- InChI
- InChI=1S/C5H10O/c6-5-3-1-2-4-5/h5-6H,1-4H2
- InChI Key
- XCIXKGXIYUWCLL-UHFFFAOYSA-N
- Formula
- C5H10O
- SMILES
- OC1CCCC1
- Molecular Weight1
- 86.13
- CAS
- 96-41-3
- Other Names
-
- CYCOLPENTYL ALCOHOL
- Cyclopentyl alcohol
- HYDROXYCYCLOPENTANE
- UN 2244
- PAff : Proton affinity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- 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).
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (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 |
|---|---|---|---|
| PAff | 798.00 ± 6.00 | kJ/mol | NIST |
| ΔcH°liquid | [-3096.70; -3096.50] | kJ/mol |
|
| ΔcH°liquid | -3096.70 ± 1.70 | kJ/mol | NIST |
| ΔcH°liquid | -3096.50 ± 1.50 | kJ/mol | NIST |
| ΔfG° | -109.05 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-243.00; -242.60] | kJ/mol |
|
| ΔfH°gas | -243.00 | kJ/mol | NIST |
| ΔfH°gas | -242.60 ± 1.70 | kJ/mol | NIST |
| ΔfH°gas | -242.90 | kJ/mol | NIST |
| ΔfH°liquid | [-300.40; -300.00] | kJ/mol |
|
| ΔfH°liquid | -300.40 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -300.00 ± 1.70 | kJ/mol | NIST |
| ΔfH°liquid | -300.30 ± 0.20 | kJ/mol | NIST |
| ΔfusH° | 6.73 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [56.10; 57.63] | kJ/mol |
|
| ΔvapH° | 57.63 | kJ/mol | NIST |
| ΔvapH° | 57.10 | kJ/mol | NIST |
| ΔvapH° | 56.10 | kJ/mol | NIST |
| ΔvapH° | 56.40 | kJ/mol | NIST |
| ΔvapH° | 57.50 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 57.50 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 57.49 | kJ/mol | NIST |
| ΔvapH° | 57.40 | kJ/mol | NIST |
| IE | [9.58; 9.72] | eV |
|
| IE | 9.72 | eV | NIST |
| IE | 9.58 ± 0.06 | eV | NIST |
| log10WS | -1.19 | Crippen Calculated Property | |
| logPoct/wat | 0.921 | Crippen Calculated Property | |
| McVol | 76.320 | ml/mol | McGowan Calculated Property |
| Pc | [4900.00; 4900.00] | kPa |
|
| Pc | 4900.00 | kPa | KDB |
| Pc | 4900.00 ± 100.00 | kPa | NIST |
| Pc | 4900.00 ± 100.00 | kPa | NIST |
| Inp | [765.00; 805.00] |
|
|
| Inp | 792.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 805.00 | NIST | |
| I | [1278.00; 1339.00] |
|
|
| I | 1298.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1300.00 | NIST | |
| I | 1314.00 | NIST | |
| I | 1314.00 | NIST | |
| I | 1309.00 | NIST | |
| I | 1323.00 | NIST | |
| I | 1278.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1328.00 | NIST | |
| I | 1300.00 | NIST | |
| I | 1290.00 | NIST | |
| I | 1303.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1289.00 | NIST | |
| I | 1292.00 | NIST | |
| I | 1289.00 | NIST | |
| I | 1292.00 | NIST | |
| I | 1323.00 | NIST | |
| I | Outlier 1339.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1283.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1297.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1323.00 | NIST | |
| I | 1297.00 | NIST | |
| I | 1300.00 | NIST | |
| I | 1278.00 | NIST | |
| S°liquid | 206.30 | J/mol×K | NIST |
| Tboil | [412.50; 413.57] | K |
|
| Tboil | 413.57 | K | KDB |
| Tboil | 412.50 | K | Solubil... |
| Tboil | 413.38 | K | A New T... |
| Tc | [619.50; 620.00] | K |
|
| Tc | 619.50 | K | KDB |
| Tc | 620.00 ± 1.00 | K | NIST |
| Tc | 619.50 ± 1.00 | K | NIST |
| Tfus | [253.00; 254.15] | K |
|
| Tfus | 254.00 | K | KDB |
| Tfus | 254.15 ± 1.00 | K | NIST |
| Tfus | 253.00 ± 2.00 | K | NIST |
| Ttriple | [255.60; 257.40] | K |
|
| Ttriple | 255.60 ± 0.30 | K | NIST |
| Ttriple | 256.00 ± 0.50 | K | NIST |
| Ttriple | 257.40 ± 0.20 | K | NIST |
| Vc | 0.276 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [149.90; 207.53] | J/mol×K | [421.26; 610.59] |
|
| Cp,gas | 149.90 | J/mol×K | 421.26 | Joback Calculated Property |
| Cp,gas | 160.80 | J/mol×K | 452.81 | Joback Calculated Property |
| Cp,gas | 171.16 | J/mol×K | 484.37 | Joback Calculated Property |
| Cp,gas | 181.00 | J/mol×K | 515.92 | Joback Calculated Property |
| Cp,gas | 190.32 | J/mol×K | 547.48 | Joback Calculated Property |
| Cp,gas | 199.16 | J/mol×K | 579.03 | Joback Calculated Property |
| Cp,gas | 207.53 | J/mol×K | 610.59 | Joback Calculated Property |
| Cp,liquid | [157.60; 234.10] | J/mol×K | [265.06; 357.78] |
|
| Cp,liquid | 157.60 | J/mol×K | 265.06 | Heat ca... |
| Cp,liquid | 157.60 | J/mol×K | 265.06 | Heat ca... |
| Cp,liquid | 160.70 | J/mol×K | 270.00 | Heat ca... |
| Cp,liquid | 160.70 | J/mol×K | 270.00 | Heat ca... |
| Cp,liquid | 164.20 | J/mol×K | 275.00 | Heat ca... |
| Cp,liquid | 164.20 | J/mol×K | 275.00 | Heat ca... |
| Cp,liquid | 167.80 | J/mol×K | 280.00 | Heat ca... |
| Cp,liquid | 167.90 | J/mol×K | 280.00 | Heat ca... |
| Cp,liquid | 171.70 | J/mol×K | 285.00 | Heat ca... |
| Cp,liquid | 171.60 | J/mol×K | 285.00 | Heat ca... |
| Cp,liquid | 175.70 | J/mol×K | 290.00 | Heat ca... |
| Cp,liquid | 175.90 | J/mol×K | 290.00 | Heat ca... |
| Cp,liquid | 180.00 | J/mol×K | 295.00 | Heat ca... |
| Cp,liquid | 180.10 | J/mol×K | 295.00 | Heat ca... |
| Cp,liquid | 185.40 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 181.57 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 184.14 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 181.57 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 184.30 | J/mol×K | 300.00 | Heat ca... |
| Cp,liquid | 184.40 | J/mol×K | 300.00 | Heat ca... |
| Cp,liquid | 188.60 | J/mol×K | 305.00 | Heat ca... |
| Cp,liquid | 188.70 | J/mol×K | 305.00 | Heat ca... |
| Cp,liquid | 193.10 | J/mol×K | 310.00 | Heat ca... |
| Cp,liquid | 193.00 | J/mol×K | 310.00 | Heat ca... |
| Cp,liquid | 197.40 | J/mol×K | 315.00 | Heat ca... |
| Cp,liquid | 197.60 | J/mol×K | 315.00 | Heat ca... |
| Cp,liquid | 201.80 | J/mol×K | 320.00 | Heat ca... |
| Cp,liquid | 202.00 | J/mol×K | 320.00 | Heat ca... |
| Cp,liquid | 206.20 | J/mol×K | 325.00 | Heat ca... |
| Cp,liquid | 206.40 | J/mol×K | 325.00 | Heat ca... |
| Cp,liquid | 210.70 | J/mol×K | 330.00 | Heat ca... |
| Cp,liquid | 210.50 | J/mol×K | 330.00 | Heat ca... |
| Cp,liquid | 215.00 | J/mol×K | 335.00 | Heat ca... |
| Cp,liquid | 215.10 | J/mol×K | 335.00 | Heat ca... |
| Cp,liquid | 219.50 | J/mol×K | 340.00 | Heat ca... |
| Cp,liquid | 219.50 | J/mol×K | 340.00 | Heat ca... |
| Cp,liquid | 223.70 | J/mol×K | 345.00 | Heat ca... |
| Cp,liquid | 223.80 | J/mol×K | 345.00 | Heat ca... |
| Cp,liquid | 228.00 | J/mol×K | 350.00 | Heat ca... |
| Cp,liquid | 228.10 | J/mol×K | 350.00 | Heat ca... |
| Cp,liquid | 232.00 | J/mol×K | 354.91 | Heat ca... |
| Cp,liquid | 232.00 | J/mol×K | 355.00 | Heat ca... |
| Cp,liquid | 234.10 | J/mol×K | 357.78 | Heat ca... |
| η | [0.0003291; 0.0690807] | Pa×s | [217.83; 421.26] |
|
| η | 0.0690807 | Pa×s | 217.83 | Joback Calculated Property |
| η | 0.0155505 | Pa×s | 251.73 | Joback Calculated Property |
| η | 0.0049874 | Pa×s | 285.64 | Joback Calculated Property |
| η | 0.0020361 | Pa×s | 319.54 | Joback Calculated Property |
| η | 0.0009871 | Pa×s | 353.45 | Joback Calculated Property |
| η | 0.0005432 | Pa×s | 387.36 | Joback Calculated Property |
| η | 0.0003291 | Pa×s | 421.26 | Joback Calculated Property |
| ΔfusH | [1.54; 3.71] | kJ/mol | [202.80; 257.40] |
|
| ΔfusH | 3.71 | kJ/mol | 202.80 | NIST |
| ΔfusH | 1.54 | kJ/mol | 257.40 | NIST |
| ΔfusH | 1.54 | kJ/mol | 257.40 | NIST |
| ΔvapH | [52.70; 57.10] | kJ/mol | [296.50; 391.50] |
|
| ΔvapH | 57.10 | kJ/mol | 296.50 | NIST |
| ΔvapH | 52.70 | kJ/mol | 391.50 | NIST |
| Pvap | [0.06; 0.93] | kPa | [279.84; 314.30] |
|
| Pvap | 0.06 | kPa | 279.84 | Vapor P... |
| Pvap | 0.08 | kPa | 281.97 | Vapor P... |
| Pvap | 0.09 | kPa | 284.15 | Vapor P... |
| Pvap | 0.14 | kPa | 289.03 | Vapor P... |
| Pvap | 0.15 | kPa | 289.76 | Vapor P... |
| Pvap | 0.20 | kPa | 293.47 | Vapor P... |
| Pvap | 0.22 | kPa | 294.55 | Vapor P... |
| Pvap | 0.29 | kPa | 298.19 | Vapor P... |
| Pvap | 0.31 | kPa | 298.87 | Vapor P... |
| Pvap | 0.47 | kPa | 304.53 | Vapor P... |
| Pvap | 0.55 | kPa | 306.93 | Vapor P... |
| Pvap | 0.74 | kPa | 311.04 | Vapor P... |
| Pvap | 0.93 | kPa | 314.30 | Vapor P... |
| n0 | 1.45120 | 298.15 | Molar h... | |
| ρl | [904.99; 948.70] | kg/m3 | [293.15; 343.15] |
|
| ρl | 947.04 | kg/m3 | 293.15 | Density... |
| ρl | 946.99 | kg/m3 | 293.15 | Densiti... |
| ρl | 948.70 | kg/m3 | 293.15 | Correla... |
| ρl | 943.05 | kg/m3 | 298.15 | Densiti... |
| ρl | 943.08 | kg/m3 | 298.15 | Density... |
| ρl | 939.05 | kg/m3 | 303.15 | Densiti... |
| ρl | 939.08 | kg/m3 | 303.15 | Density... |
| ρl | 935.03 | kg/m3 | 308.15 | Density... |
| ρl | 935.01 | kg/m3 | 308.15 | Densiti... |
| ρl | 930.91 | kg/m3 | 313.15 | Densiti... |
| ρl | 930.92 | kg/m3 | 313.15 | Density... |
| ρl | 926.76 | kg/m3 | 318.15 | Density... |
| ρl | 926.75 | kg/m3 | 318.15 | Densiti... |
| ρl | 922.53 | kg/m3 | 323.15 | Density... |
| ρl | 922.53 | kg/m3 | 323.15 | Densiti... |
| ρl | 918.24 | kg/m3 | 328.15 | Density... |
| ρl | 918.24 | kg/m3 | 328.15 | Densiti... |
| ρl | 913.89 | kg/m3 | 333.15 | Density... |
| ρl | 913.89 | kg/m3 | 333.15 | Densiti... |
| ρl | 909.48 | kg/m3 | 338.15 | Densiti... |
| ρl | 904.99 | kg/m3 | 343.15 | Densiti... |
| ΔfusS | [5.98; 18.28] | J/mol×K | [202.80; 257.40] |
|
| ΔfusS | 18.28 | J/mol×K | 202.80 | NIST |
| ΔfusS | 5.98 | J/mol×K | 257.40 | NIST |
| csound,fluid | 1435.11 | m/s | 298.15 | Study o... |
| γ | 0.03 | N/m | 298.15 | Concent... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [326.43; 413.60] | K | [2.00; 102.00] |
|
| Tboil | 326.43 | K | 2.00 | A New T... |
| Tboil | 355.30 | K | 10.00 | A New T... |
| Tboil | 370.27 | K | 20.00 | A New T... |
| Tboil | 398.02 | K | 60.00 | A New T... |
| Tboil | 403.40 | K | 71.47 | Measure... |
| Tboil | 406.20 | K | 78.36 | Measure... |
| Tboil | 408.60 | K | 85.50 | Measure... |
| Tboil | 409.40 | K | 89.49 | Measure... |
| Tboil | 413.60 | K | 102.00 | Measure... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [319.85; 434.54] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.66115e+01 | |||
| Coefficient B | -4.21086e+03 | |||
| Coefficient C | -6.18960e+01 | |||
| Temperature range, min. | 319.85 | |||
| Temperature range, max. | 434.54 | |||
| Pvap | 1.33 | kPa | 319.85 | Calculated Property |
| Pvap | 2.87 | kPa | 332.59 | Calculated Property |
| Pvap | 5.79 | kPa | 345.34 | Calculated Property |
| Pvap | 10.96 | kPa | 358.08 | Calculated Property |
| Pvap | 19.71 | kPa | 370.82 | Calculated Property |
| Pvap | 33.82 | kPa | 383.57 | Calculated Property |
| Pvap | 55.69 | kPa | 396.31 | Calculated Property |
| Pvap | 88.41 | kPa | 409.05 | Calculated Property |
| Pvap | 135.84 | kPa | 421.80 | Calculated Property |
| Pvap | 202.67 | kPa | 434.54 | Calculated Property |
| Pvap | [0.29; 101.95] | kPa | [298.15; 414.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.23026e+01 | |||
| Coefficient B | -9.37555e+03 | |||
| Coefficient C | -1.10220e+01 | |||
| Coefficient D | 8.05060e-06 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 414.15 | |||
| Pvap | 0.29 | kPa | 298.15 | Calculated Property |
| Pvap | 0.72 | kPa | 311.04 | Calculated Property |
| Pvap | 1.63 | kPa | 323.93 | Calculated Property |
| Pvap | 3.45 | kPa | 336.82 | Calculated Property |
| Pvap | 6.83 | kPa | 349.71 | Calculated Property |
| Pvap | 12.79 | kPa | 362.59 | Calculated Property |
| Pvap | 22.82 | kPa | 375.48 | Calculated Property |
| Pvap | 39.01 | kPa | 388.37 | Calculated Property |
| Pvap | 64.15 | kPa | 401.26 | Calculated Property |
| Pvap | 101.95 | kPa | 414.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclopentanol.
Mixtures
- Methyl Isobutyl Ketone + Cyclopentanol + Water
- Cyclopentanol + Ethyl Acetate + Water
- Cyclopentanol + Furfural + Water
- Cyclopentanol + 1-Butanol + Water
- Cyclopentanol + Water
- Cyclopentanol + Propanoic acid + Water
- Cyclopentanol + Cyclopentane,methoxy-
- Cyclohexanol + Cyclopentanol
- Cyclopentanol + Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans-
- Cyclopentanol + Cyclohexane, methyl-
- Cyclopentanol + 4,7-Methano-1H-indene, octahydro-
- Cyclopentanol + Adamantane, 1,3-dimethyl-
- Cyclopentanol + Adamantane, 1,3-dimethyl- + 4,7-Methano-1H-indene, octahydro-
- Cyclopentanol + Carbon dioxide
- Propane + Cyclopentanol
- Cyclopentanol + 1-Propanol, 2-methyl- + Water
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
- Molar heat capacities for (2-methyl-2-butanol + heptane) mixtures and cyclopentanol at temperatures from (284 to 353) K
- Heat capacities of selected cycloalcohols
- Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
- Correlation of Experimental Liquid Liquid Equilibrium Data for Ternary Systems Using NRTL and GMDH-Type Neural Network
- Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
- A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
- Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
- Liquid-Liquid Extraction of Biobased Isobutanol from an Aqueous Solution
- Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
- Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
- Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of Pentan-1-ol, 2-Methyl-2-butanol, and Cyclopentanol in the Pressure Range from (0.1 to 100) MPa and Temperature from (293 to 318) K
- High-Pressure Vapor-Liquid Equilibrium Data for (Carbon Dioxide + Cyclopentanol) and (Propane + Cyclopentanol)
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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