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Sulfolane

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Sulfolane
Sulfolane
Sulfolane
Ball-and-stick model of the sulfolane molecule
Ball-and-stick model of the sulfolane molecule
Names
IUPAC name
Tetrahydrothiophene 1,1-dioxide
Other names
sulfolane
tetramethylene sulfone
Identifiers
3D model (JSmol)
ChEBI
ChemSpider
ECHA InfoCard 100.004.349 Edit this at Wikidata
UNII
  • InChI=1S/C4H8O2S/c5-7(6)3-1-2-4-7/h1-4H2 checkY
    Key: HXJUTPCZVOIRIF-UHFFFAOYSA-N checkY
  • InChI=1/C4H8O2S/c5-7(6)3-1-2-4-7/h1-4H2
    Key: HXJUTPCZVOIRIF-UHFFFAOYAA
  • C1CCS(=O)(=O)C1
Properties
C4H8O2S
Molar mass 120.17 g/mol
Appearance clear colorless liquid
Density 1.261 g/cm3, liquid
Melting point 27.5 °C (81.5 °F; 300.6 K)
Boiling point 285 °C (545 °F; 558 K)
miscible
Viscosity 0.01007 Pa·s at 25 °C
Structure
4.35 D
Hazards
NFPA 704 (fire diamond)
NFPA 704 four-colored diamondHealth 2: Intense or continued but not chronic exposure could cause temporary incapacitation or possible residual injury. E.g. chloroformFlammability 1: Must be pre-heated before ignition can occur. Flash point over 93 °C (200 °F). E.g. canola oilInstability (yellow): no hazard codeSpecial hazards (white): no code
2
1
Flash point 165 °C (329 °F; 438 K)
528 °C (982 °F; 801 K)
Related compounds
Related compounds
Methylsulfonylmethane

Tetrahydrothiophene
Sulfolene

Except where otherwise noted, data are given for materials in their standard state (at 25 °C [77 °F], 100 kPa).
☒N verify (what is checkY☒N ?)

Sulfolane (also tetramethylene sulfone, systematic name: 2,3,4,5-tetrahydrothiophene-1,1-dioxide) is an organosulfur compound, formally a cyclic sulfone, with the formula (CH2)4SO2. It is a colorless liquid commonly used in the chemical industry as a solvent for extractive distillation and chemical reactions. Sulfolane was originally developed by the Shell Oil Company in the 1960s as a solvent to purify butadiene. Sulfolane is a polar aprotic solvent, and it is readily soluble in water.

Properties

Sulfolane is classified as a sulfone, a group of organosulfur compounds containing a sulfonyl functional group. The sulfone group is a sulfur atom doubly bonded to two oxygen atoms and singly bonded to two carbon centers. The sulfur-oxygen double bond is polar, conferring good solubility in water, while the four carbon ring provides non-polar stability. These properties allow it to be miscible in both water and hydrocarbons, resulting in its widespread use as a solvent for purifying hydrocarbon mixtures.

Synthesis

The original method developed by the Shell Oil Company was to first allow butadiene to react with sulfur dioxide via a cheletropic reaction to give sulfolene. This was then hydrogenated using Raney nickel as a catalyst to give sulfolane.[1][2]

Shortly thereafter, it was discovered that both the product yield and the lifetime of the catalyst could be improved by adding hydrogen peroxide and then neutralizing to a pH of roughly 5-8 before hydrogenation. Developments have continued over the years, including in the catalysts used. Recently, it was found that Ni-B/MgO showed superior catalytic activity to that of Raney nickel and other common catalysts that have been used in the hydrogenation of sulfolene.

Other syntheses have also been developed, such as oxidizing tetrahydrothiophene with hydrogen peroxide. This reaction produces tetramethylene sulfoxide, which can then be further oxidized. Because the first oxidation occurs at low temperature and the second at higher temperature, the reaction can be controlled at each stage. This gives greater freedom for the manipulation of the reaction, which can potentially lead to higher yields and purity.

Uses

Sulfolane is widely used as an industrial solvent, especially in the extraction of aromatic hydrocarbons from hydrocarbon mixtures and to purify natural gas.[1] The first large scale commercial use of sulfolane, the sulfinol process, was first implemented by Shell Oil Company in March 1964 at the Person gas plant near Karnes City, Texas. The sulfinol process purifies natural gas by removing H2S, CO2, COS and mercaptans from natural gas with a mixture of alkanolamine and sulfolane.

Shortly after the sulfinol process was implemented, sulfolane was found to be highly effective in separating high purity aromatic compounds from hydrocarbon mixtures using liquid-liquid extraction. This process is widely used in refineries and the petrochemical industry. Because sulfolane is one of the most efficient industrial solvents for purifying aromatics, the process operates at a relatively low solvent-to-feed ratio, making sulfolane relatively cost effective compared to similar-purpose solvents. In addition, it is selective in a range that complements distillation; where sulfolane can’t separate two compounds, distillation easily can and vice versa, keeping sulfolane units useful for a wide range of compounds with minimal additional cost.

Whereas sulfolane is highly stable and can therefore be reused many times, it does eventually degrade into acidic byproducts. A number of measures have been developed to remove these byproducts, allowing the sulfolane to be reused and increase the lifetime of a given supply. Some methods that have been developed to regenerate spent sulfolane include vacuum and steam distillation, back extraction, adsorption, and anion-cation exchange resin columns.

Sulfolane is also added to hydrofluoric acid as a vapor suppressant[3], commonly for use in a refinery's alkylation unit. This "modified" hydrofluoric acid is less prone to vaporization if released in its liquid form.

See also

References

  1. ^ a b Hillis O. Folkins "Benzene" Ullmann’s Encyclopedia of Industrial Chemistry, Wiley-VCH, Weinheim, 2005.doi:10.1002/14356007.a03_475
  2. ^ Earl Clark, Kirk-Othmer Encyclopedia of Chemical Technology, "Sulfolane and Sulfones", John Wiley & Sons, NY, 1997
  3. ^ "Sulfolane Fact Sheet" (PDF). Chevron Phillips Chemical Company. {{cite web}}: Cite has empty unknown parameter: |dead-url= (help)
  • Young, Eldred E. (Shell International Research) BE Patent 616856, 1962
  • Goodenbour, John W.; Carlson, George J. (Shell International Research) BE Patent 611850, 1962
  • Ge, Shaohui; Wu, Zhijie; Zhang, Minghui; Li, Wei; Tao, Keyi.Industrial & Engineering Chemistry Research,200645(7), 2229-2234,
  • Sharipov, A. Kh.Russian Journal of Applied Chemistry2003,76(1), 108-113.
  • Dunn, C. L.; Freitas, E. R.; Hill, E. S.; Sheeler, J. E. R., Jr. Proc., Ann. Conv. Nat. Gas Processors Assoc. Am.,Tech. Papers1965,44 55-8
  • Broughton, Donald B.; Asselin, George F. UOP Process Div., Universal Oil Prod. Co., Des Plaines, IL, USA. World Petrol. Congr., Proc., 7th1968, Meeting Date 1967,4 65-73. Publisher: Elsevier Publ. Co. Ltd., Barking, Engl
  • Lal, Raj Kumar Jagadamba; Bhat, Sodankoor Garadi Thirumaleshwara. (Indian Petrochemicals Corp. Ltd., India). Eur. Pat. Appl. 1989-308019 (1991)
  • Van der Wiel, A.Nature1960,187 142-3.
  • Block, E.Reactions of Organosulfur Compounds; Academic: New York, 1978
  • Belen'kii, L.I.Chemistry of Organosulfur Compounds; Horwood: New York, 1990