- InChI
- InChI=1S/C7H14/c1-6-3-4-7(2)5-6/h6-7H,3-5H2,1-2H3/t6-,7+
- InChI Key
- XAZKFISIRYLAEE-KNVOCYPGSA-N
- Formula
- C7H14
- SMILES
- CC1CCC(C)C1
- Molecular Weight1
- 98.19
- CAS
- 2532-58-3
- Other Names
-
- 1,3-Dimethylcyclopentane cis
- 1,CIS-3-DIMETHYLCYCLOPENTANE
- 1-cis-3-Dimethylcyclopentane
- CIS-1,3-DIMETHYLCYCLOPENTANE
- c-1,3-Dimethylcyclopentane
- 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).
- ΔfH°liquid : Liquid phase 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).
- 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).
- Ttriple : Triple Point Temperature (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 | -4587.30 ± 1.40 | kJ/mol | NIST |
| ΔfG° | 36.90 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -133.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | -168.20 ± 1.40 | kJ/mol | NIST |
| ΔfusH° | 8.89 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [34.20; 34.60] | kJ/mol |
|
| ΔvapH° | 34.30 | kJ/mol | NIST |
| ΔvapH° | 34.30 | kJ/mol | NIST |
| ΔvapH° | 34.20 | kJ/mol | NIST |
| ΔvapH° | 34.60 | kJ/mol | NIST |
| log10WS | -2.16 | Crippen Calculated Property | |
| logPoct/wat | 2.442 | Crippen Calculated Property | |
| McVol | 98.630 | ml/mol | McGowan Calculated Property |
| Pc | 3291.59 | kPa | Joback Calculated Property |
| Inp | [674.96; 694.00] |
|
|
| Inp | 680.40 | NIST | |
| Inp | 683.90 | NIST | |
| Inp | Outlier 675.00 | NIST | |
| Inp | 687.30 | NIST | |
| Inp | 685.50 | NIST | |
| Inp | 685.60 | NIST | |
| Inp | 685.60 | NIST | |
| Inp | 685.80 | NIST | |
| Inp | 685.30 | NIST | |
| Inp | 683.30 | NIST | |
| Inp | 687.50 | NIST | |
| Inp | 682.70 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 681.90 | NIST | |
| Inp | 685.40 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 681.70 | NIST | |
| Inp | 683.40 | NIST | |
| Inp | 685.10 | NIST | |
| Inp | 686.80 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 685.50 | NIST | |
| Inp | 685.80 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 682.90 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | Outlier 692.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 683.50 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | Outlier 694.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 681.50 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 680.80 | NIST | |
| Inp | Outlier 674.96 | NIST | |
| Inp | Outlier 675.65 | NIST | |
| Inp | 687.90 | NIST | |
| Inp | 679.90 | NIST | |
| Inp | 677.60 | NIST | |
| Inp | 677.66 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 677.50 | NIST | |
| Inp | 677.64 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 677.48 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 677.48 | NIST | |
| Inp | 680.80 | NIST | |
| Inp | 677.60 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 684.00 | NIST | |
| Tboil | [363.70; 364.87] | K |
|
| Tboil | 364.00 | K | NIST |
| Tboil | 363.90 | K | NIST |
| Tboil | 363.95 ± 0.30 | K | NIST |
| Tboil | Outlier 364.87 ± 0.02 | K | NIST |
| Tboil | 364.11 ± 0.50 | K | NIST |
| Tboil | 364.05 ± 0.20 | K | NIST |
| Tboil | 363.70 ± 0.40 | K | NIST |
| Tboil | 363.85 ± 0.60 | K | NIST |
| Tboil | 363.90 ± 0.50 | K | NIST |
| Tboil | 363.85 ± 0.50 | K | NIST |
| Tc | 551.90 | K | NIST |
| Tfus | [134.55; 139.46] | K |
|
| Tfus | 139.35 ± 0.40 | K | NIST |
| Tfus | 139.40 ± 0.30 | K | NIST |
| Tfus | Outlier 134.55 ± 4.00 | K | NIST |
| Tfus | 139.44 ± 0.05 | K | NIST |
| Tfus | 139.46 ± 0.02 | K | NIST |
| Tfus | 139.39 ± 0.20 | K | NIST |
| Tfus | 139.46 ± 0.10 | K | NIST |
| Tfus | 139.39 ± 0.07 | K | NIST |
| Tfus | 139.44 ± 0.05 | K | NIST |
| Tfus | 139.44 ± 0.05 | K | NIST |
| Tfus | 139.44 ± 0.03 | K | NIST |
| Tfus | 136.40 ± 1.50 | K | NIST |
| Ttriple | 139.48 ± 0.07 | K | NIST |
| Vc | 0.367 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [161.69; 226.12] | J/mol×K | [352.20; 500.20] |
|
| Cp,gas | 161.69 ± 0.32 | J/mol×K | 352.20 | NIST |
| Cp,gas | 172.23 ± 0.34 | J/mol×K | 375.20 | NIST |
| Cp,gas | 190.57 ± 0.38 | J/mol×K | 415.20 | NIST |
| Cp,gas | 207.77 ± 0.42 | J/mol×K | 455.20 | NIST |
| Cp,gas | 226.12 ± 0.45 | J/mol×K | 500.20 | NIST |
| η | [0.0002650; 0.0017720] | Pa×s | [175.31; 370.17] |
|
| η | 0.0017720 | Pa×s | 175.31 | Joback Calculated Property |
| η | 0.0010080 | Pa×s | 207.79 | Joback Calculated Property |
| η | 0.0006678 | Pa×s | 240.26 | Joback Calculated Property |
| η | 0.0004881 | Pa×s | 272.74 | Joback Calculated Property |
| η | 0.0003813 | Pa×s | 305.22 | Joback Calculated Property |
| η | 0.0003124 | Pa×s | 337.69 | Joback Calculated Property |
| η | 0.0002650 | Pa×s | 370.17 | Joback Calculated Property |
| ΔvapH | [30.40; 34.20] | kJ/mol | [322.62; 364.00] |
|
| ΔvapH | 32.83 ± 0.00 | kJ/mol | 322.62 | NIST |
| ΔvapH | 32.80 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 34.20 | kJ/mol | 330.50 | NIST |
| ΔvapH | 34.00 | kJ/mol | 332.50 | NIST |
| ΔvapH | 31.70 ± 0.10 | kJ/mol | 342.00 | NIST |
| ΔvapH | 30.40 | kJ/mol | 363.90 | NIST |
| ΔvapH | 30.40 ± 0.10 | kJ/mol | 364.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [261.79; 389.38] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44248e+01 | |||
| Coefficient B | -3.27206e+03 | |||
| Coefficient C | -3.03370e+01 | |||
| Temperature range, min. | 261.79 | |||
| Temperature range, max. | 389.38 | |||
| Pvap | 1.33 | kPa | 261.79 | Calculated Property |
| Pvap | 3.02 | kPa | 275.97 | Calculated Property |
| Pvap | 6.24 | kPa | 290.14 | Calculated Property |
| Pvap | 11.97 | kPa | 304.32 | Calculated Property |
| Pvap | 21.54 | kPa | 318.50 | Calculated Property |
| Pvap | 36.68 | kPa | 332.67 | Calculated Property |
| Pvap | 59.56 | kPa | 346.85 | Calculated Property |
| Pvap | 92.77 | kPa | 361.03 | Calculated Property |
| Pvap | 139.34 | kPa | 375.20 | Calculated Property |
| Pvap | 202.66 | kPa | 389.38 | Calculated Property |
| Pvap | [1.75e-07; 3508.11] | kPa | [139.45; 551.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.40317e+01 | |||
| Coefficient B | -6.01095e+03 | |||
| Coefficient C | -7.41243e+00 | |||
| Coefficient D | 6.01324e-06 | |||
| Temperature range, min. | 139.45 | |||
| Temperature range, max. | 551.00 | |||
| Pvap | 1.75e-07 | kPa | 139.45 | Calculated Property |
| Pvap | 9.83e-04 | kPa | 185.18 | Calculated Property |
| Pvap | 0.13 | kPa | 230.91 | Calculated Property |
| Pvap | 2.96 | kPa | 276.63 | Calculated Property |
| Pvap | 24.49 | kPa | 322.36 | Calculated Property |
| Pvap | 112.30 | kPa | 368.09 | Calculated Property |
| Pvap | 355.22 | kPa | 413.82 | Calculated Property |
| Pvap | 881.27 | kPa | 459.54 | Calculated Property |
| Pvap | 1858.06 | kPa | 505.27 | Calculated Property |
| Pvap | 3508.11 | kPa | 551.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclopentane, 1,3-dimethyl-, cis-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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