GB913836A - Improvements in and relating to the synthesis of hydrogen cyanide - Google Patents

Improvements in and relating to the synthesis of hydrogen cyanide

Info

Publication number
GB913836A
GB913836A GB2164660A GB2164660A GB913836A GB 913836 A GB913836 A GB 913836A GB 2164660 A GB2164660 A GB 2164660A GB 2164660 A GB2164660 A GB 2164660A GB 913836 A GB913836 A GB 913836A
Authority
GB
United Kingdom
Prior art keywords
oxides
catalyst
hydrogen cyanide
ammonia
oxygen
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
GB2164660A
Inventor
Frederick James Bellringer
Frank Christopher Newman
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.)
Distillers Co Yeast Ltd
Distillers Co Ltd
Original Assignee
Distillers Co Yeast Ltd
Distillers Co Ltd
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 Distillers Co Yeast Ltd, Distillers Co Ltd filed Critical Distillers Co Yeast Ltd
Priority to GB2164660A priority Critical patent/GB913836A/en
Publication of GB913836A publication Critical patent/GB913836A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C3/00Cyanogen; Compounds thereof
    • C01C3/02Preparation, separation or purification of hydrogen cyanide
    • C01C3/0208Preparation in gaseous phase
    • C01C3/0212Preparation in gaseous phase from hydrocarbons and ammonia in the presence of oxygen, e.g. the Andrussow-process
    • C01C3/0216Preparation in gaseous phase from hydrocarbons and ammonia in the presence of oxygen, e.g. the Andrussow-process characterised by the catalyst used

Abstract

Hydrogen cyanide is produced by vapour phase reaction, at between 350 DEG -600 DEG C., of methanol, ammonia and oxygen over a tin oxide/antimony oxide catalyst. The reaction may be effected over a fixed or fluidized bed of neat or supported catalyst. The catalyst may be prepared by mixing the oxides or compounds which decompose to the oxides and heating to 550 DEG -1100 DEG C. in an oxygen containing atmosphere to give a catalyst with a molar ratio of tin to antimony in the range of 0,1 to 20:1. The preferred method is to mix oxides obtained by the action of nitric acid of suitable concentration and calcining at 550 DEG -1100 DEG C. Other methods of preparation are referred to. When lower oxides are used as starting materials, the calcination is effected in two separate stages, the first stage being in the range of 300 DEG -650 DEG C. The gaseous reaction mixture is preferably diluted with steam or steam and nitrogen and contains ammonia and methanol in the mole ratio of 1:2 to 2:1 and 1 to 20% by volume of oxygen. Hydrogen cyanide recovery, after acid scrubbing to remove ammonia, may be by absorption in water or alkali metal hydroxides or carbonates.
GB2164660A 1960-06-21 1960-06-21 Improvements in and relating to the synthesis of hydrogen cyanide Expired GB913836A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2164660A GB913836A (en) 1960-06-21 1960-06-21 Improvements in and relating to the synthesis of hydrogen cyanide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2164660A GB913836A (en) 1960-06-21 1960-06-21 Improvements in and relating to the synthesis of hydrogen cyanide

Publications (1)

Publication Number Publication Date
GB913836A true GB913836A (en) 1962-12-28

Family

ID=10166430

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2164660A Expired GB913836A (en) 1960-06-21 1960-06-21 Improvements in and relating to the synthesis of hydrogen cyanide

Country Status (1)

Country Link
GB (1) GB913836A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0048800A1 (en) * 1980-09-27 1982-04-07 Degussa Aktiengesellschaft Process for producing hydrogen cyanide
EP0072416A2 (en) * 1981-08-19 1983-02-23 Degussa Aktiengesellschaft Process for producing hydrogen cyanide
EP0089118A1 (en) * 1982-02-22 1983-09-21 Nitto Chemical Industry Co., Ltd. Process for the production of hydrogen cyanide
US4869889A (en) * 1989-03-23 1989-09-26 W. R. Grace & Co.-Conn. Process for the production of hydrogen cyanide
WO2010061097A1 (en) 2008-11-27 2010-06-03 Arkema France Method for the production of a biomass-derived methyl methacrylate
US8735631B2 (en) 2008-11-20 2014-05-27 Arkema France Method for manufacturing methylmercaptopropionaldehyde and methionine using renewable raw materials

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0048800A1 (en) * 1980-09-27 1982-04-07 Degussa Aktiengesellschaft Process for producing hydrogen cyanide
US4387081A (en) 1980-09-27 1983-06-07 Degussa Ag Process for the production of hydrogen cyanide
EP0072416A2 (en) * 1981-08-19 1983-02-23 Degussa Aktiengesellschaft Process for producing hydrogen cyanide
EP0072416A3 (en) * 1981-08-19 1983-07-27 Degussa Aktiengesellschaft Process for producing hydrogen cyanide
EP0089118A1 (en) * 1982-02-22 1983-09-21 Nitto Chemical Industry Co., Ltd. Process for the production of hydrogen cyanide
US4869889A (en) * 1989-03-23 1989-09-26 W. R. Grace & Co.-Conn. Process for the production of hydrogen cyanide
EP0392221A1 (en) * 1989-03-23 1990-10-17 Hampshire Chemical Corporation Process for the production of hydrogen cyanide
US8735631B2 (en) 2008-11-20 2014-05-27 Arkema France Method for manufacturing methylmercaptopropionaldehyde and methionine using renewable raw materials
WO2010061097A1 (en) 2008-11-27 2010-06-03 Arkema France Method for the production of a biomass-derived methyl methacrylate

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