GB393128A - Manufacture of calcium cyanamide - Google Patents
Manufacture of calcium cyanamideInfo
- Publication number
- GB393128A GB393128A GB22826/32A GB2282632A GB393128A GB 393128 A GB393128 A GB 393128A GB 22826/32 A GB22826/32 A GB 22826/32A GB 2282632 A GB2282632 A GB 2282632A GB 393128 A GB393128 A GB 393128A
- Authority
- GB
- United Kingdom
- Prior art keywords
- temperature
- calcium
- nitrogen
- carbide
- increase
- 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
- C01C3/002—Synthesis of metal cyanides or metal cyanamides from elementary nitrogen and carbides
Abstract
Calcium cyanamide is obtained by causing nitrogen to act on finely granulated calcium carbide which is constantly kept in motion, the absorption of nitrogen being started at a relatively low temperature and the temperature being then permitted to increase at a sufficiently slow rate to prevent agglomerating until the final required temperature is attained. The temperature may be controlled by controlling the supply of external heat or the supply of nitrogen. The initial temperature may be 600-950 DEG C., which may be increased to final temperatures of 950-1050 DEG C. in periods of from 6-60 hours. The increase of temperature may be in steps say of 50 DEG C., each increase being permitted only after the absorption of nitrogen following the previous increase has ceased. Catalysts such as calcium chloride, calcium fluoride or calcium cyanamide or inert diluents such as calcium cyanamide or lime may be added to the calcium carbide and the presence or absence of such additions or the granular size of the carbide affects the allowable initial temperature or rate of increase thereof. The granular calcium carbide may contain some carbide in the form of dust. The nitrogen may be diluted with inert gases. The process may be carried out by introducing granulated calcium carbide and nitrogen continuously into an externally electrical-resistance heated rotating drum, the carbide moving continuously through the drum, which has a temperature of 780 DEG C. at the inlet and 1000 DEG C. at the outlet. Examples are given. Specifications 107,754 and 123,796, [both in Class 1 (ii), Inorganic compounds, other than &c.], are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE393128X | 1931-08-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB393128A true GB393128A (en) | 1933-06-01 |
Family
ID=6389750
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB22826/32A Expired GB393128A (en) | 1931-08-15 | 1932-08-15 | Manufacture of calcium cyanamide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB393128A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11180371B2 (en) | 2019-04-12 | 2021-11-23 | J. Dustin Hultine | Integrated synthesis of commodity chemicals from waste plastic |
-
1932
- 1932-08-15 GB GB22826/32A patent/GB393128A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11180371B2 (en) | 2019-04-12 | 2021-11-23 | J. Dustin Hultine | Integrated synthesis of commodity chemicals from waste plastic |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB1503676A (en) | Calcination of coke | |
GB393128A (en) | Manufacture of calcium cyanamide | |
SE7507333L (en) | WAY TO PRODUCE COKE. | |
JPS5828218B2 (en) | Kanshikisyoukasuiwasetsukainoseizouhouhou | |
GB891784A (en) | Lithium chloride production | |
US3324119A (en) | Production of isatoic anhydride and certain halo derivatives thereof | |
US2433498A (en) | Method of roasting copperas | |
US2809880A (en) | Production of magnesium oxide | |
US1174176A (en) | Process of making fertilizer. | |
US2781254A (en) | Method of manufacturing a chemical fertilizer from sludge, containing ammonium nitrate, dicalcium phosphate, and calcium carbonate | |
US2058980A (en) | Process for hydrating caustics and dehydrating hydrous salts | |
US768230A (en) | Manufacture of carbonic-acid gas. | |
GB1028460A (en) | Process for the manufacture of coke dust | |
US1754358A (en) | Production of potassium-ammonium sulphate | |
SU339183A1 (en) | The method of high-temperature heat treatment of carbon materials | |
SU624891A1 (en) | Method of processing granulated blast-furnace slag | |
GB191423288A (en) | Process for the Production of Chlorine and Sulphates from Chlorides. | |
US1638061A (en) | Method of dry distillation of alkalized waste liquor from the soda cellulose manufacture | |
US2021663A (en) | Method of producing lime | |
US75861A (en) | William w | |
GB100517A (en) | Improvements in the Manufacture of Iron Chloride. | |
US1773491A (en) | Method of producing the blast required for blast-furnace or similar plants by means of calcium carbide | |
SU1161464A1 (en) | Method of obtaining graphite | |
GB723715A (en) | Process for the manufacture of fluorochlorethylenes | |
SU14907A1 (en) | Method for producing barium ortho and trisilicate |