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US4354044A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for preparing methacrolein

Assignee: Asahi Kasei Corp
•
Filing: 1981-05-20
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Granted: 1982-10-12
•
Expires: 2001-05-20
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Abstract

Abstract A method for preparing methacrolein by oxidizing isobutylene or tertiary butanol with molecular oxygen, characterized by contacting a gaseous mixture of isobutylene or tertiary butanol, air or oxygen and optionally steam and an inert gas with a catalyst having the general combination: Mo.sub.12 Fe.sub.a Ni.sub.b Te.sub.c Tl.sub.d Pb.sub.f X.sub.g O.sub.h wherein a, b, c, d, f and g represent the numbers of atoms of the respective elements per 12 molybdenum atoms; X is at least one element selected from the group consisting of Cu, Nd and Sm; a is a value of 0.2-6; b is a value of 0.2-6; a+b is a value of 1-10; c is a value of 0.1-4; d is a value of 0.1-3; f is a value of 0.1-5; g is a value of 0.1-5; and h is the number of oxygen atoms for satisfying the valencies of the existing elements. The use of this catalyst enables the selectivity for methacrolein to be improved to 90-94% and the yield based on the starting material to be increased to 89-91%. In addition, the activity of said catalyst is stably maintained for a long period of time.

Inventors

  • 👤 Atsushi Aoshima
  • 👤 Ryoichi Mitsui
  • 👤 Hitoshi Nihei

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 18:59
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J23/88; B01J23/887; B01J23/8871; B01J23/8874; B01J23/8875; C; C07; C07C; C07C45/00; C07C45/27; C07C45/32; C07C45/33; C07C45/34; C07C45/35; C07C45/37; C07C51/00; C07C51/16; C07C51/21; C07C51/23; B01J2523/00

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 165 words
A process for producing methacrolein by oxidizing isobutylene or tertiary butanol with molecular oxygen in the presence of a catalyst, characterized in that said catalyst has the general composition: Mo.sub.12 Fe.sub.a Ni.sub.b Te.sub.c Tl.sub.d Pb.sub.f X.sub.g O.sub.h wherein a, b, c, d, f and g represent the number of atoms of the respective elements per 12 molybdenum atoms; X represents at least one element selected from the group consisting of Cu, Nd and Sm; a is a value of 0.2-6; b is a value of 0.2-6; a+b is a value of 1-10; c is a value of 0.1-4; d is a value of 0.1-3; f is a value of 0.1-5; g is a value of 0.1-5; and h is the number of oxygen atoms for satisfying the valencies of the existing elements, the reaction being carried out at a temperature of 200°-550° C. at a pressure of 0.5-10 atmospheres for 0.1 to 15 seconds at a space velocity of 100 to 5000 hr -1 .
Claim 2
Dependent Claim 165 words
A process for producing methacrolein by oxidizing isobutylene or tertiary butanol with molecular oxygen in the presence of a catalyst, characterized in that said catalyst has the general composition: Mo.sub.12 Fe.sub.a Ni.sub.b Te.sub.c Tl.sub.d Pb.sub.f X.sub.g O.sub.h wherein a, b, c, d, f and g represent the number of atoms of the respective elements per 12 molybdenum atoms; X represents at least one element selected from the group consisting of Cu, Nd and Sm; a is a value of 0.2-6; b is a value of 0.2-6; a+b is a value of 1-10; c is a value of 0.1-4; d is a value of 0.1-3; f is a value of 0.1-5; g is a value of 0.1-5; and h is the number of oxygen atoms for satisfying the valencies of the existing elements, the reaction being carried out at a temperature of 200°-550° C. at a pressure of 0.5-10 atmospheres for 0.1 to 15 seconds at a space velocity of 100 to 5000 hr -1 .
Claim 3
Dependent Claim 14 words
A process according to claim 1, wherein said catalyst is supported on a carrier.
Claim 4
Dependent Claim 15 words
A process according to claim 2, wherein said carrier is silica, silicon carbide or alumina.
Claim 5
Dependent Claim 31 words
A process according to claim 1, 2 or 3, wherein the reaction is carried out at a temperature of 250°-450° C. at a pressure ranging from atmospheric pressure to 2 atmospheres.
Claim 6
Dependent Claim 34 words
A process according to claim 1, 2 or 3, wherein a gaseous mixture comprising isobutylene or tertiary butanol, air or oxygen, steam and an inert gas is contacted with said catalyst under atmospheric pressure.

References Cited (Backward Citations)

US3168572A Cited
GB1001505A Cited
US3660479A Cited
US3716497A Cited
US4025565A Cited
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DE2735414A1 Cited
US4258217A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-10-11 1986-04-12 1986-10-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-10-11 1990-04-12 1990-10-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-10-11 1994-04-12 1994-10-12 $7700.00 Window Closed / Lapsed

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