- InChI
- InChI=1S/C6H10O/c7-6-4-2-1-3-5-6/h1-5H2
- InChI Key
- JHIVVAPYMSGYDF-UHFFFAOYSA-N
- Formula
- C6H10O
- SMILES
- O=C1CCCCC1
- Molecular Weight1
- 98.14
- CAS
- 108-94-1
- Other Names
-
- ANON
- Anone
- Cicloesanone
- Cyclohexanon
- Cyclohexyl ketone
- Cykloheksanon
- HEXANON
- Hytrol O
- Ketohexamethylene
- NADONE
- NCI-C55005
- NSC 5711
- Pimelic ketone
- Pimelin ketone
- Rcra waste number U057
- Sextone
- UN 1915
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- LFL : Lower Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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).
- ΔsubH : Enthalpy of sublimation 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.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4420 | KDB | |
| PAff | 841.00 | kJ/mol | NIST |
| Tig | 693.15 | K | KDB |
| BasG | 811.20 | kJ/mol | NIST |
| ΔcH°liquid | [-3536.00; -3499.00] | kJ/mol |
|
| ΔcH°liquid | -3517.60 ± 1.70 | kJ/mol | NIST |
| ΔcH°liquid | -3536.00 ± 2.00 | kJ/mol | NIST |
| ΔcH°liquid | -3518.90 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -3499.00 ± 0.80 | kJ/mol | NIST |
| μ | 3.10 | debye | KDB |
| η | 0.0020200 | Pa×s | Densiti... |
| EA | 0.00 | eV | NIST |
| LFL | 1.10 | % in Air | KDB |
| Tflash,cc | 327.04 | K | KDB |
| Tflash,oc | 317.04 | K | KDB |
| ΔfG° | -90.81 | kJ/mol | KDB |
| Rg | 3.4100 | KDB | |
| ΔfH°gas | [-231.10; -225.70] | kJ/mol |
|
| ΔfH°gas | -230.30 | kJ/mol | KDB |
| ΔfH°gas | -231.10 ± 0.88 | kJ/mol | NIST |
| ΔfH°gas | -225.70 | kJ/mol | NIST |
| ΔfH°gas | -227.70 ± 1.90 | kJ/mol | NIST |
| ΔfH°gas | -226.30 | kJ/mol | NIST |
| ΔfH°liquid | [-276.10; -254.00] | kJ/mol |
|
| ΔfH°liquid | -276.10 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | -272.60 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | -254.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -271.40 | kJ/mol | NIST |
| ΔfusH° | 1.57 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 33.94 | kJ/mol | Joback Calculated Property |
| IE | [9.14; 9.50] | eV |
|
| IE | 9.16 ± 0.02 | eV | NIST |
| IE | 9.18 | eV | NIST |
| IE | Outlier 9.50 ± 0.20 | eV | NIST |
| IE | 9.16 ± 0.01 | eV | NIST |
| IE | 9.14 ± 0.01 | eV | NIST |
| IE | 9.14 ± 0.03 | eV | NIST |
| IE | 9.29 | eV | NIST |
| IE | 9.18 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.14 ± 0.02 | eV | NIST |
| log10WS | [-0.60; -0.60] |
|
|
| log10WS | -0.60 | Aq. Sol... | |
| log10WS | -0.60 | Estimat... | |
| logPoct/wat | 1.520 | Crippen Calculated Property | |
| McVol | 86.110 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3850.35; 4600.00] | kPa |
|
| Pc | 4000.00 | kPa | KDB |
| Pc | 4600.00 ± 100.00 | kPa | NIST |
| Pc | 4000.00 ± 50.00 | kPa | NIST |
| Pc | 3850.35 ± 202.65 | kPa | NIST |
| Inp | [139.80; 903.00] |
|
|
| Inp | 854.10 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 853.90 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 855.10 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 851.70 | NIST | |
| Inp | 896.80 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | Outlier 139.80 | NIST | |
| Inp | Outlier 139.80 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 854.10 | NIST | |
| Inp | 853.90 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 867.00 | NIST | |
| I | [1273.00; 1333.00] |
|
|
| I | 1301.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1287.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1311.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1315.00 | NIST | |
| I | 1314.00 | NIST | |
| I | 1314.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1296.00 | NIST | |
| I | Outlier 1333.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1302.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1320.00 | NIST | |
| I | 1285.00 | NIST | |
| I | 1299.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1285.00 | NIST | |
| I | 1311.00 | NIST | |
| I | 1314.00 | NIST | |
| I | 1306.00 | NIST | |
| I | 1306.00 | NIST | |
| I | 1289.00 | NIST | |
| I | 1306.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1301.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1302.00 | NIST | |
| I | 1285.00 | NIST | |
| I | 1289.00 | NIST | |
| I | 1291.00 | NIST | |
| I | 1280.00 | NIST | |
| I | 1296.00 | NIST | |
| I | 1282.00 | NIST | |
| S°gas | 335.53 | J/mol×K | NIST |
| S°liquid | 229.03 | J/mol×K | NIST |
| Tboil | [428.57; 428.84] | K |
|
| Tboil | 428.58 | K | KDB |
| Tboil | 428.69 | K | (Liquid... |
| Tboil | 428.84 | K | Excess ... |
| Tboil | 428.57 | K | Measure... |
| Tc | [629.15; 664.30] | K |
|
| Tc | 653.00 | K | KDB |
| Tc | 664.30 ± 3.00 | K | NIST |
| Tc | 653.00 ± 3.00 | K | NIST |
| Tc | 629.15 ± 1.50 | K | NIST |
| Tfus | [242.00; 245.90] | K |
|
| Tfus | 242.00 | K | KDB |
| Tfus | 245.90 | K | Vapour ... |
| Ttriple | [242.40; 245.21] | K |
|
| Ttriple | 245.21 ± 0.01 | K | NIST |
| Ttriple | 242.40 ± 0.50 | K | NIST |
| Vc | 0.312 | m3/kmol | Joback Calculated Property |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [155.20; 190.18] | J/mol×K | [385.00; 480.00] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 155 160 165 170 175 180 185 190 400 450 | ||||
| Cp,gas | 155.20 | J/mol×K | 385.00 | NIST |
| Cp,gas | 161.07 | J/mol×K | 400.00 | NIST |
| Cp,gas | 168.98 | J/mol×K | 420.00 | NIST |
| Cp,gas | 175.81 | J/mol×K | 440.00 | NIST |
| Cp,gas | 183.65 | J/mol×K | 460.00 | NIST |
| Cp,gas | 190.18 | J/mol×K | 480.00 | NIST |
| Cp,liquid | [177.20; 200.40] | J/mol×K | [290.00; 304.20] |
|
| Cp,liquid | 177.80 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 177.20 | J/mol×K | 300.00 | NIST |
| Cp,liquid | 200.40 | J/mol×K | 304.20 | NIST |
| η | [0.0013730; 0.0025990] | Pa×s | [288.15; 318.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.40e-3 1.60e-3 1.80e-3 2.00e-3 2.20e-3 2.40e-3 2.60e-3 290 300 310 | ||||
| η | 0.0025990 | Pa×s | 288.15 | Densiti... |
| η | 0.0023318 | Pa×s | 293.15 | Densiti... |
| η | 0.0020212 | Pa×s | 298.15 | Thermop... |
| η | 0.0021016 | Pa×s | 298.15 | Densiti... |
| η | 0.0020570 | Pa×s | 298.15 | Densiti... |
| η | 0.0019740 | Pa×s | 298.15 | Excess ... |
| η | 0.0020190 | Pa×s | 298.15 | Density... |
| η | 0.0018057 | Pa×s | 303.15 | Thermop... |
| η | 0.0018170 | Pa×s | 303.15 | Density... |
| η | 0.0019045 | Pa×s | 303.15 | Densiti... |
| η | 0.0018470 | Pa×s | 303.15 | Densiti... |
| η | 0.0018160 | Pa×s | 303.15 | Densiti... |
| η | 0.0017338 | Pa×s | 308.15 | Densiti... |
| η | 0.0016570 | Pa×s | 308.15 | Densiti... |
| η | 0.0015849 | Pa×s | 308.15 | Thermop... |
| η | 0.0016310 | Pa×s | 308.15 | Density... |
| η | 0.0016320 | Pa×s | 308.15 | Excess ... |
| η | 0.0016940 | Pa×s | 308.15 | Densiti... |
| η | 0.0014760 | Pa×s | 313.15 | Density... |
| η | 0.0015460 | Pa×s | 313.15 | Densiti... |
| η | 0.0015420 | Pa×s | 313.15 | Densiti... |
| η | 0.0015842 | Pa×s | 313.15 | Densiti... |
| η | 0.0013730 | Pa×s | 318.15 | Excess ... |
| ΔfusH | [1.25; 8.66] | kJ/mol | [220.80; 245.20] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 2 4 6 8 230 240 | ||||
| ΔfusH | 8.66 | kJ/mol | 220.80 | NIST |
| ΔfusH | 8.51 | kJ/mol | 221.00 | NIST |
| ΔfusH | 1.25 | kJ/mol | 242.60 | NIST |
| ΔfusH | 1.33 | kJ/mol | 245.20 | NIST |
| ΔfusH | 1.33 | kJ/mol | 245.20 | NIST |
| ΔsubH | 49.30 | kJ/mol | 254.00 | NIST |
| ΔvapH | [39.75; 45.13] | kJ/mol | [285.50; 428.80] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 40 41 42 43 44 45 300 350 400 | ||||
| ΔvapH | 40.30 | kJ/mol | 285.50 | NIST |
| ΔvapH | 44.40 ± 0.10 | kJ/mol | 308.00 | NIST |
| ΔvapH | 44.00 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 43.40 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 43.10 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 42.20 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 41.80 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 41.40 ± 0.10 | kJ/mol | 348.00 | NIST |
| ΔvapH | 44.00 | kJ/mol | 373.00 | NIST |
| ΔvapH | 43.10 | kJ/mol | 385.00 | NIST |
| ΔvapH | 41.50 | kJ/mol | 400.50 | NIST |
| ΔvapH | 42.20 | kJ/mol | 401.50 | NIST |
| ΔvapH | 40.40 | kJ/mol | 410.50 | NIST |
| ΔvapH | 39.75 | kJ/mol | 428.20 | KDB |
| ΔvapH | 45.13 | kJ/mol | 428.80 | NIST |
| Pvap | [0.64; 101.30] | kPa | [298.15; 428.57] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.64 | kPa | 298.15 | (Vapour... |
| Pvap | 1.16 | kPa | 308.15 | (Vapour... |
| Pvap | 1.92 | kPa | 318.15 | (Vapour... |
| Pvap | 95.30 | kPa | 426.25 | Excess ... |
| Pvap | 99.00 | kPa | 428.01 | Vapor-L... |
| Pvap | 101.30 | kPa | 428.57 | Measure... |
| n0 | [1.44400; 1.45100] | [293.10; 308.15] |
|
|
|
T(K) Refractive Index 1.44 1.45 1.45 1.45 1.45 1.45 1.45 1.45 295 300 305 | ||||
| n0 | 1.45070 | 293.10 | Volumet... | |
| n0 | 1.45100 | 293.15 | Activit... | |
| n0 | 1.45070 | 293.15 | Effect ... | |
| n0 | 1.45100 | 298.15 | Bubble ... | |
| n0 | 1.44820 | 298.15 | Vapour ... | |
| n0 | 1.44810 | 298.15 | Isother... | |
| n0 | 1.45010 | 298.15 | Excess ... | |
| n0 | 1.44860 | 298.15 | Density... | |
| n0 | 1.44980 | 298.15 | Solubil... | |
| n0 | 1.45030 | 298.20 | Tie-lin... | |
| n0 | 1.44610 | 303.15 | Density... | |
| n0 | 1.44400 | 308.15 | Density... | |
| ρl | [920.70; 951.69] | kg/m3 | [288.00; 323.15] |
|
|
T(K) Liquid Density (kg/m3) 920 925 930 935 940 945 950 290 300 310 320 | ||||
| ρl | 951.00 | kg/m3 | 288.00 | KDB |
| ρl | 951.18 | kg/m3 | 288.15 | Volumet... |
| ρl | 951.69 | kg/m3 | 288.15 | Densiti... |
| ρl | 947.60 | kg/m3 | 293.10 | Vapor-L... |
| ρl | 947.38 | kg/m3 | 293.15 | Thermod... |
| ρl | 946.71 | kg/m3 | 293.15 | Volumet... |
| ρl | 948.80 | kg/m3 | 293.15 | Correla... |
| ρl | 942.20 | kg/m3 | 298.15 | Excess ... |
| ρl | 942.76 | kg/m3 | 298.15 | Densiti... |
| ρl | 943.10 | kg/m3 | 298.15 | Correla... |
| ρl | 942.24 | kg/m3 | 298.15 | Volumet... |
| ρl | 942.92 | kg/m3 | 298.15 | Thermod... |
| ρl | 941.10 | kg/m3 | 298.15 | Isobari... |
| ρl | 937.55 | kg/m3 | 303.15 | Excess ... |
| ρl | 938.07 | kg/m3 | 303.15 | Thermod... |
| ρl | 938.20 | kg/m3 | 303.15 | Correla... |
| ρl | 937.77 | kg/m3 | 303.15 | Volumet... |
| ρl | 933.28 | kg/m3 | 308.15 | Volumet... |
| ρl | 933.50 | kg/m3 | 308.15 | Correla... |
| ρl | 933.19 | kg/m3 | 308.15 | Thermod... |
| ρl | 933.80 | kg/m3 | 308.15 | Densiti... |
| ρl | 928.80 | kg/m3 | 313.15 | Correla... |
| ρl | 928.79 | kg/m3 | 313.15 | Volumet... |
| ρl | 924.40 | kg/m3 | 318.15 | Correla... |
| ρl | 924.82 | kg/m3 | 318.15 | Densiti... |
| ρl | 920.70 | kg/m3 | 323.15 | Correla... |
| ΔfusS | [5.20; 39.22] | J/mol×K | [220.80; 245.20] |
|
| ΔfusS | 39.22 | J/mol×K | 220.80 | NIST |
| ΔfusS | 38.50 | J/mol×K | 221.00 | NIST |
| ΔfusS | 5.20 | J/mol×K | 242.60 | NIST |
| ΔfusS | 5.42 | J/mol×K | 245.20 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 320.20 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [315.32; 454.86] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.55797e+01 | |||
| Coefficient B | -4.36137e+03 | |||
| Coefficient C | -3.01140e+01 | |||
| Temperature range, min. | 315.32 | |||
| Temperature range, max. | 454.86 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 315.32 | Calculated Property |
| Pvap | 2.93 | kPa | 330.82 | Calculated Property |
| Pvap | 5.97 | kPa | 346.33 | Calculated Property |
| Pvap | 11.38 | kPa | 361.83 | Calculated Property |
| Pvap | 20.47 | kPa | 377.34 | Calculated Property |
| Pvap | 35.02 | kPa | 392.84 | Calculated Property |
| Pvap | 57.33 | kPa | 408.35 | Calculated Property |
| Pvap | 90.27 | kPa | 423.85 | Calculated Property |
| Pvap | 137.34 | kPa | 439.36 | Calculated Property |
| Pvap | 202.66 | kPa | 454.86 | Calculated Property |
| Pvap | [7.24e-03; 4053.12] | kPa | [242.00; 629.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.05154e+02 | |||
| Coefficient B | -8.84188e+03 | |||
| Coefficient C | -1.35148e+01 | |||
| Coefficient D | 1.08668e-05 | |||
| Temperature range, min. | 242.00 | |||
| Temperature range, max. | 629.15 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 600 | ||||
| Pvap | 7.24e-03 | kPa | 242.00 | Calculated Property |
| Pvap | 0.25 | kPa | 285.02 | Calculated Property |
| Pvap | 2.93 | kPa | 328.03 | Calculated Property |
| Pvap | 17.51 | kPa | 371.05 | Calculated Property |
| Pvap | 68.22 | kPa | 414.07 | Calculated Property |
| Pvap | 201.10 | kPa | 457.08 | Calculated Property |
| Pvap | 492.54 | kPa | 500.10 | Calculated Property |
| Pvap | 1066.76 | kPa | 543.12 | Calculated Property |
| Pvap | 2132.17 | kPa | 586.13 | Calculated Property |
| Pvap | 4053.12 | kPa | 629.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexanone.
Mixtures
- Decane + Cyclohexanone
- 2-Propenenitrile + Cyclohexanone
- Cyclohexanone + Carbon Tetrachloride
- Cyclohexanone + Cyanopyrazine
- Cyclohexanone + Cyclohexane
- Pyrazine, methyl- + Cyclohexanone
- Cyclohexanone + Ethane, 1,2-dichloro-
- Trichloromethane + Cyclohexanone
- Cyclohexanol + Cyclohexanone
- Cyclohexanone + o-Xylene
- Benzene, 1,3-dimethyl- + Cyclohexanone
- p-Xylene + Cyclohexanone
- Benzene + Cyclohexanone
- Toluene + Cyclohexanone
- Ethylbenzene + Cyclohexanone
- Styrene + Cyclohexanone
- Cyclohexanone + Propanoic acid + Water
- Cyclohexanone + Ethane, 1,1,2,2-tetrachloro-
- Dimethyl Sulfoxide + Cyclohexanone
- 2-Pyrrolidinone, 1-methyl- + Cyclohexanone
Find more mixtures with Cyclohexanone.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
- Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
- 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
- Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
- Measurement on the solubility of adipic acid in various solvents at high temperature and its thermodynamics parameters.
- Liquid-liquid equilibria for ternary system water + acetic acid+ cyclohexanone at (293.2 to 323.2) K
- Distribution of cyclohexanol and cyclohexanone between water and cyclohexane
- Solubilities of adipic acid in binary cyclohexanone + cyclohexanol, cyclohexane + cyclohexanol, and cyclohexane + cyclohexanone solvent mixtures
- Solubility of 1,1-diamino-2,2-dinitroethylene in different pure solvents and binary mixtures (dimethyl sulfoxide p water) and (N,N-dimethylformamide p water) at different temperatures
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
- Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
- Phase equilibria for ternary liquid systems of (water + levulinic acid + cyclic solvent) at T = 298.2 K: Thermodynamic modeling
- (Liquid + liquid) equilibria of (water + propionic acid + cyclohexanone) at several temperatures
- 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
- Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
- Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
- Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
- (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 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 and correlation of phase equilibrium data of the mixtures consisting of butyric acid, water, cyclohexanone at different temperatures
- Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- 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
- Excess molar volumes and excess isentropic compressibilities of mixtures containing lactam, cyclic ethers and cyclic alkanones
- Enthalpic interactions between some amino acids and cyclohexanone in aqueous solutions at 298.15K
- Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
- Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures
- Measurement and Correlation for Solubilities of Adipic Acid in Acetic Acid + e-Caprolactone Mixtures and Cyclohexanone + e-Caprolactone Mixtures
- Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
- Determination and Correlation for the Solubility of Glutaric Acid in Cyclohexane + Cyclohexanol + Cyclohexanone Solvent Mixtures
- Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
- Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
- Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid and Succinic Acid in Acetic Acid + Cyclohexanone Mixtures
- Isobaric Vapor Liquid Equilibrium for Binary Systems of Cyclohexanone + Benzene, Cyclohexanone + Toluene, and Cyclohexanone + p-Xylene at 101.3 kPa
- Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid, and Succinic Acid in Dimethyl Adipate + Methanol Mixtures
- Experimental Determination and Correlation of Liquid Liquid Equilibria for Water + Cyclohexanone + Solvents (Toluene or p-Xylene) Ternary Systems at 303.15 and 323.15 K under 101.3 kPa
- Measurement and Correlation for the Solubility of Adipic Acid and Succinic Acid in Glutaric Acid + Cyclohexanone and Glutaric Acid + Acetic Acid Mixtures
- Liquid-Liquid Equilibrium in the Ternary Systems Water + Cyclohexanone + Benzene or Methyl Isobutyl Carbinol at 303.15 and 323.15 K: Experimental Data and Correlation
- Measurement and Correlation for Solubilities of Succinic Acid and Glutaric Acid in e-Caprolactone + Acetic Acid Mixtures and e-Caprolactone + Cyclohexanone Mixtures
- Measurement and Correlation of Ternary (Liquid + Liquid) Equilibria for Separation of Cyclohexanone from Water via Isophorone or Mesityl Oxide
- Determination and Correlation for the Solubilities of Succinic Acid in Cyclohexanol + Cyclohexanone + Cyclohexane Solvent Mixtures
- Isobaric Vapor-Liquid Phase Equilibrium Measurements, Correlation, and Prediction for Separation of the Mixtures of Cyclohexanone and Alcohols
- Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
- Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
- Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
- Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
- Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
- Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
- Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
- Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
- Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
- Thermodynamic Properties for 2-(1'-Hydroxycyclohexyl)cyclohexanone and Equilibrium of Dimerization of Cyclohexanone
- Excess Molar Volumes and Viscosities for Binary Mixtures of Cyclohexanone with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
- Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
- Vapor-Liquid Equilibrium Measurements and Modeling for Cyclohexane + Cyclohexanone
- Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Different Organic Solvents
- Gas Solubility in Binary Liquid Mixtures: Carbon Dioxide in Cyclohexane + Cyclohexanone
- Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
- Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
- Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
- Solubility of 6-Chloropyridazin-3-amine in Different Solvents
- Measurements and Correlation of Liquid Liquid Equilibria for the Ternary System Water + Cyclohexanol + Cyclohexanone
- Vapor-Liquid Equilibria of Cyclohexanone + 2-Cyclohexen-1-one and Cyclohexanol + 2-Cyclohexen-1-one, Validated in a Packed Column Distillation.
- Solid-Liquid Equilibrium and Activity Coefficients for Caprolactam + 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide and Cyclohexanone Oxime + 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide
- Solubility of Cyclotrimethylenetrinitramine (RDX) in Binary Solvent Mixtures
- Phase Behavior of the Reactant and Products of Cyclohexane Oxidation in Compressed CO2
- Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
- Solubilities of Terephthalic Acid, Phthalic Acid, and Isophthalic Acid in Tetrahydrofuran, Cyclohexanone, 1,2-Diethoxyethane, and Acetophenone
- Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
- (Liquid + Liquid) Equilibria of (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanone) and (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanol) at T = 303.2 K
- Solubility of 1,1'-(Ethane-1,2-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents
- Solubilities of 1,1?-(Propane-1,3-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Different Solvents
- Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Water, Acetophenone, Cyclohexanone, Acetylacetone, and 2-Butanone
- Solubility of Anthracene in Binary and Ternary Mixtures of Cyclohexanone, Ethyl Acetate, and Methanol at 298.2 K
- Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents from (288.15 to 333.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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