- InChI
- InChI=1S/C10H20/c1-8(2)10-6-4-9(3)5-7-10/h8-10H,4-7H2,1-3H3/t9-,10+
- InChI Key
- CFJYNSNXFXLKNS-AOOOYVTPSA-N
- Formula
- C10H20
- SMILES
- CC1CCC(C(C)C)CC1
- Molecular Weight1
- 140.27
- CAS
- 6069-98-3
- Other Names
-
- 1-Isopropyl-4-methyl-cyclohexane, cis
- 1-Isopropyl-cis-4-methylcyclohexane
- 1-Methyl-4-(1-methylethyl)-cyclohexane, cis
- 1-Methyl-cis-4-isopropylcyclohexane
- cis-1-Isopropyl-4-methylcyclohexane
- cis-1-Methyl-4-isopropylcyclohexane
- cis-p-Menthane
- p-Menthane, Z-
- p-Menthane, cis-
- 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).
- 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 | 0.2892 | Relay (1.0) Calculated Property | |
| ΔfG° | 47.62 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -193.50 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 11.04 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 47.38 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.18 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.17 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.469 | Crippen Calculated Property | |
| McVol | 140.900 | ml/mol | McGowan Calculated Property |
| Pc | 2505.01 | kPa | Joback Calculated Property |
| Inp | [973.00; 1027.00] |
|
|
| Inp | 989.90 | NIST | |
| Inp | 994.70 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | Outlier 1027.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 989.00 | NIST | |
| Ip | 1058.00 | NIST | |
| Tboil | 445.92 ± 0.30 | K | NIST |
| Tc | 633.62 | K | Relay (1.0) Calculated Property |
| Tfus | [183.28; 185.55] | K |
|
| Tfus | 185.55 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 183.28 ± 0.09 | K | NIST |
| Tfus | 183.30 ± 0.06 | K | NIST |
| Tfus | 183.35 ± 0.04 | K | NIST |
| Vc | 0.500 | m3/kmol | Relay (1.0) Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 444.10 | K | 96.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [181.45; 527.51] | 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 | -6.75500e+01 | |||
| Coefficient B | 1.05536e+00 | |||
| Coefficient C | -5.49000e-04 | |||
| Coefficient D | 8.87000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 181.45 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 241.03 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 294.67 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 342.65 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 385.26 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 422.78 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 455.48 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 483.65 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 507.57 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 527.51 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0103104; 0.0002409] | Pa×s | [183.87; 450.80] |
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 | -1.09184e+01 | |||
| Coefficient B | 1.16644e+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. | 183.87 | |||
| Temperature range, max. | 450.80 | |||
| η | 0.0103104 | Pa×s | 183.87 | Calculated Property |
| η | 0.0042717 | Pa×s | 213.53 | Calculated Property |
| η | 0.0021941 | Pa×s | 243.19 | Calculated Property |
| η | 0.0013026 | Pa×s | 272.85 | Calculated Property |
| η | 0.0008566 | Pa×s | 302.51 | Calculated Property |
| η | 0.0006071 | Pa×s | 332.17 | Calculated Property |
| η | 0.0004553 | Pa×s | 361.82 | Calculated Property |
| η | 0.0003566 | Pa×s | 391.48 | Calculated Property |
| η | 0.0002891 | Pa×s | 421.14 | Calculated Property |
| η | 0.0002409 | Pa×s | 450.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [328.62; 475.12] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43549e+01 | |||
| Coefficient B | -3.70979e+03 | |||
| Coefficient C | -6.49020e+01 | |||
| Temperature range, min. | 328.62 | |||
| Temperature range, max. | 475.12 | |||
| Pvap | 1.33 | kPa | 328.62 | Calculated Property |
| Pvap | 3.02 | kPa | 344.90 | Calculated Property |
| Pvap | 6.25 | kPa | 361.18 | Calculated Property |
| Pvap | 12.01 | kPa | 377.45 | Calculated Property |
| Pvap | 21.61 | kPa | 393.73 | Calculated Property |
| Pvap | 36.79 | kPa | 410.01 | Calculated Property |
| Pvap | 59.70 | kPa | 426.29 | Calculated Property |
| Pvap | 92.93 | kPa | 442.56 | Calculated Property |
| Pvap | 139.45 | kPa | 458.84 | Calculated Property |
| Pvap | 202.63 | kPa | 475.12 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexane, 1-methyl-4-(1-methylethyl)-, cis-.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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