- InChI
- InChI=1S/C4H8O2S/c5-7(6)3-1-2-4-7/h1-4H2
- InChI Key
- HXJUTPCZVOIRIF-UHFFFAOYSA-N
- Formula
- C4H8O2S
- SMILES
- O=S1(=O)CCCC1
- Molecular Weight1
- 120.17
- CAS
- 126-33-0
- Other Names
-
- 1,1-Dioxide tetrahydrothiofuran
- 1,1-Dioxidetetrahydrothiophene
- 1,1-Dioxothiolan
- 2,3,4,5-Tetrahydrothiophene-1,1-dioxide
- BONDELANE A
- Bondolane A
- CYCLIC TETRAMETHYLENE SULFONE
- Cyclotetramethylene sulfone
- Dihydrobutadiene sulfone
- Dihydrobutadiene sulphone
- Dioxothiolan
- NSC 46443
- Sulfalone
- Sulfolan
- Sulfolane
- Sulpholane
- Sulphoxaline
- TETRAHYDROTHIOPHENE DIOXIDE
- Tetrahydothiophene-1,1-dioxide
- Tetrahydrothiofen-1,1-dioxid
- Tetrahydrothiophene 1,1-dioxide
- Tetramethylene sulfone
- Thiacyclopentane dioxide
- Thiocyclopentane-1,1-dioxide
- Thiolane-1,1-dioxide
- Thiophan sulfone
- Thiophane 1,1-dioxide
- Thiophane dioxide
- Thiophene, 1,1-dioxide-tetrahydro-
- thiolane 1,1-dioxide
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (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 |
|---|---|---|---|
| ΔfG° | -434.74 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -495.03 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 9.88 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 42.69 | kJ/mol | Joback Calculated Property |
| log10WS | -0.23 | Crippen Calculated Property | |
| logPoct/wat | 0.195 | Crippen Calculated Property | |
| McVol | 84.450 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 6328.92 | kPa | Joback Calculated Property |
| Tboil | 560.48 | K | Isobari... |
| Tc | 521.90 | K | Joback Calculated Property |
| Tfus | 237.59 | K | Joback Calculated Property |
| Vc | 0.320 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [130.22; 189.37] | J/mol×K | [337.70; 521.90] | 
|
|
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 190 350 400 450 500 | ||||
| Cp,gas | 130.22 | J/mol×K | 337.70 | Joback Calculated Property |
| Cp,gas | 141.38 | J/mol×K | 368.40 | Joback Calculated Property |
| Cp,gas | 151.99 | J/mol×K | 399.10 | Joback Calculated Property |
| Cp,gas | 162.09 | J/mol×K | 429.80 | Joback Calculated Property |
| Cp,gas | 171.68 | J/mol×K | 460.50 | Joback Calculated Property |
| Cp,gas | 180.77 | J/mol×K | 491.20 | Joback Calculated Property |
| Cp,gas | 189.37 | J/mol×K | 521.90 | Joback Calculated Property |
| Cp,liquid | [179.50; 213.66] | J/mol×K | [303.15; 372.20] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 180 185 190 195 200 205 210 215 320 340 360 | ||||
| Cp,liquid | 181.50 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 182.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 179.90 | J/mol×K | 304.04 | Recomme... |
| Cp,liquid | 179.50 | J/mol×K | 304.04 | Recomme... |
| Cp,liquid | 184.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 182.42 | J/mol×K | 308.20 | Thermal... |
| Cp,liquid | 181.30 | J/mol×K | 309.14 | Recomme... |
| Cp,liquid | 181.60 | J/mol×K | 309.15 | Recomme... |
| Cp,liquid | 183.50 | J/mol×K | 312.20 | Thermal... |
| Cp,liquid | 185.10 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 185.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 182.60 | J/mol×K | 314.25 | Recomme... |
| Cp,liquid | 183.80 | J/mol×K | 314.25 | Recomme... |
| Cp,liquid | 184.70 | J/mol×K | 316.20 | Thermal... |
| Cp,liquid | 186.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 184.50 | J/mol×K | 319.35 | Recomme... |
| Cp,liquid | 184.70 | J/mol×K | 319.35 | Recomme... |
| Cp,liquid | 185.90 | J/mol×K | 320.20 | Thermal... |
| Cp,liquid | 188.70 | J/mol×K | 323.15 | Heat Ca... |
| Cp,liquid | 188.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 187.11 | J/mol×K | 324.20 | Thermal... |
| Cp,liquid | 184.40 | J/mol×K | 324.46 | Recomme... |
| Cp,liquid | 185.30 | J/mol×K | 324.46 | Recomme... |
| Cp,liquid | 189.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 188.79 | J/mol×K | 328.20 | Thermal... |
| Cp,liquid | 187.40 | J/mol×K | 329.56 | Recomme... |
| Cp,liquid | 186.60 | J/mol×K | 329.56 | Recomme... |
| Cp,liquid | 190.47 | J/mol×K | 332.20 | Thermal... |
| Cp,liquid | 191.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 192.30 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 188.70 | J/mol×K | 334.66 | Recomme... |
| Cp,liquid | 187.90 | J/mol×K | 334.67 | Recomme... |
| Cp,liquid | 192.39 | J/mol×K | 336.20 | Thermal... |
| Cp,liquid | 193.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 188.50 | J/mol×K | 339.77 | Recomme... |
| Cp,liquid | 189.70 | J/mol×K | 339.77 | Recomme... |
| Cp,liquid | 194.32 | J/mol×K | 340.20 | Thermal... |
| Cp,liquid | 194.30 | J/mol×K | 343.15 | Heat Ca... |
| Cp,liquid | 194.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 196.36 | J/mol×K | 344.20 | Thermal... |
| Cp,liquid | 190.20 | J/mol×K | 344.88 | Recomme... |
| Cp,liquid | 190.20 | J/mol×K | 344.88 | Recomme... |
| Cp,liquid | 197.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 198.52 | J/mol×K | 348.20 | Thermal... |
| Cp,liquid | 192.00 | J/mol×K | 349.98 | Recomme... |
| Cp,liquid | 192.50 | J/mol×K | 349.98 | Recomme... |
| Cp,liquid | 200.81 | J/mol×K | 352.20 | Thermal... |
| Cp,liquid | 197.80 | J/mol×K | 353.15 | Heat Ca... |
| Cp,liquid | 199.00 | J/mol×K | 353.15 | Molar H... |
| Cp,liquid | 193.40 | J/mol×K | 355.09 | Recomme... |
| Cp,liquid | 192.30 | J/mol×K | 355.09 | Recomme... |
| Cp,liquid | 203.21 | J/mol×K | 356.20 | Thermal... |
| Cp,liquid | 205.73 | J/mol×K | 360.20 | Thermal... |
| Cp,liquid | 208.26 | J/mol×K | 364.20 | Thermal... |
| Cp,liquid | 210.90 | J/mol×K | 368.20 | Thermal... |
| Cp,liquid | 213.66 | J/mol×K | 372.20 | Thermal... |
| η | [0.0014150; 0.0102280] | Pa×s | [303.15; 423.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 350 400 | ||||
| η | 0.0100700 | Pa×s | 303.15 | Densiti... |
| η | 0.0100742 | Pa×s | 303.15 | Excess ... |
| η | 0.0102280 | Pa×s | 303.15 | Viscome... |
| η | 0.0100304 | Pa×s | 303.15 | Densiti... |
| η | 0.0087947 | Pa×s | 308.15 | Densiti... |
| η | 0.0090460 | Pa×s | 308.15 | Viscome... |
| η | 0.0091940 | Pa×s | 308.20 | Phase e... |
| η | 0.0078080 | Pa×s | 313.15 | Densiti... |
| η | 0.0078440 | Pa×s | 313.15 | Viscome... |
| η | 0.0078365 | Pa×s | 313.15 | Densiti... |
| η | 0.0081160 | Pa×s | 313.20 | Phase e... |
| η | 0.0065740 | Pa×s | 318.15 | Viscome... |
| η | 0.0072010 | Pa×s | 318.20 | Phase e... |
| η | 0.0061750 | Pa×s | 323.15 | Viscome... |
| η | 0.0061940 | Pa×s | 323.15 | Densiti... |
| η | 0.0061936 | Pa×s | 323.15 | Excess ... |
| η | 0.0064390 | Pa×s | 323.20 | Phase e... |
| η | 0.0051910 | Pa×s | 328.15 | Viscome... |
| η | 0.0057720 | Pa×s | 328.20 | Phase e... |
| η | 0.0048870 | Pa×s | 333.15 | Viscome... |
| η | 0.0050090 | Pa×s | 333.15 | Densiti... |
| η | 0.0051990 | Pa×s | 333.20 | Phase e... |
| η | 0.0043100 | Pa×s | 338.15 | Viscome... |
| η | 0.0047140 | Pa×s | 338.20 | Phase e... |
| η | 0.0042140 | Pa×s | 343.15 | Viscome... |
| η | 0.0041260 | Pa×s | 343.15 | Densiti... |
| η | 0.0042680 | Pa×s | 343.20 | Phase e... |
| η | 0.0035310 | Pa×s | 353.15 | Viscome... |
| η | 0.0034400 | Pa×s | 353.15 | Densiti... |
| η | 0.0030110 | Pa×s | 363.15 | Viscome... |
| η | 0.0025760 | Pa×s | 373.15 | Viscome... |
| η | 0.0022530 | Pa×s | 383.15 | Viscome... |
| η | 0.0019870 | Pa×s | 393.15 | Viscome... |
| η | 0.0017610 | Pa×s | 403.15 | Viscome... |
| η | 0.0015710 | Pa×s | 413.15 | Viscome... |
| η | 0.0014150 | Pa×s | 423.15 | Viscome... |
| Pvap | [0.01; 4144.00] | kPa | [333.15; 829.00] |
|
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 400 600 800 | ||||
| Pvap | 0.01 | kPa | 333.15 | Vapor l... |
| Pvap | 0.04 | kPa | 353.15 | Vapor l... |
| Pvap | 103.60 | kPa | 560.20 | Critica... |
| Pvap | 203.90 | kPa | 594.40 | Critica... |
| Pvap | 350.20 | kPa | 626.30 | Critica... |
| Pvap | 556.80 | kPa | 656.30 | Critica... |
| Pvap | 829.20 | kPa | 685.10 | Critica... |
| Pvap | 1181.00 | kPa | 713.20 | Critica... |
| Pvap | 1665.00 | kPa | 742.00 | Critica... |
| Pvap | 2363.00 | kPa | 773.40 | Critica... |
| Pvap | 3185.00 | kPa | 802.70 | Critica... |
| Pvap | 4144.00 | kPa | 829.00 | Critica... |
| n0 | [1.48150; 1.48230] | [303.15; 303.15] |
|
|
| n0 | 1.48230 | 303.15 | Phase e... | |
| n0 | 1.48150 | 303.15 | (Liquid... | |
| ρl | [1206.00; 1266.40] | kg/m3 | [298.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 1200 1210 1220 1230 1240 1250 1260 1270 300 320 340 360 | ||||
| ρl | 1266.40 | kg/m3 | 298.15 | Experim... |
| ρl | 1265.75 | kg/m3 | 303.15 | Measure... |
| ρl | 1262.00 | kg/m3 | 303.15 | Measuri... |
| ρl | 1260.10 | kg/m3 | 303.15 | Volumet... |
| ρl | 1262.90 | kg/m3 | 303.15 | Density... |
| ρl | 1259.40 | kg/m3 | 303.15 | Experim... |
| ρl | 1255.70 | kg/m3 | 308.15 | Volumet... |
| ρl | 1251.30 | kg/m3 | 313.15 | Volumet... |
| ρl | 1253.00 | kg/m3 | 313.15 | Measuri... |
| ρl | 1254.10 | kg/m3 | 313.15 | Density... |
| ρl | 1251.70 | kg/m3 | 313.15 | Experim... |
| ρl | 1244.00 | kg/m3 | 323.15 | Measuri... |
| ρl | 1245.20 | kg/m3 | 323.15 | Density... |
| ρl | 1244.00 | kg/m3 | 323.15 | Experim... |
| ρl | 1235.40 | kg/m3 | 333.15 | Experim... |
| ρl | 1236.60 | kg/m3 | 333.15 | Density... |
| ρl | 1235.00 | kg/m3 | 333.15 | Measuri... |
| ρl | 1225.00 | kg/m3 | 343.15 | Experim... |
| ρl | 1226.00 | kg/m3 | 343.15 | Measuri... |
| ρl | 1228.10 | kg/m3 | 343.15 | Density... |
| ρl | 1215.00 | kg/m3 | 353.15 | Experim... |
| ρl | 1218.00 | kg/m3 | 353.15 | Measuri... |
| ρl | 1206.00 | kg/m3 | 363.15 | Experim... |
| ρl | 1209.00 | kg/m3 | 363.15 | Measuri... |
| csound,fluid | [1558.00; 1588.00] | m/s | [303.15; 313.15] |
|
| csound,fluid | 1588.00 | m/s | 303.15 | Densiti... |
| csound,fluid | 1576.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1558.00 | m/s | 313.15 | Densiti... |
| γ | [0.05; 0.05] | N/m | [303.15; 343.15] |
|
|
T(K) Surface Tension (N/m) 0.05 0.05 0.05 0.05 0.05 0.05 0.05 310 320 330 340 | ||||
| γ | 0.05 | N/m | 303.15 | Densiti... |
| γ | 0.05 | N/m | 313.15 | Densiti... |
| γ | 0.05 | N/m | 323.15 | Densiti... |
| γ | 0.05 | N/m | 333.15 | Densiti... |
| γ | 0.05 | N/m | 343.15 | Densiti... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [416.57; 592.15] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.51896e+01 | |||
| Coefficient B | -5.14444e+03 | |||
| Coefficient C | -7.13560e+01 | |||
| Temperature range, min. | 416.57 | |||
| Temperature range, max. | 592.15 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
| Pvap | 1.33 | kPa | 416.57 | Calculated Property |
| Pvap | 2.96 | kPa | 436.08 | Calculated Property |
| Pvap | 6.05 | kPa | 455.59 | Calculated Property |
| Pvap | 11.56 | kPa | 475.10 | Calculated Property |
| Pvap | 20.80 | kPa | 494.61 | Calculated Property |
| Pvap | 35.54 | kPa | 514.11 | Calculated Property |
| Pvap | 58.03 | kPa | 533.62 | Calculated Property |
| Pvap | 91.06 | kPa | 553.13 | Calculated Property |
| Pvap | 137.98 | kPa | 572.64 | Calculated Property |
| Pvap | 202.66 | kPa | 592.15 | Calculated Property |
| Pvap | [8.05e-04; 5105.08] | kPa | [300.75; 849.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.04677e+02 | |||
| Coefficient B | -1.21143e+04 | |||
| Coefficient C | -1.26025e+01 | |||
| Coefficient D | 4.33097e-06 | |||
| Temperature range, min. | 300.75 | |||
| Temperature range, max. | 849.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 400 600 800 | ||||
| Pvap | 8.05e-04 | kPa | 300.75 | Calculated Property |
| Pvap | 0.08 | kPa | 361.67 | Calculated Property |
| Pvap | 1.79 | kPa | 422.58 | Calculated Property |
| Pvap | 15.45 | kPa | 483.50 | Calculated Property |
| Pvap | 74.95 | kPa | 544.42 | Calculated Property |
| Pvap | 250.31 | kPa | 605.33 | Calculated Property |
| Pvap | 651.69 | kPa | 666.25 | Calculated Property |
| Pvap | 1433.40 | kPa | 727.17 | Calculated Property |
| Pvap | 2811.47 | kPa | 788.08 | Calculated Property |
| Pvap | 5105.08 | kPa | 849.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Thiophene, tetrahydro-, 1,1-dioxide.
Mixtures
- Ethanol, 2,2'-oxybis- + Thiophene, tetrahydro-, 1,1-dioxide
- Triethylene glycol + Thiophene, tetrahydro-, 1,1-dioxide
- Diethanolamine + Thiophene, tetrahydro-, 1,1-dioxide
- Monoethanolamine + Thiophene, tetrahydro-, 1,1-dioxide
- Benzene, 1,3-dimethyl- + Thiophene, tetrahydro-, 1,1-dioxide
- o-Xylene + Thiophene, tetrahydro-, 1,1-dioxide
- Toluene + Decane + Thiophene, tetrahydro-, 1,1-dioxide
- Acetic acid + Pentane + Thiophene, tetrahydro-, 1,1-dioxide
- Pentane + Propanoic acid + Thiophene, tetrahydro-, 1,1-dioxide
- Butanoic acid + Pentane + Thiophene, tetrahydro-, 1,1-dioxide
- Pentane + Propanoic acid, 2-methyl- + Thiophene, tetrahydro-, 1,1-dioxide
- Pentane + Pentanoic acid + Thiophene, tetrahydro-, 1,1-dioxide
- Butanoic acid, 3-methyl- + Pentane + Thiophene, tetrahydro-, 1,1-dioxide
- Toluene + Thiophene, tetrahydro-, 1,1-dioxide
- Ethylbenzene + Thiophene, tetrahydro-, 1,1-dioxide
- Benzene, (1-methylethyl)- + Thiophene, tetrahydro-, 1,1-dioxide
- Carbon dioxide + Thiophene, tetrahydro-, 1,1-dioxide
- Hydrogen sulfide + Thiophene, tetrahydro-, 1,1-dioxide
- Acetic acid + Heptane + Thiophene, tetrahydro-, 1,1-dioxide
- Heptane + Propanoic acid + Thiophene, tetrahydro-, 1,1-dioxide
Find more mixtures with Thiophene, tetrahydro-, 1,1-dioxide.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Liquid liquid equilibria for the binary systems of sulfolane with branched cycloalkanes
- Ternary liquid liquid equilibria for mixtures of toluene + n-heptane + an ionic liquid
- Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
- Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
- Recommended vapor pressures for thiophene, sulfolane, and dimethyl sulfoxide
- Extraction of benzene, ethylbenzene, and xylenes from n-heptane using binary mixtures of [4empy][Tf2N] and [emim][DCA] ionic liquids
- Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
- Phase equilibria measurements of ternary mixtures (sulfolane + a carboxylic acid + pentane) at 303.15 K
- Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
- (Liquid + liquid) equilibria of ternary and quaternary systems containing n-hexane, toluene, m-xylene, propanol, sulfolane, and water at T = 303.15 K
- (Liquid + liquid) equilibria of (sulfolane + benzene + n-hexane), (N-formylmorpholine + benzene + n-hexane), and (sulfolane + N-formylmorpholine + benzene + n-hexane) at temperatures ranging from (298.15 to 318.15) K: Experimental results and correlation
- Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
- Phase equilibria of toluene/heptane with deep eutectic solvents based on ethyltriphenylphosphonium iodide for the potential use in the separation of aromatics from naphtha
- Measuring the solubility of CO2 and H2S in sulfolane and the density and viscosity of saturated liquid binary mixtures of (sulfolane + CO2) and (sulfolane + H2S)
- (Liquid + liquid) equilibria measurements for ternary systems (sulfolane + a carboxylic acid + n-heptane) at T = 303.15 K and at 0.1 MPa
- Volumetric and transport properties of binary liquid mixtures of sulfolane with aniline, N,N-dimethylaniline and N,N-diethylaniline at different temperatures and atmospheric pressure
- Experimental investigation of hydrogen sulfide solubility in aqueous sulfolane solution
- Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
- Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
- Carbon dioxide solubility in aqueous sulfolane solution
- Simultaneous solubility measurement of (ethyl mercaptan + carbon dioxide) into the aqueous solutions of (N-methyl diethanolamine + sulfolane + water)
- Heat Capacity, Thermal Conductivity and Thermal Diffusivity of Aqueous Sulfolane Solutions
- Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
- Experimental Solubility of Carbonyl Sulfide in Sulfolane and gamma-butyrolactone
- Thermodynamic Modeling and Solubility Measurement of Cetirizine Hydrochloride and Deferiprone in Pure Solvents of Acetonitrile, Ethanol, Acetic Acid, Sulfolane, and Ethyl Acetate and Their Mixtures
- Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
- Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + Sulfolane and Methanol + N-Methyl-2-pyrrolidone (NMP)
- Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
- Liquid-Liquid Equilibria for Cyclohexane + Ethylbenzene + Sulfolane at (303.15, 313.15, and 323.15) K
- Liquid-Liquid Equilibria for the Binary Systems of Sulfolane with Cycloalkanes
- Ternary Liquid-Liquid Equilibria for Systems of (Sulfolane + Toluene or Chloronaphthalene + Octane)
- Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
- Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method
- Vapor-Liquid Equilibria and Density Measurement for Binary Mixtures of Benzene + Nonane, Methylbenzene + 1,2-Dimethylbenzene, 1,3-Dimethylbenzene + 2,3,4,5-Tetrahydrothiophene-1,1-dioxide (Sulfolane), 1,2-Dimethylbenzene + Sulfolane, 1,2-Dimethylbenzene + N-Methylformamide (NMF), 1,3-Dimethylbenzene + NMF, and 1,4-Dimethylbenzene + NMF from (333.15 to 353.15) K at Vacuum Conditions
- Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
- Densities, Viscosities, and Surface Tensions of Aqueous Mixtures of Sulfolane + Triethanolamine and Sulfolane + Diisopropanolamine
- Liquid Liquid Equilibria of Alkane (C10 C14) + sec-Butylbenzene + Sulfolane
- Liquid Liquid Equilibria of the Ternary Systems Undecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide and Tridecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide at T = (323.15, 348.15, and 373.15) K
- Thermal Properties of Cyano-Based Ionic Liquids
- Comparative Study of the Solubilities of SO2 in Five Low Volatile Organic Solvents (Sulfolane, Ethylene Glycol, Propylene Carbonate, N-Methylimidazole, and N-Methylpyrrolidone)
- Liquid Liquid Extraction of Toluene from n-Alkanes using {[4empy][Tf2N] + [emim][DCA]} Ionic Liquid Mixtures
- Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
- Liquid-Liquid Equilibria of Alkane (C10-C14) + Hexylbenzene + Sulfolane
- Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
- Liquid - Liquid Equilibria for the Binary Systems of Sulfolane with Alkanes
- Influence of the Temperature on the Liquid Liquid Equilibria of Heptane + Toluene + Sulfolane and Heptane + m-Xylene + Sulfolane
- Liquid-Liquid Equilibria of Ternary Systems Sulfide + Octane + Solvents at Different Temperatures
- Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Sulfolane with Ethyl Acetate, n-Propyl Acetate, and n-Butyl Acetate at Temperature of (303.15, 308.15, and 313.15) K
- Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
- Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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