GB810017A - Improvements in and relating to the manufacture of methyl sulphide and methyl mercaptan - Google Patents

Improvements in and relating to the manufacture of methyl sulphide and methyl mercaptan

Info

Publication number
GB810017A
GB810017A GB566157A GB566157A GB810017A GB 810017 A GB810017 A GB 810017A GB 566157 A GB566157 A GB 566157A GB 566157 A GB566157 A GB 566157A GB 810017 A GB810017 A GB 810017A
Authority
GB
United Kingdom
Prior art keywords
methyl
sulphide
mercaptan
oxide
methyl mercaptan
Prior art date
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.)
Expired
Application number
GB566157A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to GB566157A priority Critical patent/GB810017A/en
Publication of GB810017A publication Critical patent/GB810017A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C321/00Thiols, sulfides, hydropolysulfides or polysulfides

Abstract

Methyl mercaptan is prepared by passing hydrogen sulphide, methanol vapour and methyl sulphide together through a fluid bed of a metal oxide catalyst consisting of activated alumina, thorium oxide, zirconium oxide, uranium oxide, chromium oxide or the blue oxide of molybdenum or tungsten at a temperature between 400 DEG and 450 DEG C. and separating the resulting methyl mercaptan from the methyl sulphide by rectification and recycling the methyl sulphide to the reaction zone. Methyl sulphide is prepared in like manner by passing hydrogen sulphide, methanol vapour and methyl mercaptan through the fluid bed of catalyst at between 400 DEG and 450 DEG C., separating the resulting methyl sulphide from the methyl mercaptan by rectification and recycling the methyl mercaptan to the reaction zone. Examples are given of each process utilizing an illustrated form of apparatus wherein methanol vapour, excess hydrogen sulphide and recycled methyl sulphide or mercaptan are passed into the bottom of a fluid bed of activated alumina catalyst at 400-450 DEG C., the effluent product stream is cooled to strip-out by-product water and any unchanged methanol and then fractionated to separate the methyl sulphide from the methyl mercaptan and one is withdrawn from the system as the desired product and the other is recycled to the reaction zone. Reference has been directed by the Comptroller to Specification 773,697.
GB566157A 1957-02-19 1957-02-19 Improvements in and relating to the manufacture of methyl sulphide and methyl mercaptan Expired GB810017A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB566157A GB810017A (en) 1957-02-19 1957-02-19 Improvements in and relating to the manufacture of methyl sulphide and methyl mercaptan

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB566157A GB810017A (en) 1957-02-19 1957-02-19 Improvements in and relating to the manufacture of methyl sulphide and methyl mercaptan

Publications (1)

Publication Number Publication Date
GB810017A true GB810017A (en) 1959-03-04

Family

ID=9800262

Family Applications (1)

Application Number Title Priority Date Filing Date
GB566157A Expired GB810017A (en) 1957-02-19 1957-02-19 Improvements in and relating to the manufacture of methyl sulphide and methyl mercaptan

Country Status (1)

Country Link
GB (1) GB810017A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0850922A1 (en) * 1996-12-27 1998-07-01 Degussa Aktiengesellschaft Process for the continuous preparation of methyl mercaptan
CN112552217A (en) * 2020-12-26 2021-03-26 查都(海南)科技有限公司 Methyl mercaptan purification device
CN114728896A (en) * 2019-10-04 2022-07-08 阿科玛法国公司 Method for producing mercaptans by hydrogenolysis of thioethers

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0850922A1 (en) * 1996-12-27 1998-07-01 Degussa Aktiengesellschaft Process for the continuous preparation of methyl mercaptan
US5886230A (en) * 1996-12-27 1999-03-23 Degussa Aktiengesellschaft Process for continuous production of methyl mercaptan
CN114728896A (en) * 2019-10-04 2022-07-08 阿科玛法国公司 Method for producing mercaptans by hydrogenolysis of thioethers
CN112552217A (en) * 2020-12-26 2021-03-26 查都(海南)科技有限公司 Methyl mercaptan purification device

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