GB800158A - Process for the production of hydrocyanic acid from formamide - Google Patents
Process for the production of hydrocyanic acid from formamideInfo
- Publication number
- GB800158A GB800158A GB7483/56A GB748356A GB800158A GB 800158 A GB800158 A GB 800158A GB 7483/56 A GB7483/56 A GB 7483/56A GB 748356 A GB748356 A GB 748356A GB 800158 A GB800158 A GB 800158A
- Authority
- GB
- United Kingdom
- Prior art keywords
- formamide
- vaporized
- evaporator
- recycled
- catalytic decomposition
- 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
- C01C3/0204—Preparation, separation or purification of hydrogen cyanide from formamide or from ammonium formate
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Hydrogen cyanide is produced by the catalytic decomposition of vaporized formamide produced by passing liquid formamide as a thin film down the internal walls of an externally heated evaporation tube, evaporation being assisted by the presence of one or more vanes rotating at high speed within the vessel near the surface of the film. The liquid formamide may have an extended period of stay in the tube, e.g. 5-60 seconds. Vaporization may take place under reduced pressure, e.g. 130-150 mm. of mercury, at a temperature of 120-160 DEG C. or in an atmosphere of ammonia, e.g. preheated to 250 DEG C., at a temperature of e.g. 180-205 DEG C., or alternatively, the formamide may be vaporized first and the mixed with gaseous ammonia, which is if necessary preheated. A proportion of the formamide preferably is passed right through the evaporator, e.g. 4 per cent of that vaporized, is cooled, a portion or the whole thereof is purified by filtration, centrifugation or adsorption, and is thereafter recycled to the evaporator. The condensate produced by cooling the reaction product gas, which consists mainly of formamide, may be similarly purified and recycled to the evaporator. Polymerization of hydrogen cyanide contained in the formamide being recycled may be prevented by adjusting the pH to 5-7. The catalyst may form the wall of the reaction vessel and may e.g. be of steel coated with a thin layer of Fe3O4. A vessel of similar material may be used for preheating and partial catalytic decomposition of the formamide vapour. The catalyst may also be aluminium phosphate supported on kaolin. Catalyst activity may be increased by injecting phosphoric acid, an iron salt, or air into the formamide vapour before catalytic decomposition.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DED20030D DE973173C (en) | 1955-03-15 | 1955-03-15 | Process for the production of hydrocyanic acid from formamide |
Publications (1)
Publication Number | Publication Date |
---|---|
GB800158A true GB800158A (en) | 1958-08-20 |
Family
ID=6712190
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7483/56A Expired GB800158A (en) | 1955-03-15 | 1956-03-09 | Process for the production of hydrocyanic acid from formamide |
Country Status (3)
Country | Link |
---|---|
DE (1) | DE973173C (en) |
FR (1) | FR1170707A (en) |
GB (1) | GB800158A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009062897A1 (en) * | 2007-11-13 | 2009-05-22 | Basf Se | Improved method for the production of hydrocyanic acid by means of catalytic dehydration of gaseous formamide |
US9249029B2 (en) | 2010-01-22 | 2016-02-02 | Basf Se | Single chamber vaporizer and use thereof in chemical synthesis |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2064151B1 (en) | 2006-09-07 | 2011-10-19 | Basf Se | Improved method for producing prussic acid |
AP2010005262A0 (en) * | 2007-11-13 | 2010-06-30 | Basf Se | Improved method for the production of hydrocyanic acid by catalytic dehydration of gaseous formamide |
WO2011089209A2 (en) | 2010-01-22 | 2011-07-28 | Basf Se | Single-chamber evaporator and the use thereof in chemical synthesis |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2534000A (en) * | 1945-10-09 | 1950-12-12 | Du Pont | Process for producing hydrocyanic acid |
-
1955
- 1955-03-15 DE DED20030D patent/DE973173C/en not_active Expired
-
1956
- 1956-03-09 GB GB7483/56A patent/GB800158A/en not_active Expired
- 1956-03-14 FR FR1170707D patent/FR1170707A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009062897A1 (en) * | 2007-11-13 | 2009-05-22 | Basf Se | Improved method for the production of hydrocyanic acid by means of catalytic dehydration of gaseous formamide |
CN101910063B (en) * | 2007-11-13 | 2012-10-10 | 巴斯夫欧洲公司 | Improved process for the production of hydrocyanic acid by catalytic dehydration of gaseous formamide |
US9249029B2 (en) | 2010-01-22 | 2016-02-02 | Basf Se | Single chamber vaporizer and use thereof in chemical synthesis |
Also Published As
Publication number | Publication date |
---|---|
DE973173C (en) | 1959-12-17 |
FR1170707A (en) | 1959-01-16 |
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