- InChI
- InChI=1S/C5H9Cl/c6-5-3-1-2-4-5/h5H,1-4H2
- InChI Key
- NDTCXABJQNJPCF-UHFFFAOYSA-N
- Formula
- C5H9Cl
- SMILES
- ClC1CCCC1
- Molecular Weight1
- 104.58
- CAS
- 930-28-9
- Other Names
-
- Chlorocyclopentane
- Cyclopentyl chloride
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfH°gas | -101.14 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 6.84 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [38.79; 38.80] | kJ/mol |
|
| ΔvapH° | 38.79 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 38.80 | kJ/mol | NIST |
| ΔvapH° | 38.79 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 38.80 | kJ/mol | NIST |
| IE | 10.24 | eV | Relay (1.0) Calculated Property |
| logPoct/wat | 2.168 | Crippen Calculated Property | |
| McVol | 82.690 | ml/mol | McGowan Calculated Property |
| Inp | [758.00; 804.00] |
|
|
| Inp | 762.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 760.00 | NIST | |
| S°liquid | 238.04 | J/mol×K | NIST |
| Tboil | [387.20; 387.35] | K |
|
| Tboil | 387.20 | K | NIST |
| Tboil | 387.35 ± 0.20 | K | NIST |
| Tfus | 178.85 ± 0.30 | K | NIST |
| Ttriple | [180.00; 180.00] | K |
|
| Ttriple | 180.00 ± 0.10 | K | NIST |
| Ttriple | 180.00 ± 0.10 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 152.40 | J/mol×K | 298.15 | NIST |
| ΔfusH | [0.64; 7.63] | kJ/mol | [169.40; 180.00] |
|
| ΔfusH | 7.63 | kJ/mol | 169.40 | NIST |
| ΔfusH | 0.64 | kJ/mol | 180.00 | NIST |
| ΔfusH | 0.64 | kJ/mol | 180.00 | NIST |
| ΔfusH | 0.64 | kJ/mol | 180.00 | NIST |
| ΔvapH | [37.40; 38.79] | kJ/mol | [298.15; 354.50] |
|
| ΔvapH | 38.79 | kJ/mol | 298.15 | NIST |
| ΔvapH | 38.79 | kJ/mol | 298.15 | NIST |
| ΔvapH | 37.40 | kJ/mol | 354.50 | NIST |
| ΔfusS | [3.54; 45.05] | J/mol×K | [169.40; 180.00] |
|
| ΔfusS | 45.05 | J/mol×K | 169.40 | NIST |
| ΔfusS | 3.54 | J/mol×K | 180.00 | NIST |
| ΔvapS | [130.10; 130.10] | J/mol×K | [298.15; 298.15] |
|
| ΔvapS | 130.10 | J/mol×K | 298.15 | NIST |
| ΔvapS | 130.10 | J/mol×K | 298.15 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [91.73; 268.85] | 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 | -4.92500e+01 | |||
| Coefficient B | 6.17300e-01 | |||
| Coefficient C | -3.96000e-04 | |||
| Coefficient D | 9.68000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 91.73 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 123.86 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 152.16 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 176.95 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 198.52 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 217.18 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 233.23 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 246.99 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 258.76 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 268.85 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0041727; 0.0002881] | Pa×s | [178.85; 400.73] |
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 | -1.03070e+01 | |||
| Coefficient B | 8.63460e+02 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 178.85 | |||
| Temperature range, max. | 400.73 | |||
| η | 0.0041727 | Pa×s | 178.85 | Calculated Property |
| η | 0.0023249 | Pa×s | 203.50 | Calculated Property |
| η | 0.0014699 | Pa×s | 228.16 | Calculated Property |
| η | 0.0010163 | Pa×s | 252.81 | Calculated Property |
| η | 0.0007503 | Pa×s | 277.46 | Calculated Property |
| η | 0.0005820 | Pa×s | 302.12 | Calculated Property |
| η | 0.0004691 | Pa×s | 326.77 | Calculated Property |
| η | 0.0003897 | Pa×s | 351.42 | Calculated Property |
| η | 0.0003318 | Pa×s | 376.08 | Calculated Property |
| η | 0.0002881 | Pa×s | 400.73 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [294.22; 370.52] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.97435e+01 | |||
| Coefficient B | -4.26454e+03 | |||
| Coefficient C | -7.50310e+01 | |||
| Temperature range, min. | 294.22 | |||
| Temperature range, max. | 370.52 | |||
| Pvap | 1.33 | kPa | 294.22 | Calculated Property |
| Pvap | 2.75 | kPa | 302.70 | Calculated Property |
| Pvap | 5.39 | kPa | 311.18 | Calculated Property |
| Pvap | 10.08 | kPa | 319.65 | Calculated Property |
| Pvap | 18.07 | kPa | 328.13 | Calculated Property |
| Pvap | 31.20 | kPa | 336.61 | Calculated Property |
| Pvap | 52.05 | kPa | 345.09 | Calculated Property |
| Pvap | 84.17 | kPa | 353.56 | Calculated Property |
| Pvap | 132.30 | kPa | 362.04 | Calculated Property |
| Pvap | 202.63 | kPa | 370.52 | Calculated Property |
| Pvap | [10.35; 101.11] | kPa | [322.15; 386.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.15692e+01 | |||
| Coefficient B | -7.27943e+03 | |||
| Coefficient C | -9.94014e+00 | |||
| Coefficient D | 7.40421e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 322.15 | |||
| Temperature range, max. | 386.15 | |||
| Pvap | 10.35 | kPa | 322.15 | Calculated Property |
| Pvap | 14.04 | kPa | 329.26 | Calculated Property |
| Pvap | 18.77 | kPa | 336.37 | Calculated Property |
| Pvap | 24.73 | kPa | 343.48 | Calculated Property |
| Pvap | 32.16 | kPa | 350.59 | Calculated Property |
| Pvap | 41.31 | kPa | 357.71 | Calculated Property |
| Pvap | 52.47 | kPa | 364.82 | Calculated Property |
| Pvap | 65.93 | kPa | 371.93 | Calculated Property |
| Pvap | 82.03 | kPa | 379.04 | Calculated Property |
| Pvap | 101.11 | kPa | 386.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclopentane, chloro-.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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