- InChI
- InChI=1S/C5H10/c1-2-5-3-4-5/h5H,2-4H2,1H3
- InChI Key
- FOTXAJDDGPYIFU-UHFFFAOYSA-N
- Formula
- C5H10
- SMILES
- CCC1CC1
- Molecular Weight1
- 70.13
- CAS
- 1191-96-4
- Other Names
-
- Ethylcyclopropane
- 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).
- 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 |
|---|---|---|---|
| ω | 0.2395 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | [-3384.00; -3371.90] | kJ/mol |
|
| ΔcH°liquid | -3371.90 ± 0.75 | kJ/mol | NIST |
| ΔcH°liquid | -3384.00 | kJ/mol | NIST |
| ΔfG° | 51.97 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -26.42 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | -24.80 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 6.84 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 26.86 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [8.96; 9.50] | eV |
|
| IE | 8.96 ± 0.05 | eV | NIST |
| IE | 9.50 | eV | NIST |
| log10WS | -3.33 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.806 | Crippen Calculated Property | |
| McVol | 70.450 | ml/mol | McGowan Calculated Property |
| Pc | 4067.32 | kPa | Joback Calculated Property |
| Inp | [506.00; 550.00] |
|
|
| Inp | 508.00 | NIST | |
| Inp | 508.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 511.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 516.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 508.30 | NIST | |
| Inp | 511.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | Outlier 550.00 | NIST | |
| Inp | 508.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 506.00 | NIST | |
| Inp | 510.00 | NIST | |
| Tboil | [307.90; 309.80] | K |
|
| Tboil | 309.10 | K | NIST |
| Tboil | 309.00 ± 0.60 | K | NIST |
| Tboil | 309.08 ± 0.20 | K | NIST |
| Tboil | 309.22 ± 0.30 | K | NIST |
| Tboil | 309.11 ± 0.30 | K | NIST |
| Tboil | 309.40 ± 0.40 | K | NIST |
| Tboil | 309.09 ± 0.30 | K | NIST |
| Tboil | 309.05 ± 0.50 | K | NIST |
| Tboil | 309.15 ± 1.00 | K | NIST |
| Tboil | 309.80 ± 0.30 | K | NIST |
| Tboil | Outlier 307.90 ± 1.00 | K | NIST |
| Tc | 498.81 | K | Relay (1.0) Calculated Property |
| Tfus | [123.74; 124.05] | K |
|
| Tfus | 124.05 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 123.87 ± 0.06 | K | NIST |
| Tfus | 123.88 ± 0.03 | K | NIST |
| Tfus | 123.74 ± 0.20 | K | NIST |
| Tfus | 123.75 ± 0.20 | K | NIST |
| Ttriple | [123.55; 123.56] | K |
|
| Ttriple | 123.56 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | 123.55 ± 0.20 | K | NIST |
| Vc | 0.259 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [88.11; 257.02] | 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 | -5.18990e+01 | |||
| Coefficient B | 6.29720e-01 | |||
| Coefficient C | -4.68400e-04 | |||
| Coefficient D | 1.47600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 88.11 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 118.79 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 145.41 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 168.42 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 188.30 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 205.52 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 220.53 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 233.80 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 245.81 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 257.02 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0008487; 0.0002129] | Pa×s | [123.86; 349.35] |
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 | -9.21458e+00 | |||
| Coefficient B | 2.65400e+02 | |||
| 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. | 123.86 | |||
| Temperature range, max. | 349.35 | |||
| η | 0.0008487 | Pa×s | 123.86 | Calculated Property |
| η | 0.0005918 | Pa×s | 148.91 | Calculated Property |
| η | 0.0004578 | Pa×s | 173.97 | Calculated Property |
| η | 0.0003778 | Pa×s | 199.02 | Calculated Property |
| η | 0.0003255 | Pa×s | 224.08 | Calculated Property |
| η | 0.0002889 | Pa×s | 249.13 | Calculated Property |
| η | 0.0002621 | Pa×s | 274.19 | Calculated Property |
| η | 0.0002417 | Pa×s | 299.24 | Calculated Property |
| η | 0.0002257 | Pa×s | 324.30 | Calculated Property |
| η | 0.0002129 | Pa×s | 349.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [227.26; 328.84] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.52123e+01 | |||
| Coefficient B | -2.98777e+03 | |||
| Coefficient C | -2.70740e+01 | |||
| Temperature range, min. | 227.26 | |||
| Temperature range, max. | 328.84 | |||
| Pvap | 1.33 | kPa | 227.26 | Calculated Property |
| Pvap | 2.96 | kPa | 238.55 | Calculated Property |
| Pvap | 6.05 | kPa | 249.83 | Calculated Property |
| Pvap | 11.55 | kPa | 261.12 | Calculated Property |
| Pvap | 20.78 | kPa | 272.41 | Calculated Property |
| Pvap | 35.50 | kPa | 283.69 | Calculated Property |
| Pvap | 57.97 | kPa | 294.98 | Calculated Property |
| Pvap | 91.00 | kPa | 306.27 | Calculated Property |
| Pvap | 137.92 | kPa | 317.55 | Calculated Property |
| Pvap | 202.62 | kPa | 328.84 | Calculated Property |
Similar Compounds
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bW1vnl3v5ubm7u5unJHoevToEcdxNTU1Tk5Oe/bsyczMxMqugekns2vXLtYzEuLj47Njx45r165N+r7ANNjo9fq3vwH9/f3Nzc2Dg4NvftPNzc3Dw8OY7ztR0dHR2O4ynslzB7Aa2JkBQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMhyB0IQe5ACHIHQpA7EILcgRDkDoQgdyAEuQMh/wEisF+rahRzGAAAAABJRU5ErkJggg==)
Find more compounds similar to Cyclopropane, ethyl-.
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).
- Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
- 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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