GB1054534A - - Google Patents

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Publication number
GB1054534A
GB1054534A GB1054534DA GB1054534A GB 1054534 A GB1054534 A GB 1054534A GB 1054534D A GB1054534D A GB 1054534DA GB 1054534 A GB1054534 A GB 1054534A
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United Kingdom
Prior art keywords
sulpholane
hydrocarbons
sulpholene
purified
carried out
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Publication of GB1054534A publication Critical patent/GB1054534A/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D333/00Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom
    • C07D333/02Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings
    • C07D333/46Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings substituted on the ring sulfur atom
    • C07D333/48Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings substituted on the ring sulfur atom by oxygen atoms

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1,054,534. Sulpholanes and their manufacture and purification. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. June 21. 1965. No. 26046/65. Heading C2C. A sulpholane is purified by subjecting it to an extractive treatment with an aliphatic hydrocarbon or mixture of aliphatic hydrocarbons, the term " aliphatic hydrocarbons " being used to include cycloaliphatic hydrocarbons. The hydrocarbons are preferably those which are at least partially immiscible with the sulpholane and which can be separated from the latter by distillation and one or more other compounds may also be present but the presence of aromatic hydrocarbons should be avoided. Specified solvents are cyclohexane and petroleum ether (B.P. 60-80‹ C.). The process is preferably carried out within the temperature range 20- 60‹ C. and in at least two stages. The purified sulpholane may be used as a solvent for the manufacture of a sulpholane, by reacting a 1: 3 alkadiene with sulphur dioxide to produce a sulpholene and catalytically hydrogenating the sulpholene. both steps of the process being carried out in the presence of the purified sulpholane. The hydrogenation may be carried out, in the case of 3-sulpholene, in the presence of Raney nickel and at 30‹ C. under a hydrogen pressure of 500 p.s.i.g. in a stirred autoclave.
GB1054534D Active GB1054534A (en)

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ID=1758183

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0103824A2 (en) * 1982-09-20 1984-03-28 Dow Corning Corporation Separation of chlorosilanes
FR2569695A1 (en) * 1984-08-31 1986-03-07 El Paso Products Co PROCESS FOR THE PURIFICATION OF SULFOLANE USE FROM A PROCESS FOR OBTAINING TERTIO-BUTYLSTYRENE

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0103824A2 (en) * 1982-09-20 1984-03-28 Dow Corning Corporation Separation of chlorosilanes
EP0103824A3 (en) * 1982-09-20 1985-11-21 Dow Corning Corporation Separation of chlorosilanes
FR2569695A1 (en) * 1984-08-31 1986-03-07 El Paso Products Co PROCESS FOR THE PURIFICATION OF SULFOLANE USE FROM A PROCESS FOR OBTAINING TERTIO-BUTYLSTYRENE

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