GB867227A - Improvements in or relating to the manufacture of hydrocyanic acid - Google Patents

Improvements in or relating to the manufacture of hydrocyanic acid

Info

Publication number
GB867227A
GB867227A GB2433957A GB2433957A GB867227A GB 867227 A GB867227 A GB 867227A GB 2433957 A GB2433957 A GB 2433957A GB 2433957 A GB2433957 A GB 2433957A GB 867227 A GB867227 A GB 867227A
Authority
GB
United Kingdom
Prior art keywords
arc
hydrocarbon
litres
carbon atoms
hour
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
GB2433957A
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.)
Compagnie de Saint Gobain SA
Original Assignee
Compagnie de Saint Gobain SA
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 Compagnie de Saint Gobain SA filed Critical Compagnie de Saint Gobain SA
Publication of GB867227A publication Critical patent/GB867227A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C3/00Cyanogen; Compounds thereof
    • C01C3/02Preparation, separation or purification of hydrogen cyanide
    • C01C3/0208Preparation in gaseous phase
    • C01C3/025Preparation in gaseous phase by using a plasma
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/08Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
    • B01J19/087Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
    • B01J19/088Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Plasma & Fusion (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

<PICT:0867227/III/1> Hydrocyanic acid is produced from a gaseous mixture of ammonia and a lower hydrocarbon of the aliphatic series by exposing it at sub-atmospheric pressure to the action of an electric arc discharge, supplying it at a rate of 120-350 litres (measured at N.T.P) per hour per kilowatt of power consumed by the arc. An oxygen free mixture of ammonia gas with gaseous lower aliphatic hydrocarbon, i.e. one containing 1-12 carbon atoms/molecule, preferably one containing 1-4 carbon atoms/molecule, is introduced through 17 into the reactor 15, which is provided with a double wall 16, a water jacket, and means to evacuate the interior thereof to a pressure of 40-120 mm., preferably 40-75 mm. of mercury and at a rate depending upon the hydrocarbon used. Thus for methane the rate is 270-350 litres/hour/kw of power consumed by the arc; 240-260 litres/hour/kw when the hydrocarbon contains 2 carbon atoms per molecule and 180-240 litres/hour/kw. When the hydrocarbon contains 3 carbon atoms or more. The mixture of ammonia and hydrocarbon may contain stoichiometric proportions of the reactants or a 10% excess of either one. The mixture is passed through an electric arc struck between electrodes 18 and 19 which are preferably obliquely disposed to one another and which rotate about their axes. The electrodes may be further drawn apart by mechanisms 7 and 71 which causes the arc to be extended through the gas. The rate of supply of the gases is such that they are subjected to the arc for only 0.04 to 0.001 seconds. The electrical circuit shown in the Figure is a device for maintaining a high voltage: amperage ratio, e.g. 400:1 to 1500:1 and also a temperature of 1100-1500 DEG C., preferably 1100-1300 DEG C., in the arc. After reaction the gaseous product containing hydrocyanic acid is removed from the reactor at 20 to be cooled and the acid recovered.
GB2433957A 1956-07-31 1957-07-31 Improvements in or relating to the manufacture of hydrocyanic acid Expired GB867227A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR719636 1956-07-31

Publications (1)

Publication Number Publication Date
GB867227A true GB867227A (en) 1961-05-03

Family

ID=8703479

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2433957A Expired GB867227A (en) 1956-07-31 1957-07-31 Improvements in or relating to the manufacture of hydrocyanic acid

Country Status (2)

Country Link
CH (1) CH365714A (en)
GB (1) GB867227A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19754982A1 (en) * 1997-12-11 1999-06-17 Degussa Process for the production of hydrocyanic acid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19754982A1 (en) * 1997-12-11 1999-06-17 Degussa Process for the production of hydrocyanic acid
US6096173A (en) * 1997-12-11 2000-08-01 Degussa Aktiengesellschaft Method of producing hydrogen cyanide

Also Published As

Publication number Publication date
CH365714A (en) 1962-11-30

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