GB820125A - Process for the manufacture of benzonitrile - Google Patents

Process for the manufacture of benzonitrile

Info

Publication number
GB820125A
GB820125A GB17548/56A GB1754856A GB820125A GB 820125 A GB820125 A GB 820125A GB 17548/56 A GB17548/56 A GB 17548/56A GB 1754856 A GB1754856 A GB 1754856A GB 820125 A GB820125 A GB 820125A
Authority
GB
United Kingdom
Prior art keywords
catalyst
naphthalene
silica gel
benzonitrile
oxidation
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
GB17548/56A
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.)
BASF Schweiz AG
Original Assignee
Ciba AG
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 Ciba AG filed Critical Ciba AG
Publication of GB820125A publication Critical patent/GB820125A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C63/00Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
    • C07C63/14Monocyclic dicarboxylic acids
    • C07C63/15Monocyclic dicarboxylic acids all carboxyl groups bound to carbon atoms of the six-membered aromatic ring
    • C07C63/161,2 - Benzenedicarboxylic acid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • C07C253/24Preparation of carboxylic acid nitriles by ammoxidation of hydrocarbons or substituted hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/255Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
    • C07C51/265Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups

Abstract

Benzonitrile is manufactured by a continuous process, wherein an aromatic hydrocarbon capable of yielding phthalic anhydride by oxidation is subjected in the vapour phase to catalytic oxidation with air, and the oxidation product so obtained, and without being cooled or isolated, is converted in the vapour phase by reaction with ammonia in the presence of a dehydration catalyst into benzonitrile. Suitable aromatic hydrocarbons are naphthalene and ortho-xylene, and suitable catalysts for the oxidation step are vanadium pentoxide supported on e.g. silica gel, or alumina, to which phosphorus pentoxide, potassium hydrogen sulphate or potassium sulphate may be added. Suitable dehydration catalysts are aluminium oxide or silica gel. The process may be carried out by preheating a gaseous mixture of air and naphthalene in a ratio within the range 20:1 to 50:1 at a temperature up to 350 DEG C. and passing the mixture at a space velocity within the range of 500-4000 parts by volume per volume of catalyst per hour, over the catalyst heated at 300-500 DEG C. At least 1 mol. of ammonia per mol. of naphthalene is then added and the gaseous mixture is then passed at a space velocity of 100-1000 volumes per volume of catalyst per hour over e.g. silica gel, and is heated at 360 DEG to 500 DEG C. Examples are given of the preparation of benzonitrile from (1) naphthalene with a catalyst of vanadium pentoxide, potassium sulphate and silica gel mixture, for the oxidation step, and silica gel of bulk density 0.4 for the dehydration step; (2) ortho xylene with a catalyst of vanadium pentoxide on pumice; (3) naphthalene with active alumina as the dehydration catalyst.
GB17548/56A 1955-06-09 1956-06-06 Process for the manufacture of benzonitrile Expired GB820125A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH820125X 1955-06-09

Publications (1)

Publication Number Publication Date
GB820125A true GB820125A (en) 1959-09-16

Family

ID=4539350

Family Applications (1)

Application Number Title Priority Date Filing Date
GB17548/56A Expired GB820125A (en) 1955-06-09 1956-06-06 Process for the manufacture of benzonitrile

Country Status (1)

Country Link
GB (1) GB820125A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4178304A (en) * 1978-03-13 1979-12-11 Efendiev Medzhid R O Method of producing ortho-aminobenzonitrile
US4778890A (en) * 1986-08-04 1988-10-18 Koei Chemical Co., Ltd. Process for preparing nitriles

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4178304A (en) * 1978-03-13 1979-12-11 Efendiev Medzhid R O Method of producing ortho-aminobenzonitrile
US4778890A (en) * 1986-08-04 1988-10-18 Koei Chemical Co., Ltd. Process for preparing nitriles

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