- InChI
- InChI=1S/C6H12/c1-5(2)6-3-4-6/h5-6H,3-4H2,1-2H3
- InChI Key
- HPBROFGYTXOJIO-UHFFFAOYSA-N
- Formula
- C6H12
- SMILES
- CC(C)C1CC1
- Molecular Weight1
- 84.16
- CAS
- 3638-35-5
- Other Names
-
- 2-CYCLOPROPYLPROPANE
- Cyclopropane, (1-methylethyl)-
- Cyclopropane, isopropyl-
- Isopropylcyclopropane
- 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).
- 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.
- 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 |
|---|---|---|---|
| ΔfG° | 57.95 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -99.65 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 5.91 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 28.48 | kJ/mol | Joback Calculated Property |
| log10WS | -1.75 | Crippen Calculated Property | |
| logPoct/wat | 2.052 | Crippen Calculated Property | |
| McVol | 84.540 | ml/mol | McGowan Calculated Property |
| Pc | 3646.53 | kPa | Joback Calculated Property |
| Inp | [569.90; 577.00] |
|
|
| Inp | 570.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 569.90 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 570.00 | NIST | |
| Tboil | 342.98 | K | Joback Calculated Property |
| Tc | 525.87 | K | Joback Calculated Property |
| Tfus | [154.83; 160.22] | K |
|
| Tfus | 160.18 ± 0.10 | K | NIST |
| Tfus | 160.22 ± 0.06 | K | NIST |
| Tfus | 160.18 ± 0.20 | K | NIST |
| Tfus | 160.22 ± 0.10 | K | NIST |
| Tfus | 160.18 ± 0.10 | K | NIST |
| Tfus | 160.22 ± 0.07 | K | NIST |
| Tfus | 159.98 ± 0.10 | K | NIST |
| Tfus | 160.08 ± 0.06 | K | NIST |
| Tfus | 159.98 ± 0.08 | K | NIST |
| Tfus | 159.45 ± 0.20 | K | NIST |
| Tfus | 160.08 ± 0.10 | K | NIST |
| Tfus | 154.85 ± 0.40 | K | NIST |
| Tfus | 154.85 ± 3.00 | K | NIST |
| Tfus | 154.83 ± 3.00 | K | NIST |
| Vc | 0.323 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [140.64; 207.39] | J/mol×K | [342.98; 525.87] |
|
| Cp,gas | 140.64 | J/mol×K | 342.98 | Joback Calculated Property |
| Cp,gas | 153.29 | J/mol×K | 373.46 | Joback Calculated Property |
| Cp,gas | 165.30 | J/mol×K | 403.94 | Joback Calculated Property |
| Cp,gas | 176.68 | J/mol×K | 434.43 | Joback Calculated Property |
| Cp,gas | 187.48 | J/mol×K | 464.91 | Joback Calculated Property |
| Cp,gas | 197.71 | J/mol×K | 495.39 | Joback Calculated Property |
| Cp,gas | 207.39 | J/mol×K | 525.87 | Joback Calculated Property |
| η | [0.0002728; 0.0010214] | Pa×s | [160.32; 342.98] |
|
| η | 0.0010214 | Pa×s | 160.32 | Joback Calculated Property |
| η | 0.0006877 | Pa×s | 190.76 | Joback Calculated Property |
| η | 0.0005163 | Pa×s | 221.21 | Joback Calculated Property |
| η | 0.0004154 | Pa×s | 251.65 | Joback Calculated Property |
| η | 0.0003504 | Pa×s | 282.09 | Joback Calculated Property |
| η | 0.0003054 | Pa×s | 312.54 | Joback Calculated Property |
| η | 0.0002728 | Pa×s | 342.98 | Joback Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [245.18; 352.43] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.52356e+01 | |||
| Coefficient B | -3.16714e+03 | |||
| Coefficient C | -3.32990e+01 | |||
| Temperature range, min. | 245.18 | |||
| Temperature range, max. | 352.43 | |||
| Pvap | 1.33 | kPa | 245.18 | Calculated Property |
| Pvap | 2.96 | kPa | 257.10 | Calculated Property |
| Pvap | 6.05 | kPa | 269.01 | Calculated Property |
| Pvap | 11.54 | kPa | 280.93 | Calculated Property |
| Pvap | 20.76 | kPa | 292.85 | Calculated Property |
| Pvap | 35.47 | kPa | 304.76 | Calculated Property |
| Pvap | 57.93 | kPa | 316.68 | Calculated Property |
| Pvap | 90.95 | kPa | 328.60 | Calculated Property |
| Pvap | 137.88 | kPa | 340.51 | Calculated Property |
| Pvap | 202.62 | kPa | 352.43 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 2-cyclopropyl-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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