Property |
| Cp,gas | 388.28 | J/mol×K | 623.32 | Joback Calculated Property |
| Cp,gas | 407.16 | J/mol×K | 661.77 | Joback Calculated Property |
| Cp,gas | 424.80 | J/mol×K | 700.22 | Joback Calculated Property |
| η | [0.0001282; 0.1570752] | Pa×s | [200.00; 469.50] |
|
| η | 0.1570752 | Pa×s | 200.00 | Joback Calculated Property |
| η | 0.0161987 | Pa×s | 244.92 | Joback Calculated Property |
| η | 0.0033780 | Pa×s | 289.83 | Joback Calculated Property |
| η | 0.0010728 | Pa×s | 334.75 | Joback Calculated Property |
| η | 0.0004470 | Pa×s | 379.67 | Joback Calculated Property |
| η | 0.0002241 | Pa×s | 424.58 | Joback Calculated Property |
| η | 0.0001282 | Pa×s | 469.50 | Joback Calculated Property |
| ΔfusH | 18.95 | kJ/mol | 282.70 | NIST |
| ΔvapH | [45.10; 48.20] | kJ/mol | [364.50; 446.50] |
|
| ΔvapH | 48.20 | kJ/mol | 364.50 | NIST |
| ΔvapH | 45.10 | kJ/mol | 446.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [346.41; 494.02] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47755e+01 | |||
| Coefficient B | -4.02883e+03 | |||
| Coefficient C | -6.83260e+01 | |||
| Temperature range, min. | 346.41 | |||
| Temperature range, max. | 494.02 | |||
| Pvap | 1.33 | kPa | 346.41 | Calculated Property |
| Pvap | 2.99 | kPa | 362.81 | Calculated Property |
| Pvap | 6.15 | kPa | 379.21 | Calculated Property |
| Pvap | 11.77 | kPa | 395.61 | Calculated Property |
| Pvap | 21.18 | kPa | 412.01 | Calculated Property |
| Pvap | 36.13 | kPa | 428.42 | Calculated Property |
| Pvap | 58.82 | kPa | 444.82 | Calculated Property |
| Pvap | 91.95 | kPa | 461.22 | Calculated Property |
| Pvap | 138.68 | kPa | 477.62 | Calculated Property |
| Pvap | 202.63 | kPa | 494.02 | Calculated Property |
| Pvap | [1.14; 137.00] | kPa | [343.15; 489.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.04758e+02 | |||
| Coefficient B | -9.84919e+03 | |||
| Coefficient C | -1.31529e+01 | |||
| Coefficient D | 7.31120e-06 | |||
| Temperature range, min. | 343.15 | |||
| Temperature range, max. | 489.15 | |||
| Pvap | 1.14 | kPa | 343.15 | Calculated Property |
| Pvap | 2.46 | kPa | 359.37 | Calculated Property |
| Pvap | 4.90 | kPa | 375.59 | Calculated Property |
| Pvap | 9.11 | kPa | 391.82 | Calculated Property |
| Pvap | 15.96 | kPa | 408.04 | Calculated Property |
| Pvap | 26.55 | kPa | 424.26 | Calculated Property |
| Pvap | 42.22 | kPa | 440.48 | Calculated Property |
| Pvap | 64.58 | kPa | 456.71 | Calculated Property |
| Pvap | 95.47 | kPa | 472.93 | Calculated Property |
| Pvap | 137.00 | kPa | 489.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclodecane.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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