GB890268A - Improvements relating to the production of cyanogen halides - Google Patents

Improvements relating to the production of cyanogen halides

Info

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
Application number
GB31401/60A
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Publication of GB890268A publication Critical patent/GB890268A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C3/00Cyanogen; Compounds thereof
    • C01C3/004Halogenides 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.
GB31401/60A 1959-09-24 1960-09-12 Improvements relating to the production of cyanogen halides Expired GB890268A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US2802887A (en) Hydrogenation of chlorotrifluoroethylene
US2989376A (en) Method of producing pure silicon
US3041145A (en) Production of pure silicon
GB890268A (en) Improvements relating to the production of cyanogen halides
US3267161A (en) Chlorination process
US3417126A (en) Method of producing malononitrile
NO132659B (en)
US3138643A (en) Preparation of trichloroethanes
GB975498A (en) Halopropane production
US3278264A (en) Hydrogen iodide production
US2915548A (en) Production of nitriles
GB902076A (en) Improvements relating to the production of silicon tetrachloride
DE3380064D1 (en) Process for producing metallic chlorides
US3920799A (en) Process for preparing silicon tetrachloride from silicon carbide with hydrogen chloride
US3173760A (en) Process for the preparation of a boron trihalide
US2908551A (en) Process for the preparation of cyanogen
US2952706A (en) Preparation of thiocarbonyl fluoride
US3023077A (en) Process of preparing cyanogen halide
US3059034A (en) Process of hydrohalogenation of acetylene
US2639300A (en) Preparation of fluoromethanes
GB1056225A (en) Improvements relating to the reactivation of catalysts
GB971458A (en) Pellet bed chlorinator and pellet bed chlorination process
US3564066A (en) Fixed bed catalytic process for the preparation of trichloropropanes
GB584662A (en) Improvements in or relating to the production of vinyl cyanide
US3493333A (en) Preparation of anhydrous magnesium chloride