- InChI
- InChI=1S/C5H10/c1-4-3-5(4)2/h4-5H,3H2,1-2H3/t4-,5+
- InChI Key
- VKJLDXGFBJBTRQ-SYDPRGILSA-N
- Formula
- C5H10
- SMILES
- CC1CC1C
- Molecular Weight1
- 70.13
- CAS
- 930-18-7
- Other Names
-
- 1,cis-2-Dimethylcyclopropane
- c-1,2-Dimethylcyclopropane
- cis-1,2-Dimethylcyclopropane
- ω : Acentric Factor.
- 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).
- 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.
- 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 | 0.2591 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -3370.40 ± 0.59 | kJ/mol | NIST |
| ΔfG° | 44.26 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -28.65 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | -26.30 ± 0.67 | kJ/mol | NIST |
| ΔfusH° | 7.91 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 26.81 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.76 ± 0.02 | eV | NIST |
| log10WS | -3.59 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.662 | Crippen Calculated Property | |
| McVol | 70.450 | ml/mol | McGowan Calculated Property |
| Pc | 3901.37 | kPa | Joback Calculated Property |
| Inp | [513.00; 519.00] |
|
|
| Inp | 513.00 | NIST | |
| Inp | 514.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 517.00 | NIST | |
| Inp | 516.00 | NIST | |
| Inp | 518.00 | NIST | |
| Inp | 519.00 | NIST | |
| Inp | 516.00 | NIST | |
| Inp | 516.00 | NIST | |
| Inp | 513.10 | NIST | |
| Inp | 514.00 | NIST | |
| Inp | 516.00 | NIST | |
| Inp | 517.00 | NIST | |
| Inp | 518.00 | NIST | |
| Inp | 515.80 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 517.00 | NIST | |
| Inp | 515.00 | NIST | |
| Tboil | [305.65; 310.45] | K |
|
| Tboil | 310.20 | K | NIST |
| Tboil | 310.45 ± 0.50 | K | NIST |
| Tboil | 310.18 ± 0.20 | K | NIST |
| Tboil | 310.18 ± 0.30 | K | NIST |
| Tboil | 308.55 ± 1.00 | K | NIST |
| Tboil | 310.45 ± 0.60 | K | NIST |
| Tboil | Outlier 305.65 ± 4.00 | K | NIST |
| Tc | 483.98 | K | Relay (1.0) Calculated Property |
| Tfus | [124.28; 132.28] | K |
|
| Tfus | 132.22 ± 1.50 | K | NIST |
| Tfus | 132.22 ± 0.20 | K | NIST |
| Tfus | 132.24 ± 0.04 | K | NIST |
| Tfus | 132.25 ± 0.03 | K | NIST |
| Tfus | 132.28 ± 0.02 | K | NIST |
| Tfus | 132.07 ± 0.20 | K | NIST |
| Tfus | 132.24 ± 0.80 | K | NIST |
| Tfus | 132.25 ± 0.06 | K | NIST |
| Tfus | Outlier 124.28 ± 0.03 | K | NIST |
| Tfus | 132.22 ± 0.20 | K | NIST |
| Tfus | 132.20 ± 0.20 | K | NIST |
| Vc | 0.259 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [90.37; 263.68] | 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 | -4.59600e+01 | |||
| Coefficient B | 6.03240e-01 | |||
| Coefficient C | -4.13000e-04 | |||
| Coefficient D | 1.19400e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 90.37 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 121.05 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 147.99 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 171.57 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 192.17 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 210.17 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 225.94 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 239.87 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 252.32 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 263.68 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0001932; 0.0001779] | Pa×s | [132.22; 345.44] |
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 | -8.68558e+00 | |||
| Coefficient B | 1.77100e+01 | |||
| 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. | 132.22 | |||
| Temperature range, max. | 345.44 | |||
| η | 0.0001932 | Pa×s | 132.22 | Calculated Property |
| η | 0.0001893 | Pa×s | 155.91 | Calculated Property |
| η | 0.0001865 | Pa×s | 179.60 | Calculated Property |
| η | 0.0001844 | Pa×s | 203.29 | Calculated Property |
| η | 0.0001827 | Pa×s | 226.98 | Calculated Property |
| η | 0.0001814 | Pa×s | 250.67 | Calculated Property |
| η | 0.0001803 | Pa×s | 274.36 | Calculated Property |
| η | 0.0001794 | Pa×s | 298.06 | Calculated Property |
| η | 0.0001786 | Pa×s | 321.75 | Calculated Property |
| η | 0.0001779 | Pa×s | 345.44 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [228.14; 328.40] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53715e+01 | |||
| Coefficient B | -3.02830e+03 | |||
| Coefficient C | -2.73800e+01 | |||
| Temperature range, min. | 228.14 | |||
| Temperature range, max. | 328.40 | |||
| Pvap | 1.33 | kPa | 228.14 | Calculated Property |
| Pvap | 2.95 | kPa | 239.28 | Calculated Property |
| Pvap | 6.01 | kPa | 250.42 | Calculated Property |
| Pvap | 11.47 | kPa | 261.56 | Calculated Property |
| Pvap | 20.64 | kPa | 272.70 | Calculated Property |
| Pvap | 35.28 | kPa | 283.84 | Calculated Property |
| Pvap | 57.68 | kPa | 294.98 | Calculated Property |
| Pvap | 90.67 | kPa | 306.12 | Calculated Property |
| Pvap | 137.65 | kPa | 317.26 | Calculated Property |
| Pvap | 202.62 | kPa | 328.40 | Calculated Property |
Similar Compounds
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bW1vnl3v5ubm7u5unJHoevToEcdxNTU1Tk5Oe/bsyczMxMqugekns2vXLtYzEuLj47Njx45r165N+r7ANNjo9fq3vwH9/f3Nzc2Dg4NvftPNzc3Dw8OY7ztR0dHR2O4ynslzB7Aa2JkBQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMh/wEisF+rahRzGAAAAABJRU5ErkJggg==)
Find more compounds similar to Cyclopropane, 1,2-dimethyl-, cis-.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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