- InChI
- InChI=1S/C5H8O/c6-5-3-1-2-4-5/h1-4H2
- InChI Key
- BGTOWKSIORTVQH-UHFFFAOYSA-N
- Formula
- C5H8O
- SMILES
- O=C1CCCC1
- Molecular Weight1
- 84.12
- CAS
- 120-92-3
- Other Names
-
- ADIPIC KETONE
- Adipinketon
- DUMASIN
- KETOCYCLOPENTANE
- Ketopentamethylene
- NSC 4122
- UN 2245
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- 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.
- γ : Surface Tension (N/m).
- 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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3500 | KDB | |
| PAff | [823.70; 828.00] | kJ/mol |
|
| PAff | 823.70 | kJ/mol | NIST |
| PAff | 828.00 ± 4.00 | kJ/mol | NIST |
| BasG | 794.00 | kJ/mol | NIST |
| ΔcH°liquid | [-2874.00; -2870.00] | kJ/mol |
|
| ΔcH°liquid | -2873.50 ± 1.60 | kJ/mol | NIST |
| ΔcH°liquid | -2874.00 ± 0.92 | kJ/mol | NIST |
| ΔcH°liquid | -2870.00 ± 0.80 | kJ/mol | NIST |
| μ | 3.00 | debye | KDB |
| EA | 0.00 | eV | NIST |
| ΔfG° | -87.11 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-197.40; -192.80] | kJ/mol |
|
| ΔfH°gas | -192.80 | kJ/mol | KDB |
| ΔfH°gas | -197.40 ± 1.30 | kJ/mol | NIST |
| ΔfH°gas | -194.80 ± 1.70 | kJ/mol | NIST |
| ΔfH°gas | -193.00 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | [-240.20; -236.50] | kJ/mol |
|
| ΔfH°liquid | -240.20 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -237.40 ± 1.70 | kJ/mol | NIST |
| ΔfH°liquid | -236.50 | kJ/mol | NIST |
| ΔfusH° | 1.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [42.10; 42.77] | kJ/mol |
|
| ΔvapH° | 42.77 | kJ/mol | NIST |
| ΔvapH° | Outlier 42.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 42.63 ± 0.42 | kJ/mol | NIST |
| ΔvapH° | 42.60 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 42.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.72 | kJ/mol | NIST |
| IE | [9.10; 9.42] | eV |
|
| IE | 9.26 ± 0.01 | eV | NIST |
| IE | 9.28 ± 0.01 | eV | NIST |
| IE | 9.25 ± 0.02 | eV | NIST |
| IE | 9.26 ± 0.01 | eV | NIST |
| IE | Outlier 9.42 ± 0.03 | eV | NIST |
| IE | 9.30 | eV | NIST |
| IE | Outlier 9.10 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.25 ± 0.02 | eV | NIST |
| log10WS | -1.09 | Crippen Calculated Property | |
| logPoct/wat | 1.129 | Crippen Calculated Property | |
| McVol | 72.020 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [4600.00; 4600.00] | kPa |
|
| Pc | 4600.00 | kPa | KDB |
| Pc | 4600.00 ± 50.00 | kPa | NIST |
| Inp | [116.00; 811.00] |
|
|
| Inp | 741.10 | NIST | |
| Inp | 740.90 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 749.60 | NIST | |
| Inp | 793.80 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 761.10 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | Outlier 116.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | Outlier 116.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 754.00 | NIST | |
| I | [1142.00; 1211.70] |
|
|
| I | 1176.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1150.00 | NIST | |
| I | 1164.00 | NIST | |
| I | 1211.70 | NIST | |
| I | 1200.00 | NIST | |
| I | 1203.10 | NIST | |
| I | 1200.00 | NIST | |
| I | 1206.30 | NIST | |
| I | 1166.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1154.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1170.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1154.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1167.00 | NIST | |
| I | 1167.00 | NIST | |
| I | 1168.00 | NIST | |
| I | 1168.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1211.70 | NIST | |
| I | 1166.00 | NIST | |
| I | 1154.00 | NIST | |
| I | 1168.00 | NIST | |
| Tboil | 403.72 | K | KDB |
| Tc | [624.50; 624.50] | K |
|
| Tc | 624.50 | K | KDB |
| Tc | 624.50 ± 2.00 | K | NIST |
| Tfus | [220.05; 222.60] | K |
|
| Tfus | 221.80 | K | KDB |
| Tfus | 221.70 ± 0.30 | K | NIST |
| Tfus | Outlier 220.05 ± 0.50 | K | NIST |
| Tfus | 222.60 ± 0.60 | K | NIST |
| Tfus | 221.85 ± 0.40 | K | NIST |
| Tfus | 221.85 ± 0.50 | K | NIST |
| Ttriple | [220.77; 221.44] | K |
|
| Ttriple | 220.77 | K | Thermod... |
| Ttriple | 221.44 ± 0.02 | K | NIST |
| Vc | 0.268 | m3/kmol | KDB |
| Zc | 0.2374230 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [116.90; 149.22] | J/mol×K | [360.00; 480.00] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 115 120 125 130 135 140 145 150 400 450 | ||||
| Cp,gas | 116.90 | J/mol×K | 360.00 | NIST |
| Cp,gas | 121.16 | J/mol×K | 375.00 | NIST |
| Cp,gas | 128.03 | J/mol×K | 400.00 | NIST |
| Cp,gas | 133.86 | J/mol×K | 420.00 | NIST |
| Cp,gas | 139.31 | J/mol×K | 440.00 | NIST |
| Cp,gas | 144.04 | J/mol×K | 460.00 | NIST |
| Cp,gas | 149.22 | J/mol×K | 480.00 | NIST |
| η | [0.0008610; 0.0010840] | Pa×s | [298.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 8.50e-4 9.00e-4 9.50e-4 1.00e-3 1.05e-3 1.10e-3 300 305 310 | ||||
| η | 0.0010840 | Pa×s | 298.15 | Density... |
| η | 0.0009990 | Pa×s | 303.15 | Densiti... |
| η | 0.0009980 | Pa×s | 303.15 | Density... |
| η | 0.0009270 | Pa×s | 308.15 | Densiti... |
| η | 0.0009230 | Pa×s | 308.15 | Density... |
| η | 0.0008650 | Pa×s | 313.15 | Densiti... |
| η | 0.0008610 | Pa×s | 313.15 | Density... |
| ΔfusH | [11.40; 11.40] | kJ/mol | [221.20; 221.20] |
|
| ΔfusH | 11.40 | kJ/mol | 221.20 | NIST |
| ΔfusH | 11.40 | kJ/mol | 221.20 | NIST |
| ΔvapH | [36.35; 43.60] | kJ/mol | [286.00; 403.70] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36 38 40 42 44 300 350 400 | ||||
| ΔvapH | 43.60 | kJ/mol | 286.00 | NIST |
| ΔvapH | 42.60 | kJ/mol | 348.50 | NIST |
| ΔvapH | 41.50 | kJ/mol | 363.00 | NIST |
| ΔvapH | 40.60 | kJ/mol | 372.00 | NIST |
| ΔvapH | 39.60 | kJ/mol | 377.00 | NIST |
| ΔvapH | 36.35 | kJ/mol | 403.70 | NIST |
| n0 | [1.43470; 1.43490] | [298.15; 298.15] |
|
|
| n0 | 1.43470 | 298.15 | Vapour ... | |
| n0 | 1.43470 | 298.15 | Isother... | |
| n0 | 1.43490 | 298.15 | Isother... | |
| n0 | 1.43470 | 298.15 | Isother... | |
| ρl | [924.99; 969.10] | kg/m3 | [273.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 930 940 950 960 970 280 290 300 310 | ||||
| ρl | 969.10 | kg/m3 | 273.15 | Phase e... |
| ρl | 964.30 | kg/m3 | 278.15 | Phase e... |
| ρl | 959.50 | kg/m3 | 283.15 | Phase e... |
| ρl | 954.70 | kg/m3 | 288.15 | Phase e... |
| ρl | 953.99 | kg/m3 | 288.15 | Densiti... |
| ρl | 950.00 | kg/m3 | 293.00 | KDB |
| ρl | 949.90 | kg/m3 | 293.15 | Phase e... |
| ρl | 945.00 | kg/m3 | 298.15 | Phase e... |
| ρl | 944.30 | kg/m3 | 298.15 | Excess ... |
| ρl | 944.35 | kg/m3 | 298.15 | Densiti... |
| ρl | 934.69 | kg/m3 | 308.15 | Densiti... |
| ρl | 924.99 | kg/m3 | 318.15 | Densiti... |
| γ | 0.03 | N/m | 298.15 | Concent... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [298.15; 429.12] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54060e+01 | |||
| Coefficient B | -3.97854e+03 | |||
| Coefficient C | -3.49970e+01 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 429.12 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 298.15 | Calculated Property |
| Pvap | 2.94 | kPa | 312.70 | Calculated Property |
| Pvap | 6.01 | kPa | 327.25 | Calculated Property |
| Pvap | 11.46 | kPa | 341.81 | Calculated Property |
| Pvap | 20.61 | kPa | 356.36 | Calculated Property |
| Pvap | 35.24 | kPa | 370.91 | Calculated Property |
| Pvap | 57.62 | kPa | 385.46 | Calculated Property |
| Pvap | 90.60 | kPa | 400.02 | Calculated Property |
| Pvap | 137.60 | kPa | 414.57 | Calculated Property |
| Pvap | 202.63 | kPa | 429.12 | Calculated Property |
| Pvap | [2.80e-03; 5798.48] | kPa | [221.85; 626.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.04761e+02 | |||
| Coefficient B | -8.53493e+03 | |||
| Coefficient C | -1.34566e+01 | |||
| Coefficient D | 1.06922e-05 | |||
| Temperature range, min. | 221.85 | |||
| Temperature range, max. | 626.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 600 | ||||
| Pvap | 2.80e-03 | kPa | 221.85 | Calculated Property |
| Pvap | 0.19 | kPa | 266.76 | Calculated Property |
| Pvap | 3.15 | kPa | 311.66 | Calculated Property |
| Pvap | 22.34 | kPa | 356.57 | Calculated Property |
| Pvap | 94.75 | kPa | 401.47 | Calculated Property |
| Pvap | 290.11 | kPa | 446.38 | Calculated Property |
| Pvap | 719.30 | kPa | 491.28 | Calculated Property |
| Pvap | 1555.53 | kPa | 536.19 | Calculated Property |
| Pvap | 3083.56 | kPa | 581.09 | Calculated Property |
| Pvap | 5798.48 | kPa | 626.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclopentanone.
Mixtures
- Trichloromethane + Cyclopentanone
- 2-Pyrrolidinone, 1-methyl- + Cyclopentanone
- Ethane, 1,2-dichloro- + Cyclopentanone
- Ethane, 1,1,1-trichloro- + Cyclopentanone
- Cyclopentanone + Ethane, 1,1,2,2-tetrachloro-
- Butane, 1-chloro- + Cyclopentanone
- Cyclopentanone + Propane, 1,3-dichloro-
- Butane, 1,4-dichloro- + Cyclopentanone
- Cyclopentanone + Nonane
- 1-Octanol + Cyclopentanone
- Benzenesulfonamide + Cyclopentanone
- Benzenesulfonamide, 2-methyl- + Cyclopentanone
- Cyclopentanone + Water
- Ethanedioic acid, diethyl ester + Cyclopentanone
- Acetic acid, butyl ester + Cyclopentanone
- Betaine + Pentanoic acid, 4-oxo- + Cyclopentanone
- Choline chloride + Urea + Cyclopentanone
- Choline chloride + 1,2-Ethanediol + Cyclopentanone
- Cyclopentanone + Cyclohexane, methyl- + Water
- n-Propyl acetate + Cyclopentanone + Water
Find more mixtures with Cyclopentanone.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
- Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
- Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
- Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
- (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
- Isothermal (vapour + liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15) K
- Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K
- Partial molar volumes of organic solutes in water. XXIII. Cyclic ketones at T = (298 to 573) K and pressures up to 30 MPa
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Excess molar enthalpies for binary mixtures of cyclopentanone, cyclohexanone, or cycloheptanone with n-nonane at T = 298.15 K and atmospheric pressure
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- Thermodynamic properties of ternary mixtures containing 1-ethyl-3-methylimidazolium tetrafluoroborate with cyclic amides and cyclopentanone or cyclohexanone at T = (293.15, 298.15, 303.15 and 308.15) K
- Excess molar volumes and excess isentropic compressibilities of ternary mixtures containing ionic liquids and cyclic alkanone
- Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
- Liquid-Liquid Extraction of Cyclopentanone from Aqueous Solution with Methylcyclohexane or Propyl Acetate at Different Temperatures
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
- Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
- Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
- Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
- Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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