GB913836A - Improvements in and relating to the synthesis of hydrogen cyanide - Google Patents
Improvements in and relating to the synthesis of hydrogen cyanideInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C3/00—Cyanogen; Compounds thereof
- C01C3/02—Preparation, separation or purification of hydrogen cyanide
- C01C3/0208—Preparation in gaseous phase
- C01C3/0212—Preparation in gaseous phase from hydrocarbons and ammonia in the presence of oxygen, e.g. the Andrussow-process
- C01C3/0216—Preparation in gaseous phase from hydrocarbons and ammonia in the presence of oxygen, e.g. the Andrussow-process characterised by the catalyst used
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Inorganic Chemistry (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
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.
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)
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 |
-
1960
- 1960-06-21 GB GB2164660A patent/GB913836A/en not_active Expired
Cited By (9)
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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