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US3959339A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing aromatic nitriles

Assignee: Mitsubishi Gas Chemical Co Inc
•
Filing: 1974-06-04
•
Granted: 1976-05-25
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Expires: 1994-06-04
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Abstract

Abstract Aromatic nitriles are produced in good yield from a gas mixture comprising alkyl-substituted aromatic compound, ammonia and molecular oxygen by ammoxidation by passing the gas mixture over a catalyst comprising vanadium oxide, chromium oxide, boron oxide and phosphorus oxide, deposited on a silica carrier, in an atomic ratio of V : Cr : B : P of 1 : 0.5 - 2.0 : 0.1 - 1.2 : 0.01 - 0.3 and a catalyst concentration of 20 to 80 % by weight at a reaction temperature of 300° to 500°C for a contact time of 0.5 to 30 seconds.

Inventors

  • 👤 Masao Saito
  • 👤 Mamoru Onozawa
  • 👤 Takamasa Kawakami

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 12:39
CPC Classifications
C; C07; C07C; C07C253/00; C07C253/24; C07C253/28; B; B01; B01J; B01J23/00; B01J23/002; B01J23/16; B01J23/24; B01J23/26; B01J27/00; B01J27/14; B01J27/186; B01J27/195; B01J27/198; B01J27/199; B01J2523/00

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 94 words
A process for producing aromatic nitriles by ammoxidation, which comprises passing a gas mixture comprising alkyl-substituted aromatic compound, ammonia and molecular oxygen over a catalyst comprising vanadium oxide, chromium oxide, boron oxide and phosphorus oxide, deposited on a silica carrier, in an atomic ratio of V : Cr : B : P of 1 : 0.5 - 2.0 : 0.1 - 1.2 : 0.01 - 0.3 and a catalyst concentration of 20 to 80 % by weight at a reaction temperature of 300° to 500°C for a contact time of 0.5 to 30 seconds.
Claim 2
Dependent Claim 94 words
A process for producing aromatic nitriles by ammoxidation, which comprises passing a gas mixture comprising alkyl-substituted aromatic compound, ammonia and molecular oxygen over a catalyst comprising vanadium oxide, chromium oxide, boron oxide and phosphorus oxide, deposited on a silica carrier, in an atomic ratio of V : Cr : B : P of 1 : 0.5 - 2.0 : 0.1 - 1.2 : 0.01 - 0.3 and a catalyst concentration of 20 to 80 % by weight at a reaction temperature of 300° to 500°C for a contact time of 0.5 to 30 seconds.
Claim 3
Dependent Claim 46 words
A process according to claim 1, wherein the catalyst has an atomic ratio of V : Cr : B : P of 1 : 0.7 - 1.5 : 0.3 - 1.0 : 0.01 - 0.2 and a catalyst concentration of 30 to 60 % by weight.
Claim 4
Dependent Claim 31 words
A process according to claim 1, wherein the gas mixture contains 0.5 to 5 % by volume of the aromatic compound when the molecular oxygen is in a form of air.
Claim 5
Dependent Claim 24 words
A process according to claim 1, wherein the gas mixture contains ammonia in volumes 2 to 10 times as much as theoretically required one.
Claim 6
Dependent Claim 25 words
A process according to claim 1, wherein the gas mixture contains molecular oxygen in volumes at least 1.5 times as much as theoretically required one.
Claim 7
Dependent Claim 22 words
A process according to claim 5, wherein the molecular oxygen is contained in volumes 2 to 50 times as much as theoretical.
Claim 8
Dependent Claim 14 words
A process according to claim 1, wherein the reaction temperature is 330° to 470°C.
Claim 9
Dependent Claim 21 words
A process according to claim 1, wherein the alkyl-substituted aromatic compound is toluene, ethylbenzene, xylene, mesitylene, cymene, durene, diethylbenzene or methylnaphthalene.

References Cited (Backward Citations)

US3772212A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-05-25 1979-11-24 1980-05-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-05-25 1983-11-24 1984-05-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-05-25 1987-11-24 1988-05-25 $7700.00 Window Closed / Lapsed

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