- InChI
- InChI=1S/C4H4S/c1-2-4-5-3-1/h1-4H
- InChI Key
- YTPLMLYBLZKORZ-UHFFFAOYSA-N
- Formula
- C4H4S
- SMILES
- c1ccsc1
- Molecular Weight1
- 84.14
- CAS
- 110-02-1
- Other Names
-
- CP 34
- Divinylene sulfide
- Furan, thio-
- Hopkin's lactic acid reagent
- Huile H50
- Huile HSO
- NSC 405073
- THIACYCLOPENTADIENE
- THIOFURAN
- Thiaphene
- Thiofen
- Thiofuram
- Thiofurfuran
- Thiole
- Thiophen
- Thiotetrole
- UN 2414
- USAF EK-1860
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- μ : Dipole Moment (debye).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation 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.
- 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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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.1960 | KDB | |
| PAff | 815.00 | kJ/mol | NIST |
| BasG | 784.30 | kJ/mol | NIST |
| μ | 0.50 | debye | KDB |
| ΔfG° | 126.90 | kJ/mol | KDB |
| ΔfH°gas | [115.00; 218.40] | kJ/mol |
|
| ΔfH°gas | 115.80 | kJ/mol | KDB |
| ΔfH°gas | 218.40 | kJ/mol | NIST |
| ΔfH°gas | 116.40 | kJ/mol | NIST |
| ΔfH°gas | 115.00 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | 116.70 | kJ/mol | NIST |
| ΔvapH° | [34.60; 35.40] | kJ/mol |
|
| ΔvapH° | 34.79 | kJ/mol | NIST |
| ΔvapH° | 34.60 | kJ/mol | NIST |
| ΔvapH° | 34.70 ± 0.03 | kJ/mol | NIST |
| ΔvapH° | 35.40 | kJ/mol | NIST |
| IE | [8.80; 9.12] | eV |
|
| IE | 8.86 ± 0.02 | eV | NIST |
| IE | 8.85 | eV | NIST |
| IE | 8.85 | eV | NIST |
| IE | 9.00 ± 0.10 | eV | NIST |
| IE | 8.87 ± 0.01 | eV | NIST |
| IE | 8.80 | eV | NIST |
| IE | 8.80 ± 0.05 | eV | NIST |
| IE | 8.90 | eV | NIST |
| IE | Outlier 9.05 | eV | NIST |
| IE | 8.87 ± 0.01 | eV | NIST |
| IE | Outlier 9.12 ± 0.05 | eV | NIST |
| IE | 8.87 ± 0.01 | eV | NIST |
| IE | 8.86 ± 0.01 | eV | NIST |
| IE | 8.80 ± 0.05 | eV | NIST |
| IE | 8.87 ± 0.05 | eV | NIST |
| IE | 8.86 ± 0.01 | eV | NIST |
| IE | 8.95 ± 0.02 | eV | NIST |
| IE | 8.85 | eV | NIST |
| IE | 8.90 | eV | NIST |
| IE | 8.90 | eV | NIST |
| IE | 8.85 | eV | NIST |
| IE | 8.87 | eV | NIST |
| log10WS | [-1.45; -1.33] |
|
|
| log10WS | -1.45 | Aq. Sol... | |
| log10WS | -1.33 | Estimat... | |
| logPoct/wat | 1.748 | Crippen Calculated Property | |
| McVol | 64.110 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [5690.00; 5700.00] | kPa |
|
| Pc | 5690.00 | kPa | KDB |
| Pc | 5700.00 ± 68.94 | kPa | NIST |
| Inp | [626.00; 703.00] |
|
|
| Inp | 694.00 | NIST | |
| Inp | 686.10 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 674.60 | NIST | |
| Inp | 679.60 | NIST | |
| Inp | 685.30 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 664.60 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 670.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 646.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | Outlier 626.00 | NIST | |
| Inp | 636.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 655.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 646.00 | NIST | |
| Inp | 647.00 | NIST | |
| Inp | 643.23 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 645.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 645.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 647.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 653.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 647.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 685.30 | NIST | |
| Inp | 641.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 652.00 | NIST | |
| I | [995.00; 1054.00] |
|
|
| I | Outlier 1054.00 | NIST | |
| I | 1039.00 | NIST | |
| I | 1046.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1034.00 | NIST | |
| I | 1030.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1041.00 | NIST | |
| I | Outlier 995.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1034.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 1035.00 | NIST | |
| I | Outlier 1054.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1035.00 | NIST | |
| I | Outlier 1054.00 | NIST | |
| Tboil | [356.80; 357.90] | K |
|
| Tboil | 357.10 | K | KDB |
| Tboil | 357.42 | K | Isobari... |
| Tboil | 357.42 | K | Isobari... |
| Tboil | 357.40 | K | NIST |
| Tboil | 357.26 ± 0.20 | K | NIST |
| Tboil | 357.30 | K | NIST |
| Tboil | 357.35 ± 0.10 | K | NIST |
| Tboil | 356.80 ± 0.50 | K | NIST |
| Tboil | Outlier 357.90 ± 0.50 | K | NIST |
| Tboil | 357.15 ± 0.50 | K | NIST |
| Tc | [579.40; 580.00] | K |
|
| Tc | 579.40 | K | KDB |
| Tc | 579.40 | K | NIST |
| Tc | 579.40 ± 0.30 | K | NIST |
| Tc | 580.00 ± 2.00 | K | NIST |
| Tfus | [233.15; 234.94] | K |
|
| Tfus | 233.70 | K | KDB |
| Tfus | 234.68 | K | Aq. Sol... |
| Tfus | 234.93 ± 0.05 | K | NIST |
| Tfus | 234.94 ± 0.10 | K | NIST |
| Tfus | 233.15 ± 0.40 | K | NIST |
| Ttriple | [233.70; 235.02] | K |
|
| Ttriple | 235.02 ± 0.05 | K | NIST |
| Ttriple | 234.90 ± 0.08 | K | NIST |
| Ttriple | 234.95 ± 0.06 | K | NIST |
| Ttriple | 233.70 ± 0.40 | K | NIST |
| Vc | [0.219; 0.220] | m3/kmol |
|
| Vc | 0.219 | m3/kmol | KDB |
| Vc | 0.220 ± 0.005 | m3/kmol | NIST |
| Zc | 0.2586670 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | 4.97 | kJ/mol | 235.20 | NIST |
| ΔsubH | [46.80; 49.00] | kJ/mol | [202.50; 211.50] |
|
| ΔsubH | 49.00 | kJ/mol | 202.50 | NIST |
| ΔsubH | 46.80 | kJ/mol | 211.50 | NIST |
| ΔvapH | [31.46; 35.80] | kJ/mol | [258.50; 357.30] |
|
| ΔvapH | 35.00 | kJ/mol | 258.50 | NIST |
| ΔvapH | 33.60 ± 0.10 | kJ/mol | 319.00 | NIST |
| ΔvapH | 35.80 | kJ/mol | 324.00 | NIST |
| ΔvapH | 34.10 | kJ/mol | 333.00 | NIST |
| ΔvapH | 32.70 ± 0.10 | kJ/mol | 336.00 | NIST |
| ΔvapH | 33.70 | kJ/mol | 352.00 | NIST |
| ΔvapH | 34.80 | kJ/mol | 353.00 | NIST |
| ΔvapH | 32.60 | kJ/mol | 353.50 | NIST |
| ΔvapH | 31.46 | kJ/mol | 357.00 | KDB |
| ΔvapH | 31.50 ± 0.10 | kJ/mol | 357.00 | NIST |
| ΔvapH | 31.48 | kJ/mol | 357.30 | NIST |
| Pvap | [2.78; 119.90] | kPa | [273.15; 363.15] |
|
| Pvap | 2.78 | kPa | 273.15 | Measure... |
| Pvap | 4.89 | kPa | 283.15 | Measure... |
| Pvap | 6.78 | kPa | 288.15 | Experim... |
| Pvap | 6.75 | kPa | 288.15 | Experim... |
| Pvap | 8.22 | kPa | 293.15 | Measure... |
| Pvap | 8.74 | kPa | 293.15 | Experim... |
| Pvap | 8.70 | kPa | 293.15 | Experim... |
| Pvap | 10.58 | kPa | 298.15 | Experim... |
| Pvap | 10.37 | kPa | 298.15 | Experim... |
| Pvap | 13.23 | kPa | 303.15 | Measure... |
| Pvap | 13.29 | kPa | 303.15 | Vapor P... |
| Pvap | 12.98 | kPa | 303.15 | Experim... |
| Pvap | 16.70 | kPa | 308.12 | Vapor-L... |
| Pvap | 16.50 | kPa | 308.13 | Vapor-L... |
| Pvap | 17.10 | kPa | 308.14 | Vapor-L... |
| Pvap | 17.10 | kPa | 308.15 | Vapor-L... |
| Pvap | 16.61 | kPa | 308.15 | Vapor P... |
| Pvap | 20.52 | kPa | 313.15 | Measure... |
| Pvap | 20.59 | kPa | 313.15 | Vapor P... |
| Pvap | 25.31 | kPa | 318.15 | Vapor P... |
| Pvap | 30.87 | kPa | 323.15 | Vapor P... |
| Pvap | 30.80 | kPa | 323.15 | Measure... |
| Pvap | 37.40 | kPa | 328.15 | Vapor P... |
| Pvap | 44.88 | kPa | 333.15 | Measure... |
| Pvap | 44.98 | kPa | 333.15 | Vapor P... |
| Pvap | 49.70 | kPa | 335.61 | Vapor-L... |
| Pvap | 49.60 | kPa | 335.84 | Vapor-L... |
| Pvap | 49.60 | kPa | 335.87 | Vapor-L... |
| Pvap | 51.20 | kPa | 336.83 | Vapor-L... |
| Pvap | 63.71 | kPa | 343.15 | Measure... |
| Pvap | 88.33 | kPa | 353.15 | Measure... |
| Pvap | 119.90 | kPa | 363.15 | Measure... |
| n0 | [1.52530; 1.52869] | [298.10; 298.15] |
|
|
| n0 | 1.52530 | 298.10 | Liquid-... | |
| n0 | 1.52550 | 298.15 | Vapor l... | |
| n0 | 1.52581 | 298.15 | Phase b... | |
| n0 | 1.52530 | 298.15 | Thiophe... | |
| n0 | 1.52550 | 298.15 | Vapor-L... | |
| n0 | 1.52550 | 298.15 | Vapor-L... | |
| n0 | 1.52869 | 298.15 | Vapor L... | |
| n0 | 1.52581 | 298.15 | Liquid-... | |
| n0 | 1.52581 | 298.15 | Measure... | |
| n0 | 1.52581 | 298.15 | (Liquid... | |
| ρl | [1058.46; 1071.00] | kg/m3 | [289.00; 298.15] |
|
| ρl | 1071.00 | kg/m3 | 289.00 | KDB |
| ρl | 1058.50 | kg/m3 | 298.15 | Solvent... |
| ρl | 1058.48 | kg/m3 | 298.15 | Phase b... |
| ρl | 1058.61 | kg/m3 | 298.15 | Desulfu... |
| ρl | 1058.48 | kg/m3 | 298.15 | Phase b... |
| ρl | 1058.56 | kg/m3 | 298.15 | Phase d... |
| ρl | 1058.61 | kg/m3 | 298.15 | Hexyl d... |
| ρl | 1058.64 | kg/m3 | 298.15 | Separat... |
| ρl | 1058.92 | kg/m3 | 298.15 | Effect ... |
| ρl | 1058.92 | kg/m3 | 298.15 | Extract... |
| ρl | 1058.56 | kg/m3 | 298.15 | Volumet... |
| ρl | 1058.46 | kg/m3 | 298.15 | Measure... |
| ρl | 1058.56 | kg/m3 | 298.15 | Thermod... |
| γ | 0.03 | N/m | 293.20 | KDB |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 101.00 | 1063.59 |
| 303.15 | 101.00 | 1051.55 |
| 313.09 | 1029.00 | 1040.96 |
| 313.09 | 1969.00 | 1041.84 |
| 313.09 | 2970.00 | 1042.78 |
| 313.09 | 3987.00 | 1043.71 |
| 313.09 | 5055.00 | 1044.72 |
| 313.09 | 5952.00 | 1045.51 |
| 313.09 | 6937.00 | 1046.43 |
| 313.09 | 8032.00 | 1047.39 |
| 313.09 | 9218.00 | 1048.44 |
| 313.09 | 10045.00 | 1049.18 |
| 313.09 | 11012.00 | 1050.03 |
| 313.09 | 12014.00 | 1050.9 |
| 313.09 | 12995.00 | 1051.74 |
| 313.09 | 13961.00 | 1052.59 |
| 313.09 | 14970.00 | 1053.43 |
| 313.09 | 15953.00 | 1054.26 |
| 313.09 | 17004.00 | 1055.16 |
| 313.09 | 18003.00 | 1055.95 |
| 313.09 | 18904.00 | 1056.76 |
| 313.15 | 101.00 | 1039.32 |
| 323.01 | 1047.00 | 1028.97 |
| 323.01 | 2059.00 | 1029.98 |
| 323.01 | 3070.00 | 1031.02 |
| 323.01 | 4047.00 | 1031.99 |
| 323.01 | 5002.00 | 1032.9 |
| 323.01 | 6005.00 | 1033.9 |
| 323.01 | 7068.00 | 1034.92 |
| 323.01 | 8021.00 | 1035.81 |
| 323.01 | 9013.00 | 1036.76 |
| 323.01 | 10005.00 | 1037.67 |
| 323.01 | 10991.00 | 1038.62 |
| 323.01 | 12034.00 | 1039.58 |
| 323.01 | 12977.00 | 1040.44 |
| 323.01 | 13999.00 | 1041.38 |
| 323.01 | 14991.00 | 1042.26 |
| 323.01 | 15995.00 | 1043.17 |
| 323.01 | 16998.00 | 1044.03 |
| 323.01 | 17983.00 | 1044.93 |
| 323.01 | 18951.00 | 1045.78 |
| 323.15 | 101.00 | 1026.98 |
| 332.85 | 1015.00 | 1016.93 |
| 332.85 | 2035.00 | 1018.0 |
| 332.85 | 3004.00 | 1019.06 |
| 332.85 | 3964.00 | 1020.05 |
| 332.85 | 4991.00 | 1021.14 |
| 332.85 | 6001.00 | 1022.17 |
| 332.85 | 7014.00 | 1023.21 |
| 332.85 | 7998.00 | 1024.2 |
| 332.85 | 9009.00 | 1025.23 |
| 332.85 | 9995.00 | 1026.19 |
| 332.85 | 10989.00 | 1027.18 |
| 332.85 | 12006.00 | 1028.17 |
| 332.85 | 13009.00 | 1029.18 |
| 332.85 | 13971.00 | 1030.09 |
| 332.85 | 15006.00 | 1031.04 |
| 332.85 | 15990.00 | 1032.01 |
| 332.85 | 17050.00 | 1033.03 |
| 332.85 | 17976.00 | 1033.88 |
| 332.85 | 19018.00 | 1034.92 |
| 333.15 | 101.00 | 1014.58 |
| 342.77 | 1039.00 | 1004.75 |
| 342.77 | 2072.00 | 1005.93 |
| 342.77 | 3033.00 | 1007.02 |
| 342.77 | 4023.00 | 1008.17 |
| 342.77 | 5027.00 | 1009.26 |
| 342.77 | 6033.00 | 1010.36 |
| 342.77 | 7008.00 | 1011.44 |
| 342.77 | 7998.00 | 1012.5 |
| 342.77 | 9005.00 | 1013.59 |
| 342.77 | 10000.00 | 1014.65 |
| 342.77 | 10963.00 | 1015.65 |
| 342.77 | 12009.00 | 1016.72 |
| 342.77 | 13023.00 | 1017.82 |
| 342.77 | 13928.00 | 1018.74 |
| 342.77 | 15009.00 | 1019.83 |
| 342.77 | 15998.00 | 1020.79 |
| 342.77 | 17025.00 | 1021.8 |
| 342.77 | 17995.00 | 1022.8 |
| 342.77 | 19013.00 | 1023.79 |
| 342.77 | 20001.00 | 1024.73 |
| 343.15 | 101.00 | 1002.15 |
| 352.67 | 1064.00 | 992.39 |
| 352.67 | 2003.00 | 993.54 |
| 352.67 | 3024.00 | 994.79 |
| 352.67 | 4003.00 | 995.98 |
| 352.67 | 5048.00 | 997.22 |
| 352.67 | 6013.00 | 998.36 |
| 352.67 | 7013.00 | 999.51 |
| 352.67 | 8050.00 | 1000.73 |
| 352.67 | 9018.00 | 1001.82 |
| 352.67 | 10003.00 | 1002.93 |
| 352.67 | 11003.00 | 1004.07 |
| 352.67 | 12004.00 | 1005.16 |
| 352.67 | 12998.00 | 1006.25 |
| 352.67 | 14005.00 | 1007.34 |
| 352.67 | 15038.00 | 1008.46 |
| 352.67 | 16006.00 | 1009.49 |
| 352.67 | 17027.00 | 1010.58 |
| 352.67 | 18001.00 | 1011.6 |
| 352.67 | 19031.00 | 1012.65 |
| 352.67 | 20017.00 | 1013.74 |
| 353.15 | 101.00 | 989.76 |
| 362.51 | 1007.00 | 979.8 |
| 362.51 | 2022.00 | 981.13 |
| 362.51 | 3029.00 | 982.49 |
| 362.51 | 4004.00 | 983.74 |
| 362.51 | 5006.00 | 985.01 |
| 362.51 | 6003.00 | 986.27 |
| 362.51 | 6999.00 | 987.5 |
| 362.51 | 7993.00 | 988.73 |
| 362.51 | 9007.00 | 989.99 |
| 362.51 | 9993.00 | 991.16 |
| 362.51 | 10997.00 | 992.36 |
| 362.51 | 11993.00 | 993.56 |
| 362.51 | 12838.00 | 994.53 |
| 362.51 | 14038.00 | 995.94 |
| 362.51 | 15044.00 | 997.1 |
| 362.51 | 16029.00 | 998.18 |
| 362.51 | 17006.00 | 999.27 |
| 362.51 | 18016.00 | 1000.4 |
| 362.51 | 18987.00 | 1001.47 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 1058.44 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 1076.4 |
| 288.15 | 100.00 | 1070.54 |
| 293.15 | 100.00 | 1064.59 |
| 298.15 | 100.00 | 1058.65 |
| 303.15 | 100.00 | 1052.71 |
| 308.15 | 100.00 | 1046.7 |
| 313.15 | 100.00 | 1040.68 |
| 318.15 | 100.00 | 1034.64 |
| 323.15 | 100.00 | 1028.59 |
| 328.15 | 100.00 | 1022.43 |
| 333.15 | 100.00 | 1016.27 |
| 338.15 | 100.00 | 1010.08 |
| 283.15 | 2000.00 | 1077.94 |
| 288.15 | 2000.00 | 1072.11 |
| 293.15 | 2000.00 | 1066.21 |
| 298.15 | 2000.00 | 1060.32 |
| 303.15 | 2000.00 | 1054.43 |
| 308.15 | 2000.00 | 1048.48 |
| 313.15 | 2000.00 | 1042.52 |
| 318.15 | 2000.00 | 1036.54 |
| 323.15 | 2000.00 | 1030.52 |
| 328.15 | 2000.00 | 1024.49 |
| 333.15 | 2000.00 | 1018.35 |
| 338.15 | 2000.00 | 1012.22 |
| 283.15 | 5000.00 | 1080.27 |
| 288.15 | 5000.00 | 1074.53 |
| 293.15 | 5000.00 | 1068.67 |
| 298.15 | 5000.00 | 1062.91 |
| 303.15 | 5000.00 | 1057.07 |
| 308.15 | 5000.00 | 1051.21 |
| 313.15 | 5000.00 | 1045.35 |
| 318.15 | 5000.00 | 1039.44 |
| 323.15 | 5000.00 | 1033.54 |
| 328.15 | 5000.00 | 1027.57 |
| 333.15 | 5000.00 | 1021.56 |
| 338.15 | 5000.00 | 1015.53 |
| 283.15 | 7000.00 | 1081.81 |
| 288.15 | 7000.00 | 1076.12 |
| 293.15 | 7000.00 | 1070.33 |
| 298.15 | 7000.00 | 1064.57 |
| 303.15 | 7000.00 | 1058.82 |
| 308.15 | 7000.00 | 1052.99 |
| 313.15 | 7000.00 | 1047.19 |
| 318.15 | 7000.00 | 1041.36 |
| 323.15 | 7000.00 | 1035.52 |
| 328.15 | 7000.00 | 1029.6 |
| 333.15 | 7000.00 | 1023.65 |
| 338.15 | 7000.00 | 1017.69 |
| 283.15 | 10000.00 | 1084.09 |
| 288.15 | 10000.00 | 1078.46 |
| 293.15 | 10000.00 | 1072.75 |
| 298.15 | 10000.00 | 1067.05 |
| 303.15 | 10000.00 | 1061.36 |
| 308.15 | 10000.00 | 1055.61 |
| 313.15 | 10000.00 | 1049.91 |
| 318.15 | 10000.00 | 1044.15 |
| 323.15 | 10000.00 | 1038.37 |
| 328.15 | 10000.00 | 1032.58 |
| 333.15 | 10000.00 | 1026.72 |
| 338.15 | 10000.00 | 1020.86 |
| 283.15 | 15000.00 | 1087.78 |
| 288.15 | 15000.00 | 1082.24 |
| 293.15 | 15000.00 | 1076.63 |
| 298.15 | 15000.00 | 1071.07 |
| 303.15 | 15000.00 | 1065.48 |
| 308.15 | 15000.00 | 1059.87 |
| 313.15 | 15000.00 | 1054.25 |
| 318.15 | 15000.00 | 1048.65 |
| 323.15 | 15000.00 | 1042.99 |
| 328.15 | 15000.00 | 1037.33 |
| 333.15 | 15000.00 | 1031.63 |
| 338.15 | 15000.00 | 1025.92 |
| 283.15 | 20000.00 | 1091.37 |
| 288.15 | 20000.00 | 1085.9 |
| 293.15 | 20000.00 | 1080.39 |
| 298.15 | 20000.00 | 1074.94 |
| 303.15 | 20000.00 | 1069.46 |
| 308.15 | 20000.00 | 1063.97 |
| 313.15 | 20000.00 | 1058.47 |
| 318.15 | 20000.00 | 1052.97 |
| 323.15 | 20000.00 | 1047.45 |
| 328.15 | 20000.00 | 1041.91 |
| 333.15 | 20000.00 | 1036.34 |
| 338.15 | 20000.00 | 1030.78 |
| 283.15 | 25000.00 | 1094.82 |
| 288.15 | 25000.00 | 1089.45 |
| 293.15 | 25000.00 | 1084.05 |
| 298.15 | 25000.00 | 1078.69 |
| 303.15 | 25000.00 | 1073.3 |
| 308.15 | 25000.00 | 1067.92 |
| 313.15 | 25000.00 | 1062.52 |
| 318.15 | 25000.00 | 1057.12 |
| 323.15 | 25000.00 | 1051.73 |
| 328.15 | 25000.00 | 1046.31 |
| 333.15 | 25000.00 | 1040.87 |
| 338.15 | 25000.00 | 1035.41 |
| 283.15 | 30000.00 | 1098.18 |
| 288.15 | 30000.00 | 1092.91 |
| 293.15 | 30000.00 | 1087.58 |
| 298.15 | 30000.00 | 1082.3 |
| 303.15 | 30000.00 | 1077.03 |
| 308.15 | 30000.00 | 1071.73 |
| 313.15 | 30000.00 | 1066.43 |
| 318.15 | 30000.00 | 1061.15 |
| 323.15 | 30000.00 | 1055.85 |
| 328.15 | 30000.00 | 1050.54 |
| 333.15 | 30000.00 | 1045.21 |
| 338.15 | 30000.00 | 1039.88 |
| 283.15 | 35000.00 | 1101.44 |
| 288.15 | 35000.00 | 1096.24 |
| 293.15 | 35000.00 | 1091.01 |
| 298.15 | 35000.00 | 1085.81 |
| 303.15 | 35000.00 | 1080.62 |
| 308.15 | 35000.00 | 1075.4 |
| 313.15 | 35000.00 | 1070.21 |
| 318.15 | 35000.00 | 1065.02 |
| 323.15 | 35000.00 | 1059.82 |
| 328.15 | 35000.00 | 1054.61 |
| 333.15 | 35000.00 | 1049.39 |
| 338.15 | 35000.00 | 1044.17 |
| 283.15 | 40000.00 | 1104.61 |
| 288.15 | 40000.00 | 1099.5 |
| 293.15 | 40000.00 | 1094.34 |
| 298.15 | 40000.00 | 1089.21 |
| 303.15 | 40000.00 | 1084.1 |
| 308.15 | 40000.00 | 1078.99 |
| 313.15 | 40000.00 | 1073.88 |
| 318.15 | 40000.00 | 1068.77 |
| 323.15 | 40000.00 | 1063.67 |
| 328.15 | 40000.00 | 1058.55 |
| 333.15 | 40000.00 | 1053.43 |
| 338.15 | 40000.00 | 1048.31 |
| 283.15 | 45000.00 | 1107.7 |
| 288.15 | 45000.00 | 1102.65 |
| 293.15 | 45000.00 | 1097.57 |
| 298.15 | 45000.00 | 1092.53 |
| 303.15 | 45000.00 | 1087.49 |
| 308.15 | 45000.00 | 1082.45 |
| 313.15 | 45000.00 | 1077.41 |
| 318.15 | 45000.00 | 1072.41 |
| 323.15 | 45000.00 | 1067.38 |
| 328.15 | 45000.00 | 1062.36 |
| 333.15 | 45000.00 | 1057.32 |
| 338.15 | 45000.00 | 1052.28 |
| 283.15 | 50000.00 | 1110.71 |
| 288.15 | 50000.00 | 1105.72 |
| 293.15 | 50000.00 | 1100.7 |
| 298.15 | 50000.00 | 1095.73 |
| 303.15 | 50000.00 | 1090.79 |
| 308.15 | 50000.00 | 1085.8 |
| 313.15 | 50000.00 | 1080.86 |
| 318.15 | 50000.00 | 1075.92 |
| 323.15 | 50000.00 | 1070.98 |
| 328.15 | 50000.00 | 1066.05 |
| 333.15 | 50000.00 | 1061.09 |
| 338.15 | 50000.00 | 1056.13 |
| 283.15 | 55000.00 | 1113.62 |
| 288.15 | 55000.00 | 1108.7 |
| 293.15 | 55000.00 | 1103.77 |
| 298.15 | 55000.00 | 1098.86 |
| 303.15 | 55000.00 | 1093.96 |
| 308.15 | 55000.00 | 1089.07 |
| 313.15 | 55000.00 | 1084.2 |
| 318.15 | 55000.00 | 1079.33 |
| 323.15 | 55000.00 | 1074.48 |
| 328.15 | 55000.00 | 1069.6 |
| 333.15 | 55000.00 | 1064.72 |
| 338.15 | 55000.00 | 1059.87 |
| 283.15 | 60000.00 | 1116.47 |
| 288.15 | 60000.00 | 1111.61 |
| 293.15 | 60000.00 | 1106.72 |
| 298.15 | 60000.00 | 1101.89 |
| 303.15 | 60000.00 | 1097.06 |
| 308.15 | 60000.00 | 1092.23 |
| 313.15 | 60000.00 | 1087.42 |
| 318.15 | 60000.00 | 1082.65 |
| 323.15 | 60000.00 | 1077.86 |
| 328.15 | 60000.00 | 1073.07 |
| 333.15 | 60000.00 | 1068.26 |
| 338.15 | 60000.00 | 1063.48 |
| 283.15 | 65000.00 | 1119.27 |
| 288.15 | 65000.00 | 1114.44 |
| 293.15 | 65000.00 | 1109.63 |
| 298.15 | 65000.00 | 1104.85 |
| 303.15 | 65000.00 | 1100.09 |
| 308.15 | 65000.00 | 1095.31 |
| 313.15 | 65000.00 | 1090.59 |
| 318.15 | 65000.00 | 1085.87 |
| 323.15 | 65000.00 | 1081.13 |
| 328.15 | 65000.00 | 1076.42 |
| 333.15 | 65000.00 | 1071.7 |
| 338.15 | 65000.00 | 1066.99 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.19; 5693.44] | kPa | [234.94; 579.35] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42640e+01 | |||
| Coefficient B | -2.98618e+03 | |||
| Coefficient C | -4.77130e+01 | |||
| Temperature range, min. | 234.94 | |||
| Temperature range, max. | 579.35 | |||
| Pvap | 0.19 | kPa | 234.94 | Calculated Property |
| Pvap | 2.78 | kPa | 273.21 | Calculated Property |
| Pvap | 18.96 | kPa | 311.48 | Calculated Property |
| Pvap | 79.60 | kPa | 349.74 | Calculated Property |
| Pvap | 241.98 | kPa | 388.01 | Calculated Property |
| Pvap | 587.51 | kPa | 426.28 | Calculated Property |
| Pvap | 1212.04 | kPa | 464.55 | Calculated Property |
| Pvap | 2213.77 | kPa | 502.81 | Calculated Property |
| Pvap | 3682.68 | kPa | 541.08 | Calculated Property |
| Pvap | 5693.44 | kPa | 579.35 | Calculated Property |
| Pvap | [0.19; 5690.84] | kPa | [234.94; 579.35] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.19473e+01 | |||
| Coefficient B | -6.84652e+03 | |||
| Coefficient C | -1.00558e+01 | |||
| Coefficient D | 7.42178e-06 | |||
| Temperature range, min. | 234.94 | |||
| Temperature range, max. | 579.35 | |||
| Pvap | 0.19 | kPa | 234.94 | Calculated Property |
| Pvap | 2.79 | kPa | 273.21 | Calculated Property |
| Pvap | 19.16 | kPa | 311.48 | Calculated Property |
| Pvap | 79.87 | kPa | 349.74 | Calculated Property |
| Pvap | 238.99 | kPa | 388.01 | Calculated Property |
| Pvap | 570.14 | kPa | 426.28 | Calculated Property |
| Pvap | 1161.50 | kPa | 464.55 | Calculated Property |
| Pvap | 2117.24 | kPa | 502.81 | Calculated Property |
| Pvap | 3568.04 | kPa | 541.08 | Calculated Property |
| Pvap | 5690.84 | kPa | 579.35 | Calculated Property |
Similar Compounds
Find more compounds similar to Thiophene.
Mixtures
- Carbon dioxide + Thiophene
- Thiophene + Pentane, 2,2,4-trimethyl-
- Thiophene + Propane, 2-ethoxy-2-methyl-
- Thiophene + Heptane
- Thiophene + Butane, 2-methyl-
- Thiophene + 1-Butene, 2,3-dimethyl-
- Thiophene + 2-Butene, 2,3-dimethyl-
- Thiophene + Cyclohexane
- n-Hexane + Thiophene
- Thiophene + Octane
- Toluene + Thiophene
- 1-Hexene + Thiophene
- Butane + Thiophene
- Thiophene + Isobutane
- 1-Propene, 2-methyl- + Thiophene
- Thiophene + 2-Butene, (E)-
- Thiophene + Dimethyl ether
- Thiophene + Water
- 1,2-Ethanediol + Thiophene + Tetramethylammonium chloride
- Thiophene + Tetramethylammonium chloride + Glycerin
Find more mixtures with Thiophene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Solubility of thiopene in carbon dioxide and carbon dioxide + 1-propanol mixtures at temperatures from 313 to 363K
- High pressure vapor liquid equilibria for the systems thiophene + nonane +CO2, and thiophene + decane +CO2
- Compressed liquid densities and excess volumes of CO2 + thiophene binary mixtures from 313 to 363 K and pressures up to 25 MPa
- Infinite dilution activity coefficient measurements by inert gas stripping method
- Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
- Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
- Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
- Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Ionic liquids on desulfurization of fuel oils
- Liquid-liquid equilibrium and interfacial tension of the ternary system heptane + thiophene + 1-ethyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Influence of the ionic liquid structure on thiophene solubility
- Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
- Isobaric vapor-liquid equilibrium for four binary systems of thiophene
- Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + thiophene + n-heptane. The influence of cation structure
- Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
- Isobaric vapor-liquid equilibrium for systems containing sulfur compounds
- Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
- Separation of benzene and thiophene with a mixture of N-methyl-2- pyrrolidinone (NMP) and ionic liquid as the entrainer
- Phase diagrams of binary systems containing tricyanomethanide-based ionic liquids and thiophene or pyridine - new experimental data and PC-SAFT modeling
- Novel liquid-liquid equilibrium data for six ternary systems containing IL, hydrocarbon and thiophene at 25 C
- Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
- 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
- Effect of cation alkyl chain length on liquid-liquid equilibria of {ionic liquids + thiophene + heptane}: COSMO-RS prediction and experimental verification
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Liquid-liquid equilibrium data for extractive desulfurization using 1-butyl-3-methyl imidazolium thiocyanate, n-alkane and thiophene
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- Extraction of benzothiazole and thiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive denitrogenation and desulfurization agents
- 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
- Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- (Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
- Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Evaluation of the polysubstituted pyridinium ionic liquid [hmmpy][Ntf2] as a suitable solvent for desulfurization: Phase equilibria
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- 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
- Interactions of volatile organic compounds with 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 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
- Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl)phosphate based ionic liquids + thiophene + heptane}
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- 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
- Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- 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
- Separation of thiophene from heptane with ionic liquids
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Quaternary (liquid +liquid) equilibria for systems of imidazolium based ionic liquid + thiophene + pyridine + cyclohexane at 298.15 K: Experiments and quantum chemical predictions
- Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
- 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
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Solvent extraction of aromatic sulfur compounds from n-heptane using the 1-ethyl-3-methylimidazolium tricyanomethanide ionic liquid
- 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
- Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
- Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
- Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
- Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Extraction desulfurization process of fuels with ionic liquids
- Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl) phosphate based ionic liquids + thiophene + heptane}: Part 2
- Phase equilibria study of binary systems comprising an (ionic liquid + hydrocarbon)
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- 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
- Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
- 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
- Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
- Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
- 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
- Densities at high pressures and derived properties of thiophenes
- 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
- Liquid-liquid extraction of sulfur compounds from heptane with tricyanomethanide based ionic liquids
- Ternary liquid-liquid phase equilibria of {ionic liquid + thiophene + (octane/hexadecane)}
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
- Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
- Effect of the Type of Ammonium Salt on the Extractive Desulfurization of Fuels Using Deep Eutectic Solvents
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Experimental Measurements and Modeling Study of Liquid-Liquid Equilibrium [(Water + Methyl Oleate + Model Molecules of Tar Issued from the Biomass Gasification Process (Benzene, Toluene, Phenol, Thiophene, and Pyridine)]
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Experimental Determination of the Solubility of Thiophene in Carbon Dioxide and in Carbon Dioxide + Ethanol
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
- Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
- 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
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
- Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
- Measurement and Correlation of Liquid-Liquid Equilibria of Two Imidazolium Ionic Liquids with Thiophene and Methylcyclohexane
- Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
- Liquid-Liquid Equilibria of Ternary Systems Sulfide + Octane + Solvents at Different Temperatures
- 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
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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