- 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
- ω : Acentric Factor.
- 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).
- 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).
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3914 | Relay (1.0) Calculated Property | |
| ΔfG° | -434.74 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -365.81 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 9.88 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 88.51 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.26 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.24 | Relay (1.0) 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 | Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa |
| Tc | 754.21 | K | Relay (1.0) Calculated Property |
| Tfus | 376.83 | K | Relay (1.0) Calculated Property |
| Vc | 0.286 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [416.57; 592.15] |
The Yaws Handbook of Vapor Pressure
|
| 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 | |||
| 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 Vapor Pressure Data
|
| 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 | |||
| 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
- Cheméo Relay (1.0)
- 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.