- InChI
- InChI=1S/C6H10/c1-2-4-6-5-3-1/h1-2H,3-6H2
- InChI Key
- HGCIXCUEYOPUTN-UHFFFAOYSA-N
- Formula
- C6H10
- SMILES
- C1=CCCCC1
- Molecular Weight1
- 82.14
- CAS
- 110-83-8
- Other Names
-
- 1,2,3,4-TETRAHYDROBENZENE
- 1-Cyclohexene
- BENZENETETRAHYDRIDE
- Benzene tetrahydride
- Benzene, tetrahydro-
- Cyclohex-1-ene
- Cykloheksen
- Hexanaphthylene
- NSC 24835
- TETRAHYDROBENZENE
- UN 2256
- 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).
- 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).
- 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).
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×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 | 784.50 | kJ/mol | NIST |
| BasG | 752.00 | kJ/mol | NIST |
| ΔcH°liquid | [-3761.00; -3751.50] | kJ/mol |
|
| ΔcH°liquid | -3752.39 ± 0.49 | kJ/mol | NIST |
| ΔcH°liquid | -3752.00 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | -3751.50 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | -3761.00 | kJ/mol | NIST |
| ΔfG° | 61.76 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-7.10; -4.32] | kJ/mol |
|
| ΔfH°gas | -4.32 ± 0.98 | kJ/mol | NIST |
| ΔfH°gas | -4.70 | kJ/mol | NIST |
| ΔfH°gas | -5.30 | kJ/mol | NIST |
| ΔfH°gas | -7.10 | kJ/mol | NIST |
| ΔfH°liquid | [-40.60; -37.80] | kJ/mol |
|
| ΔfH°liquid | -37.80 ± 8.20 | kJ/mol | NIST |
| ΔfH°liquid | -38.20 ± 0.59 | kJ/mol | NIST |
| ΔfH°liquid | -38.80 ± 0.59 | kJ/mol | NIST |
| ΔfH°liquid | -40.60 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 3.28 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.50; 33.57] | kJ/mol |
|
| ΔvapH° | 33.57 | kJ/mol | NIST |
| ΔvapH° | 33.50 ± 0.53 | kJ/mol | NIST |
| ΔvapH° | 33.50 | kJ/mol | NIST |
| ΔvapH° | 33.50 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 30.50 ± 0.30 | kJ/mol | NIST |
| IE | [8.92; 9.57] | eV |
|
| IE | 8.95 ± 0.01 | eV | NIST |
| IE | 8.94 | eV | NIST |
| IE | 8.94 ± 0.02 | eV | NIST |
| IE | 8.95 | eV | NIST |
| IE | 8.94 ± 0.01 | eV | NIST |
| IE | Outlier 9.57 ± 0.05 | eV | NIST |
| IE | 8.99 | eV | NIST |
| IE | 8.92 | eV | NIST |
| IE | 8.95 ± 0.01 | eV | NIST |
| IE | 8.94 | eV | NIST |
| IE | 8.92 ± 0.02 | eV | NIST |
| IE | 8.95 ± 0.01 | eV | NIST |
| IE | 9.09 | eV | NIST |
| IE | 9.12 | eV | NIST |
| IE | 9.12 | eV | NIST |
| IE | 9.12 | eV | NIST |
| IE | 9.11 | eV | NIST |
| log10WS | [-2.59; -2.59] |
|
|
| log10WS | -2.59 | Aq. Sol... | |
| log10WS | -2.59 | Estimat... | |
| logPoct/wat | 2.117 | Crippen Calculated Property | |
| McVol | 80.240 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 4328.25 | kPa | Joback Calculated Property |
| Inp | [643.00; 714.00] |
|
|
| Inp | Outlier 705.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | Outlier 704.40 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 680.50 | NIST | |
| Inp | 676.80 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 687.50 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 685.10 | NIST | |
| Inp | 675.90 | NIST | |
| Inp | Outlier 704.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 675.70 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 670.50 | NIST | |
| Inp | 670.40 | NIST | |
| Inp | 672.40 | NIST | |
| Inp | 672.40 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 702.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 668.30 | NIST | |
| Inp | 674.40 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | Outlier 707.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 673.60 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 687.40 | NIST | |
| Inp | 701.10 | NIST | |
| Inp | 677.10 | NIST | |
| Inp | 676.70 | NIST | |
| Inp | 678.80 | NIST | |
| Inp | 677.10 | NIST | |
| Inp | 676.70 | NIST | |
| Inp | 678.80 | NIST | |
| Inp | 667.76 | NIST | |
| Inp | 667.80 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | Outlier 643.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | Outlier 714.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | Outlier 705.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 679.00 | NIST | |
| I | [808.00; 850.00] |
|
|
| I | 822.00 | NIST | |
| I | 850.00 | NIST | |
| I | 832.00 | NIST | |
| I | 841.00 | NIST | |
| I | 825.00 | NIST | |
| I | 850.00 | NIST | |
| I | 849.70 | NIST | |
| I | 832.40 | NIST | |
| I | 840.90 | NIST | |
| I | 849.70 | NIST | |
| I | 832.40 | NIST | |
| I | 840.90 | NIST | |
| I | 808.00 | NIST | |
| I | 808.00 | NIST | |
| I | 808.00 | NIST | |
| I | 811.00 | NIST | |
| I | 808.00 | NIST | |
| S°gas | 310.45 | J/mol×K | NIST |
| S°liquid | [214.60; 216.70] | J/mol×K |
|
| S°liquid | 214.60 | J/mol×K | NIST |
| S°liquid | 216.19 | J/mol×K | NIST |
| S°liquid | 216.70 | J/mol×K | NIST |
| Tboil | [355.97; 356.15] | K |
|
| Tboil | 356.13 | K | KDB |
| Tboil | 355.97 | K | Isobari... |
| Tboil | 356.15 | K | Vapor L... |
| Tboil | 355.97 | K | Isobari... |
| Tboil | 355.97 | K | Isobari... |
| Tc | [553.50; 560.42] | K |
|
| Tc | 560.40 | K | KDB |
| Tc | 560.40 ± 0.10 | K | NIST |
| Tc | 560.40 | K | NIST |
| Tc | 560.40 ± 0.30 | K | NIST |
| Tc | 560.42 ± 0.02 | K | NIST |
| Tc | Outlier 553.50 ± 0.15 | K | NIST |
| Tfus | [168.00; 169.80] | K |
|
| Tfus | 169.60 | K | KDB |
| Tfus | 169.27 | K | Aq. Sol... |
| Tfus | 169.64 ± 0.06 | K | NIST |
| Tfus | 169.45 ± 0.50 | K | NIST |
| Tfus | 169.49 ± 0.20 | K | NIST |
| Tfus | Outlier 168.00 ± 3.00 | K | NIST |
| Tfus | 169.80 ± 0.30 | K | NIST |
| Tfus | 169.00 ± 1.50 | K | NIST |
| Tfus | 169.05 ± 0.20 | K | NIST |
| Tfus | 169.10 ± 1.00 | K | NIST |
| Tfus | 169.00 ± 0.30 | K | NIST |
| Ttriple | [169.00; 169.67] | K |
|
| Ttriple | 169.66 ± 0.02 | K | NIST |
| Ttriple | 169.67 ± 0.05 | K | NIST |
| Ttriple | 169.00 ± 0.20 | K | NIST |
| Vc | 0.291 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [133.47; 148.53] | J/mol×K | [370.00; 410.00] |
|
| Cp,gas | 133.47 | J/mol×K | 370.00 | NIST |
| Cp,gas | 141.42 | J/mol×K | 390.00 | NIST |
| Cp,gas | 148.53 | J/mol×K | 410.00 | NIST |
| Cp,liquid | [145.60; 152.90] | J/mol×K | [293.20; 298.15] |
|
| Cp,liquid | 145.60 | J/mol×K | 293.20 | NIST |
| Cp,liquid | 152.90 | J/mol×K | 298.12 | NIST |
| Cp,liquid | 148.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 148.35 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 149.16 | J/mol×K | 298.15 | NIST |
| η | [0.0002771; 0.0099936] | Pa×s | [169.76; 360.06] |
|
| η | 0.0099936 | Pa×s | 169.76 | Joback Calculated Property |
| η | 0.0034351 | Pa×s | 201.48 | Joback Calculated Property |
| η | 0.0015788 | Pa×s | 233.19 | Joback Calculated Property |
| η | 0.0008741 | Pa×s | 264.91 | Joback Calculated Property |
| η | 0.0005491 | Pa×s | 296.63 | Joback Calculated Property |
| η | 0.0003774 | Pa×s | 328.34 | Joback Calculated Property |
| η | 0.0002771 | Pa×s | 360.06 | Joback Calculated Property |
| ΔfusH | [3.28; 4.23] | kJ/mol | [138.70; 169.70] |
|
| ΔfusH | 4.23 | kJ/mol | 138.70 | NIST |
| ΔfusH | 3.28 | kJ/mol | 169.70 | NIST |
| ΔfusH | 3.28 | kJ/mol | 169.70 | NIST |
| ΔvapH | [30.46; 33.70] | kJ/mol | [260.50; 356.20] |
|
| ΔvapH | 32.60 | kJ/mol | 260.50 | NIST |
| ΔvapH | 32.59 | kJ/mol | 300.00 | NIST |
| ΔvapH | 32.70 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 33.10 | kJ/mol | 313.50 | NIST |
| ΔvapH | 33.70 | kJ/mol | 321.00 | NIST |
| ΔvapH | 32.20 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 31.70 ± 0.10 | kJ/mol | 333.00 | NIST |
| ΔvapH | 32.90 | kJ/mol | 333.00 | NIST |
| ΔvapH | 32.60 | kJ/mol | 334.00 | NIST |
| ΔvapH | 32.80 | kJ/mol | 335.50 | NIST |
| ΔvapH | 32.70 | kJ/mol | 337.00 | NIST |
| ΔvapH | 31.20 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 30.70 ± 0.10 | kJ/mol | 353.00 | NIST |
| ΔvapH | 30.46 | kJ/mol | 356.20 | NIST |
| Pvap | [19.80; 101.80] | kPa | [310.15; 356.35] |
|
| Pvap | 19.80 | kPa | 310.15 | VLE and... |
| Pvap | 24.94 | kPa | 315.56 | Isobari... |
| Pvap | 27.43 | kPa | 318.01 | Isobari... |
| Pvap | 29.98 | kPa | 320.26 | Isobari... |
| Pvap | 29.70 | kPa | 320.35 | VLE and... |
| Pvap | 32.47 | kPa | 322.34 | Isobari... |
| Pvap | 34.95 | kPa | 324.31 | Isobari... |
| Pvap | 37.52 | kPa | 326.23 | Isobari... |
| Pvap | 39.98 | kPa | 327.96 | Isobari... |
| Pvap | 39.70 | kPa | 328.05 | VLE and... |
| Pvap | 42.45 | kPa | 329.61 | Isobari... |
| Pvap | 45.01 | kPa | 331.23 | Isobari... |
| Pvap | 47.48 | kPa | 332.73 | Isobari... |
| Pvap | 49.60 | kPa | 334.20 | VLE and... |
| Pvap | 50.02 | kPa | 334.22 | Isobari... |
| Pvap | 52.51 | kPa | 335.62 | Isobari... |
| Pvap | 55.02 | kPa | 336.98 | Isobari... |
| Pvap | 57.52 | kPa | 338.27 | Isobari... |
| Pvap | 59.98 | kPa | 339.52 | Isobari... |
| Pvap | 59.60 | kPa | 339.55 | VLE and... |
| Pvap | 62.46 | kPa | 340.73 | Isobari... |
| Pvap | 65.02 | kPa | 341.94 | Isobari... |
| Pvap | 67.51 | kPa | 343.07 | Isobari... |
| Pvap | 69.97 | kPa | 344.16 | Isobari... |
| Pvap | 69.70 | kPa | 344.25 | VLE and... |
| Pvap | 72.51 | kPa | 345.27 | Isobari... |
| Pvap | 74.96 | kPa | 346.30 | Isobari... |
| Pvap | 77.48 | kPa | 347.33 | Isobari... |
| Pvap | 80.02 | kPa | 348.35 | Isobari... |
| Pvap | 79.80 | kPa | 348.45 | VLE and... |
| Pvap | 82.52 | kPa | 349.31 | Isobari... |
| Pvap | 84.99 | kPa | 350.26 | Isobari... |
| Pvap | 87.45 | kPa | 351.18 | Isobari... |
| Pvap | 89.96 | kPa | 352.09 | Isobari... |
| Pvap | 89.80 | kPa | 352.20 | VLE and... |
| Pvap | 92.46 | kPa | 352.97 | Isobari... |
| Pvap | 95.01 | kPa | 353.85 | Isobari... |
| Pvap | 97.52 | kPa | 354.71 | Isobari... |
| Pvap | 101.33 | kPa | 355.97 | Isobari... |
| Pvap | 101.33 | kPa | 356.15 | Vapor L... |
| Pvap | 101.80 | kPa | 356.35 | VLE and... |
| n0 | [1.44378; 1.44378] | [298.15; 298.15] |
|
|
| n0 | 1.44378 | 298.15 | Experim... | |
| n0 | 1.44378 | 298.15 | Separat... | |
| ρl | 805.69 | kg/m3 | 298.15 | Phase b... |
| ΔfusS | [19.35; 30.50] | J/mol×K | [138.70; 169.70] |
|
| ΔfusS | 30.50 | J/mol×K | 138.70 | NIST |
| ΔfusS | 19.35 | J/mol×K | 169.70 | NIST |
| csound,fluid | [1169.60; 1252.10] | m/s | [303.15; 318.15] |
|
| csound,fluid | 1252.10 | m/s | 303.15 | Densiti... |
| csound,fluid | 1224.80 | m/s | 308.15 | Densiti... |
| csound,fluid | 1196.60 | m/s | 313.15 | Densiti... |
| csound,fluid | 1169.60 | m/s | 318.15 | Densiti... |
| λ | [0.12; 0.14] | W/m×K | [257.22; 328.22] |
|
| λ | 0.14 | W/m×K | 257.22 | Thermal... |
| λ | 0.14 | W/m×K | 257.42 | Thermal... |
| λ | 0.14 | W/m×K | 257.57 | Thermal... |
| λ | 0.13 | W/m×K | 275.37 | Thermal... |
| λ | 0.13 | W/m×K | 275.58 | Thermal... |
| λ | 0.13 | W/m×K | 275.73 | Thermal... |
| λ | 0.13 | W/m×K | 295.57 | Thermal... |
| λ | 0.13 | W/m×K | 295.77 | Thermal... |
| λ | 0.13 | W/m×K | 295.92 | Thermal... |
| λ | 0.13 | W/m×K | 296.28 | Thermal... |
| λ | 0.13 | W/m×K | 296.49 | Thermal... |
| λ | 0.13 | W/m×K | 296.65 | Thermal... |
| λ | 0.12 | W/m×K | 311.67 | Thermal... |
| λ | 0.12 | W/m×K | 311.89 | Thermal... |
| λ | 0.12 | W/m×K | 312.04 | Thermal... |
| λ | 0.12 | W/m×K | 327.85 | Thermal... |
| λ | 0.12 | W/m×K | 328.07 | Thermal... |
| λ | 0.12 | W/m×K | 328.22 | Thermal... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [258.08; 380.72] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41558e+01 | |||
| Coefficient B | -2.99426e+03 | |||
| Coefficient C | -4.21740e+01 | |||
| Temperature range, min. | 258.08 | |||
| Temperature range, max. | 380.72 | |||
| Pvap | 1.33 | kPa | 258.08 | Calculated Property |
| Pvap | 3.04 | kPa | 271.71 | Calculated Property |
| Pvap | 6.31 | kPa | 285.33 | Calculated Property |
| Pvap | 12.13 | kPa | 298.96 | Calculated Property |
| Pvap | 21.82 | kPa | 312.59 | Calculated Property |
| Pvap | 37.12 | kPa | 326.21 | Calculated Property |
| Pvap | 60.14 | kPa | 339.84 | Calculated Property |
| Pvap | 93.42 | kPa | 353.47 | Calculated Property |
| Pvap | 139.83 | kPa | 367.09 | Calculated Property |
| Pvap | 202.63 | kPa | 380.72 | Calculated Property |
| Pvap | [9.03e-05; 4391.33] | kPa | [169.67; 560.40] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.66975e+01 | |||
| Coefficient B | -6.84280e+03 | |||
| Coefficient C | -1.08968e+01 | |||
| Coefficient D | 9.11435e-06 | |||
| Temperature range, min. | 169.67 | |||
| Temperature range, max. | 560.40 | |||
| Pvap | 9.03e-05 | kPa | 169.67 | Calculated Property |
| Pvap | 0.03 | kPa | 213.08 | Calculated Property |
| Pvap | 1.19 | kPa | 256.50 | Calculated Property |
| Pvap | 12.83 | kPa | 299.91 | Calculated Property |
| Pvap | 67.91 | kPa | 343.33 | Calculated Property |
| Pvap | 232.04 | kPa | 386.74 | Calculated Property |
| Pvap | 599.80 | kPa | 430.16 | Calculated Property |
| Pvap | 1293.07 | kPa | 473.57 | Calculated Property |
| Pvap | 2475.87 | kPa | 516.99 | Calculated Property |
| Pvap | 4391.33 | kPa | 560.40 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexene.
Mixtures
- Cyclohexene + Cyclohexane
- Morpholine + Cyclohexene
- Morpholine + Cyclohexene + Cyclohexane
- Acetic acid, pentyl ester + Cyclohexene
- 2-Pyrrolidinone, 1-methyl- + Cyclohexene
- N,N-Dimethylacetamide + Cyclohexene
- Cyclohexanol + Cyclohexene
- Cyclohexanol + Cyclohexene + Water
- Methyl Isobutyl Ketone + Cyclohexene
- Methyl Isobutyl Ketone + Cyclohexene + Cyclohexane
- Diethyl carbonate + Cyclohexene
- Diethyl carbonate + Cyclohexene + Cyclohexane
- Ethanol, 2-methoxy- + Cyclohexene
- Ethanol, 2-methoxy- + Cyclohexene + Cyclohexane
- Benzene + Cyclohexene
- Pyridine + Cyclohexene
- Dimethyl Sulfoxide + Cyclohexene
- Carbon dioxide + Cyclohexene
- Cyclic octaatomic sulfur + Cyclohexene
- Isopropyl Alcohol + Cyclohexene + Water
Find more mixtures with Cyclohexene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
- Isobaric vapor-liquid equilibria for binary and ternary mixtures with cyclohexane, cyclohexene, and morpholine at 100 kPa
- Phase equilibria for benzene-cyclohexene and activity coefficients at infinite dilution for the ternary systems with ionic liquids
- Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
- Liquid liquid and liquid liquid equilibrium for ternary system water acetonitrile cyclohexene at 298.15 K
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [EMIM]-based ionic liquids
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Ternary LLE measurements for the separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [DCA]-based ionic liquids
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
- Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Bis(trifluoromethylsulfonyl)imide, or dicyanamide-based ionic liquids in the liquid liquid extraction of hex-1-ene from hexane and cyclohexene from cyclohexane
- Liquid-liquid separation of hex-1-ene from hexane and cyclohexene from cyclohexane with ionic liquids
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Liquid-liquid separation of hexane/hex-1-ene and cyclohexane/cyclohexene by dicyanamide-based ionic liquids
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Imidazolium and pyridinium-based ionic liquids for the cyclohexane/cyclohexene separation by liquid-liquid extraction
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
- Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Vapor Liquid Equilibrium Measurements for Carbon Dioxide + Cyclohexene + Squalane at High Pressures Using a Synthetic Method
- Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
- Vapor-Liquid Phase Equilibrium of a Cyclohexene + Water + Cyclohexanol + Isophorone Quaternary System at 500 kPa
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Physical Properties (Density, Viscosity, Surface Tension, Interfacial Tension, and Contact Angle) of the System Isopropyl Alcohol + Cyclohexene + Water
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
- Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- Liquid-Liquid Equilibrium for the System Water + Cyclohexene + Cyclohexanol over the Temperature Range of (303.2 to 403.2) 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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