- InChI
- InChI=1S/C4H8O/c1-2-3-4-5/h4H,2-3H2,1H3
- InChI Key
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N
- Formula
- C4H8O
- SMILES
- CCCC=O
- Molecular Weight1
- 72.11
- CAS
- 123-72-8
- Other Names
-
- 1-Butanal
- 1-propanecarbaldehyde
- Aldehyde butyrique
- Aldeide butirrica
- BUTAL
- BUTYL ALDEHYDE
- Butaldehyde
- Butalyde
- Butan-1-al
- Butanaldehyde
- Butyral
- Butyraldehyd
- Butyraldehyde
- Butyric aldehyde
- Butyrylaldehyde
- NCI-C56291
- NSC 62779
- UN 1129
- n-Butanal
- n-Butyl aldehyde
- n-Butyraldehyde
- n-C3H7CHO
- propanecarbaldehyde
- 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).
- UFL : Upper 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).
- 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.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- 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).
- 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 | 0.3520 | KDB | |
| PAff | 792.70 | kJ/mol | NIST |
| Tig | 503.15 | K | KDB |
| BasG | 760.80 | kJ/mol | NIST |
| ΔcH°liquid | [-2478.70; -2477.10] | kJ/mol |
|
| ΔcH°liquid | -2477.10 ± 1.40 | kJ/mol | NIST |
| ΔcH°liquid | -2478.70 ± 0.71 | kJ/mol | NIST |
| μ | 2.60 | debye | KDB |
| EA | 6.94e-04 | eV | NIST |
| LFL | 2.50 | % in Air | KDB |
| UFL | 10.60 | % in Air | KDB |
| Tflash,cc | 263.71 | K | KDB |
| Tflash,oc | 266.48 | K | KDB |
| ΔfG° | -114.80 | kJ/mol | KDB |
| ΔfH°gas | [-211.80; -204.40] | kJ/mol |
|
| ΔfH°gas | -205.20 | kJ/mol | KDB |
| ΔfH°gas | -211.80 ± 0.92 | kJ/mol | NIST |
| ΔfH°gas | -204.40 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -206.70 | kJ/mol | NIST |
| ΔfH°gas | -205.10 | kJ/mol | NIST |
| ΔfH°liquid | [-245.40; -238.10] | kJ/mol |
|
| ΔfH°liquid | -245.40 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | -238.10 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | -240.30 | kJ/mol | NIST |
| ΔfH°liquid | -238.70 ± 0.71 | kJ/mol | NIST |
| ΔfusH° | 8.40 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [33.20; 33.70] | kJ/mol |
|
| ΔvapH° | 33.20 | kJ/mol | NIST |
| ΔvapH° | 33.60 | kJ/mol | NIST |
| ΔvapH° | 33.70 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 33.70 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 33.70 | kJ/mol | NIST |
| IE | [9.73; 9.86] | eV |
|
| IE | 9.82 ± 0.04 | eV | NIST |
| IE | 9.83 | eV | NIST |
| IE | 9.80 | eV | NIST |
| IE | 9.73 ± 0.01 | eV | NIST |
| IE | 9.84 ± 0.01 | eV | NIST |
| IE | 9.73 ± 0.03 | eV | NIST |
| IE | 9.86 ± 0.02 | eV | NIST |
| IE | 9.85 | eV | NIST |
| IE | 9.83 | eV | NIST |
| log10WS | [-0.01; -1.00e-02] |
|
|
| log10WS | -1.00e-02 | Aq. Sol... | |
| log10WS | -0.01 | Estimat... | |
| logPoct/wat | 0.985 | Crippen Calculated Property | |
| McVol | 68.790 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | [4320.00; 4320.00] | kPa |
|
| Pc | 4320.00 | kPa | KDB |
| Pc | 4320.00 ± 100.00 | kPa | NIST |
| ρc | 279.77 ± 5.05 | kg/m3 | NIST |
| Inp | [542.10; 618.79] |
|
|
| Inp | 571.50 | NIST | |
| Inp | 570.91 | NIST | |
| Inp | 568.78 | NIST | |
| Inp | 569.15 | NIST | |
| Inp | 571.57 | NIST | |
| Inp | 573.77 | NIST | |
| Inp | 575.99 | NIST | |
| Inp | 578.18 | NIST | |
| Inp | 580.49 | NIST | |
| Inp | 583.70 | NIST | |
| Inp | 587.66 | NIST | |
| Inp | 588.95 | NIST | |
| Inp | Outlier 615.44 | NIST | |
| Inp | Outlier 618.79 | NIST | |
| Inp | 573.33 | NIST | |
| Inp | 570.90 | NIST | |
| Inp | 570.70 | NIST | |
| Inp | 571.10 | NIST | |
| Inp | 571.90 | NIST | |
| Inp | 572.54 | NIST | |
| Inp | Outlier 542.10 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 553.00 | NIST | |
| Inp | 554.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 555.00 | NIST | |
| Inp | 553.00 | NIST | |
| Inp | 586.00 | NIST | |
| Inp | 586.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 561.00 | NIST | |
| Inp | 589.50 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | Outlier 613.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | Outlier 545.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 563.31 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 583.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | Outlier 614.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 550.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 571.50 | NIST | |
| Inp | 573.77 | NIST | |
| Inp | 587.66 | NIST | |
| Inp | 570.90 | NIST | |
| Inp | Outlier 542.10 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 554.00 | NIST | |
| Inp | 586.00 | NIST | |
| Inp | 605.00 | NIST | |
| I | [830.00; 911.46] |
|
|
| I | 854.46 | NIST | |
| I | 867.47 | NIST | |
| I | 874.62 | NIST | |
| I | 891.30 | NIST | |
| I | 911.46 | NIST | |
| I | 907.20 | NIST | |
| I | 894.80 | NIST | |
| I | 897.80 | NIST | |
| I | 901.80 | NIST | |
| I | 906.00 | NIST | |
| I | 867.00 | NIST | |
| I | 853.00 | NIST | |
| I | 839.00 | NIST | |
| I | 875.00 | NIST | |
| I | 875.00 | NIST | |
| I | 904.00 | NIST | |
| I | 867.00 | NIST | |
| I | 867.00 | NIST | |
| I | 867.00 | NIST | |
| I | 877.00 | NIST | |
| I | 899.00 | NIST | |
| I | 891.00 | NIST | |
| I | 877.00 | NIST | |
| I | 866.00 | NIST | |
| I | 883.00 | NIST | |
| I | 878.00 | NIST | |
| I | 880.00 | NIST | |
| I | 883.00 | NIST | |
| I | 881.00 | NIST | |
| I | Outlier 830.00 | NIST | |
| I | Outlier 831.00 | NIST | |
| I | 862.00 | NIST | |
| I | 887.00 | NIST | |
| I | 878.00 | NIST | |
| I | 895.00 | NIST | |
| I | 899.00 | NIST | |
| I | 905.00 | NIST | |
| I | 880.00 | NIST | |
| I | 895.00 | NIST | |
| I | 895.00 | NIST | |
| I | 886.00 | NIST | |
| I | 867.00 | NIST | |
| I | 839.00 | NIST | |
| I | 839.00 | NIST | |
| I | 839.00 | NIST | |
| I | 877.00 | NIST | |
| I | 890.00 | NIST | |
| I | 864.00 | NIST | |
| I | 875.00 | NIST | |
| I | 891.00 | NIST | |
| I | 861.00 | NIST | |
| I | 866.00 | NIST | |
| I | 861.00 | NIST | |
| I | 878.00 | NIST | |
| I | 880.00 | NIST | |
| I | 859.00 | NIST | |
| I | 867.00 | NIST | |
| I | 837.00 | NIST | |
| I | 895.00 | NIST | |
| I | 877.00 | NIST | |
| I | 865.00 | NIST | |
| I | Outlier 832.00 | NIST | |
| I | 885.00 | NIST | |
| I | 875.00 | NIST | |
| I | 880.00 | NIST | |
| I | 898.00 | NIST | |
| I | 910.00 | NIST | |
| I | 891.00 | NIST | |
| I | 880.00 | NIST | |
| I | 877.00 | NIST | |
| I | 853.00 | NIST | |
| S°gas | 344.80 ± 4.20 | J/mol×K | NIST |
| S°liquid | [242.70; 246.90] | J/mol×K |
|
| S°liquid | 242.70 | J/mol×K | NIST |
| S°liquid | 246.90 | J/mol×K | NIST |
| Tboil | [75.70; 1021.99] | K |
|
| Tboil | 347.90 | K | KDB |
| Tboil | 348.70 | K | NIST |
| Tboil | Outlier 1021.99 ± 0.10 | K | NIST |
| Tboil | 347.95 ± 0.40 | K | NIST |
| Tboil | 347.94 ± 0.30 | K | NIST |
| Tboil | 347.95 | K | NIST |
| Tboil | 347.40 ± 0.50 | K | NIST |
| Tboil | 347.65 ± 0.50 | K | NIST |
| Tboil | 347.85 ± 1.00 | K | NIST |
| Tboil | 344.90 ± 3.00 | K | NIST |
| Tboil | 347.35 ± 1.00 | K | NIST |
| Tboil | 348.35 ± 0.50 | K | NIST |
| Tboil | 348.40 ± 0.60 | K | NIST |
| Tboil | 346.00 ± 3.00 | K | NIST |
| Tboil | 348.35 ± 0.50 | K | NIST |
| Tboil | 348.65 ± 1.00 | K | NIST |
| Tboil | 349.15 ± 2.00 | K | NIST |
| Tboil | 348.65 ± 1.00 | K | NIST |
| Tboil | 347.75 ± 0.50 | K | NIST |
| Tboil | 347.95 ± 0.30 | K | NIST |
| Tboil | 346.15 ± 2.00 | K | NIST |
| Tboil | 348.05 ± 1.00 | K | NIST |
| Tboil | 346.65 ± 1.00 | K | NIST |
| Tboil | 346.65 ± 2.00 | K | NIST |
| Tboil | 347.85 ± 0.50 | K | NIST |
| Tboil | 346.00 ± 3.00 | K | NIST |
| Tboil | 350.15 ± 1.00 | K | NIST |
| Tboil | 347.40 ± 1.00 | K | NIST |
| Tboil | Outlier 75.70 ± 0.50 | K | NIST |
| Tboil | 348.15 ± 2.00 | K | NIST |
| Tboil | 345.65 ± 3.00 | K | NIST |
| Tboil | 348.15 ± 2.00 | K | NIST |
| Tboil | 346.65 ± 2.00 | K | NIST |
| Tboil | 348.15 ± 3.00 | K | NIST |
| Tboil | 348.15 ± 2.00 | K | NIST |
| Tc | [537.10; 537.20] | K |
|
| Tc | 537.20 | K | KDB |
| Tc | 537.10 ± 4.00 | K | NIST |
| Tc | 537.20 ± 0.80 | K | NIST |
| Tfus | [174.00; 175.40] | K |
|
| Tfus | 174.00 | K | KDB |
| Tfus | 175.40 | K | Aq. Sol... |
| Ttriple | [176.28; 176.80] | K |
|
| Ttriple | 176.28 ± 0.02 | K | NIST |
| Ttriple | 176.80 ± 0.20 | K | NIST |
| Ttriple | 176.80 ± 0.20 | K | NIST |
| Vc | 0.258 | m3/kmol | KDB |
| Zc | 0.2495350 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [112.13; 149.84] | J/mol×K | [339.58; 512.50] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 150 350 400 450 500 | ||||
| Cp,gas | 112.13 | J/mol×K | 339.58 | Joback Calculated Property |
| Cp,gas | 119.02 | J/mol×K | 368.40 | Joback Calculated Property |
| Cp,gas | 125.66 | J/mol×K | 397.22 | Joback Calculated Property |
| Cp,gas | 132.06 | J/mol×K | 426.04 | Joback Calculated Property |
| Cp,gas | 138.22 | J/mol×K | 454.86 | Joback Calculated Property |
| Cp,gas | 144.14 | J/mol×K | 483.68 | Joback Calculated Property |
| Cp,gas | 149.84 | J/mol×K | 512.50 | Joback Calculated Property |
| Cp,liquid | [163.51; 164.70] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 164.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 163.51 | J/mol×K | 298.15 | NIST |
| η | [0.0002849; 0.0030911] | Pa×s | [176.84; 339.58] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 200 250 300 | ||||
| η | 0.0030911 | Pa×s | 176.84 | Joback Calculated Property |
| η | 0.0015952 | Pa×s | 203.96 | Joback Calculated Property |
| η | 0.0009615 | Pa×s | 231.09 | Joback Calculated Property |
| η | 0.0006446 | Pa×s | 258.21 | Joback Calculated Property |
| η | 0.0004663 | Pa×s | 285.33 | Joback Calculated Property |
| η | 0.0003568 | Pa×s | 312.46 | Joback Calculated Property |
| η | 0.0002849 | Pa×s | 339.58 | Joback Calculated Property |
| ΔfusH | [10.77; 11.10] | kJ/mol | [176.28; 176.80] |
|
| ΔfusH | 10.77 | kJ/mol | 176.28 | NIST |
| ΔfusH | 11.09 | kJ/mol | 176.80 | NIST |
| ΔfusH | 11.10 | kJ/mol | 176.80 | NIST |
| ΔvapH | [31.51; 34.20] | kJ/mol | [305.50; 347.90] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 31.5 32 32.5 33 33.5 34 310 320 330 340 | ||||
| ΔvapH | 33.90 | kJ/mol | 305.50 | NIST |
| ΔvapH | 34.20 | kJ/mol | 321.00 | NIST |
| ΔvapH | 33.30 | kJ/mol | 325.50 | NIST |
| ΔvapH | 32.90 | kJ/mol | 339.00 | NIST |
| ΔvapH | 31.51 | kJ/mol | 347.90 | KDB |
| n0 | 1.38390 | 293.15 | Liquid ... | |
| ρl | [771.30; 802.00] | kg/m3 | [293.00; 323.15] |
|
|
T(K) Liquid Density (kg/m3) 770 775 780 785 790 795 800 805 300 310 320 | ||||
| ρl | 802.00 | kg/m3 | 293.00 | KDB |
| ρl | 796.99 | kg/m3 | 298.15 | Binary ... |
| ρl | 791.80 | kg/m3 | 303.15 | Binary ... |
| ρl | 786.41 | kg/m3 | 308.15 | Binary ... |
| ρl | 781.37 | kg/m3 | 313.15 | Binary ... |
| ρl | 776.39 | kg/m3 | 318.15 | Binary ... |
| ρl | 771.30 | kg/m3 | 323.15 | Binary ... |
| ΔfusS | [61.11; 62.81] | J/mol×K | [176.28; 176.80] |
|
| ΔfusS | 61.11 | J/mol×K | 176.28 | NIST |
| ΔfusS | 62.81 | J/mol×K | 176.80 | NIST |
| γ | 0.02 | N/m | 293.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [256.01; 370.69] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45982e+01 | |||
| Coefficient B | -3.03353e+03 | |||
| Coefficient C | -4.40350e+01 | |||
| Temperature range, min. | 256.01 | |||
| Temperature range, max. | 370.69 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 256.01 | Calculated Property |
| Pvap | 3.00 | kPa | 268.75 | Calculated Property |
| Pvap | 6.19 | kPa | 281.49 | Calculated Property |
| Pvap | 11.87 | kPa | 294.24 | Calculated Property |
| Pvap | 21.36 | kPa | 306.98 | Calculated Property |
| Pvap | 36.40 | kPa | 319.72 | Calculated Property |
| Pvap | 59.19 | kPa | 332.46 | Calculated Property |
| Pvap | 92.36 | kPa | 345.21 | Calculated Property |
| Pvap | 139.01 | kPa | 357.95 | Calculated Property |
| Pvap | 202.66 | kPa | 370.69 | Calculated Property |
| Pvap | [2.63e-04; 4452.12] | kPa | [176.75; 535.36] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.06744e+02 | |||
| Coefficient B | -7.59444e+03 | |||
| Coefficient C | -1.39976e+01 | |||
| Coefficient D | 1.32212e-05 | |||
| Temperature range, min. | 176.75 | |||
| Temperature range, max. | 535.36 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 500 | ||||
| Pvap | 2.63e-04 | kPa | 176.75 | Calculated Property |
| Pvap | 0.05 | kPa | 216.60 | Calculated Property |
| Pvap | 1.43 | kPa | 256.44 | Calculated Property |
| Pvap | 13.56 | kPa | 296.29 | Calculated Property |
| Pvap | 67.53 | kPa | 336.13 | Calculated Property |
| Pvap | 224.56 | kPa | 375.98 | Calculated Property |
| Pvap | 576.41 | kPa | 415.82 | Calculated Property |
| Pvap | 1251.51 | kPa | 455.67 | Calculated Property |
| Pvap | 2440.54 | kPa | 495.51 | Calculated Property |
| Pvap | 4452.12 | kPa | 535.36 | Calculated Property |
Similar Compounds
Find more compounds similar to Butanal.
Mixtures
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
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- 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
- 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
- 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
- Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol). Part II: (Propanal or butanal or heptanal) + (methanol or ethanol or 1-propanol)
- 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
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- 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, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
- 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
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- 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
- 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
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Solubility Measurement and Correlation of Carbon Monoxide (CO) in Butyraldehydes: n-Butyraldehyde and iso-Butyraldehyde
- Liquid Liquid Equilibrium Data of Water + Butyric Acid + {Butanal or n-Butanol} Ternary Systems at 293.15, 308.15, and 323.15 K
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- 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
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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