GB890268A - Improvements relating to the production of cyanogen halides - Google Patents
Improvements relating to the production of cyanogen halidesInfo
- Publication number
- GB890268A GB890268A GB31401/60A GB3140160A GB890268A GB 890268 A GB890268 A GB 890268A GB 31401/60 A GB31401/60 A GB 31401/60A GB 3140160 A GB3140160 A GB 3140160A GB 890268 A GB890268 A GB 890268A
- Authority
- GB
- United Kingdom
- Prior art keywords
- carbon
- halogen
- reaction temperature
- nitrogen
- reaction
- 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
- C01C3/004—Halogenides of cyanogen
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Cyanogen chloride and bromide are prepared by bringing the appropriate halogen and nitrogen into contact with carbon at a temperature of 1800 DEG to 3600 DEG C., quenching the product gases to 500 DEG C. or below and condensing and separating the cyanogen halide formed. A suitable type of reactor consists of a jacketted quartz (or alumina or other refractory material that is inert towards the halogen and its reaction products with carbon and nitrogen at the required reaction temperature) tube enclosing an electrically heated graphite rod. On a large scale, an electric resistance furnace or an electric-arc furnace containing a fluidized or stationary bed of carbon particles may be used. In a fluidized carbon-bed reactor, graphite, other forms of carbon, alumina or other inert refractory material may be used as the materials of construction. Non-electrical heat sources, e.g. construction reactions and focused solar heat rays may also be used. The carbon used may be in the form of bars, filaments, rods or beds of particulate material having any shape. The halogen used in the process must be free from impurities such as H2, O2, H2O and other compounds containing H2 or O2, which would preferentially combine at the reaction temperature with the halogen or carbon. The nitrogen must also be free from reactive impurities. The carbon and halogen may be formed in situ from compounds thereof, e.g. CCl4, tetrachloroethylene, and hexachloroethane, decomposing at the reaction temperature. The reaction temperature is preferably between 2400 DEG and 3000 DEG C., and pressures between 0,1 and 3 atmospheres are preferred. The nitrogen/halogen ratio (by volume) should be between 2:1 and 3:1 when the reaction temperature is between 2400 DEG and 3000 DEG C., and 1:1 when the range is 1800 DEG to 2400 DEG C. The carbon that reacts to form the cyanogen halide is in the gas phase, the amount of carbon present being in considerable excess of the amount needed for the reaction. The time of contact of the reactants must be long enough for equilibrium to be attained at the reaction temperature, and after this the gaseous products are quenched to 500 DEG C. or below in from 1 to 10 milliseconds. The quenched gases are further cooled and the cyanogen halide collected, unreacted nitrogen and halogen being recycled. In Example 1, the graphite heating element is heated to 2700 DEG C. and the molar ratio N2:Cl2 is 2,3:1, the reaction time being 40 to 45 minutes. Example 2 is similar, the reaction time being 145 minutes at a temperature of 2850 DEG C. In Example 3, a bed of graphite heated to 2600 DEG C. is used.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US890268XA | 1959-09-24 | 1959-09-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB890268A true GB890268A (en) | 1962-02-28 |
Family
ID=22215083
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31401/60A Expired GB890268A (en) | 1959-09-24 | 1960-09-12 | Improvements relating to the production of cyanogen halides |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB890268A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3245754A (en) * | 1962-03-10 | 1966-04-12 | Roehm & Haas Gmbh | Preparation of cyanogen chloride |
FR2465686A1 (en) * | 1979-08-02 | 1981-03-27 | Degussa | METHOD AND DEVICE FOR OBTAINING PURE CYANOGEN CHLORIDE |
-
1960
- 1960-09-12 GB GB31401/60A patent/GB890268A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3245754A (en) * | 1962-03-10 | 1966-04-12 | Roehm & Haas Gmbh | Preparation of cyanogen chloride |
FR2465686A1 (en) * | 1979-08-02 | 1981-03-27 | Degussa | METHOD AND DEVICE FOR OBTAINING PURE CYANOGEN CHLORIDE |
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