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US4260520A Expired / Lapsed US ⏱️ 0.0 years remaining

Carrier-supported catalyst and process for making it

Assignee: Hoechst AG
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Filing: 1979-11-13
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Granted: 1981-04-07
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Expires: 1999-11-13
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Abstract

Abstract The invention relates to a carrier-supported catalyst comprising oxides of cobalt and phosphorus and at least one of the oxides of molybdenum and potassium in the atomic ratio of Co 1 P 1-2 Mo 0-0 .05 K 0-0 .5 on a porous carrier material, and to a process for making it. To this end, the process provides (a) for a dry porous carrier material to be saturated with water up to 40 to 80% of its predetermined saturation value; (b) for the carrier material treated as under (a) to be impregnated either at least once with an aqueous solution of water-soluble compounds of cobalt and phosphorus, molybdenum and/or potassium, or repeatedly and successively, each impregnation being interrupted by an intermediary drying period as specified under (c), with an aqueous solution of a water-soluble compound of merely one of the elements aforesaid, the aqueous solution being used in either case in a quantity which is at most necessary for complete saturation; (c) for the carrier material to be dried after each impregnation over a period of 2 to 20 hours at 350 to 500 K; and (d) for the carrier material treated as described under (a) through (c) to be sintered over a period of 0.5 to 4 hours at 550 to 1000 K, in a stream of air. The carrier-supported catalyst finds use in the production of styrene by subjecting ethylbenzene to oxidative dehydrogenation with molecular oxygen in gas phase.

Inventors

  • 👤 Heinz Erpenbach
  • 👤 Klaus Gehrmann
  • 👤 Herbert Joest

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 14:42
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/186; B01J27/188; B01J27/19; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J23/88; B01J23/882; C; C07; C07C; C07C5/00; C07C5/42; C07C5/48

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 40 words
A carrier-supported catalyst comprising oxides of cobalt and phosphorus and at least one of the oxides of molybdenum and potassium in the atomic ratio of Co 1 P 1-2 Mo 0-0 .05 K 0-0 .05 on a porous carrier material.
Claim 2
Dependent Claim 40 words
A carrier-supported catalyst comprising oxides of cobalt and phosphorus and at least one of the oxides of molybdenum and potassium in the atomic ratio of Co 1 P 1-2 Mo 0-0 .05 K 0-0 .05 on a porous carrier material.
Claim 3
Dependent Claim 23 words
A carrier-supported catalyst as claimed in claim 1, wherein the carrier material has a BET-surface area of 0.1 to 500 m 2 /g.
Claim 4
Dependent Claim 23 words
A carrier-supported catalyst as claimed in claim 1, wherein the carrier material consists of particles with a size of 0.01 to 6 mm.
Claim 5
Dependent Claim 28 words
A carrier-supported catalyst as claimed in claim 1, wherein the carrier material consists of particles with a size of 0.01 to 0.2 mm for use in flow bed.
Claim 6
Dependent Claim 29 words
A carrier-supported catalyst as claimed in claim 1, wherein the carrier material consists of particles with a size of 3 to 6 mm for use in a fixed bed.
Claim 7
Dependent Claim 33 words
A carrier-supported catalyst as claimed in claim 1, containing 2 to 30 weight % of the oxides of cobalt and phosphorus and at least one of the elements selected from molybdenum and potassium.
Claim 8
Dependent Claim 19 words
A carrier-supported catalyst as claimed in claim 1, containing silicic acid or aluminum oxide as the porous carrier material.
Claim 9
Dependent Claim 172 words
A process for making a carrier-supported catalyst as claimed in claim 1, which comprises: (a) saturating a dry porous carrier material with water up to 40 to 80% of its predetermined saturation value; (b) impregnating the carrier material treated as under (a) either at least once with an aqueous solution of water-soluble compounds of cobalt and phosphorus, and at least one of the elements selected from molybdenum and potassium, or repeatedly and successively, each impregnation being interrupted by an intermediary drying period as specified under (c), with an aqueous solution of a water-soluble compound of merely one of the elements aforesaid, the aqueous solution being used in either case in a quantity which is at most necessary for complete saturation. (c) drying the carrier material after each impregnation over a period of 2 to 20 hours at 350° to 500° K.; and (d) sintering the carrier material treated as described under (a) through (c) over a period of 0.5 to 4 hours at 550° to 1000° K., in a stream of air.
Claim 10
Dependent Claim 29 words
A process as claimed in claim 8, wherein the carrier material treated as described under (a) is impregnated as described under (b) at temperatures of 290° to 375° K.

References Cited (Backward Citations)

GB1148108A Cited
US3755196A Cited
US4039476A Cited
US4122039A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-04-06 1984-10-06 1985-04-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-04-06 1988-10-06 1989-04-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-04-06 1992-10-06 1993-04-07 $7700.00 Window Closed / Lapsed

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