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US4140773A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of high pore volume alumina spheres

Assignee: Vista Chemical Co
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Filing: 1978-02-24
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Granted: 1979-02-20
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Expires: 1998-02-24
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Abstract

Abstract High macro-pore content spheres (>1000A) are produced by use of a rotating wheel, wherein dry alumina is dropped onto the wheel under a peptizing spray misted onto the wheel through an atomizing device. Compressive stresses normally encountered in procedures such as pelletizing are avoided, thereby preserving macro-pores. Size of spheres can be adjusted by altering, for example, the angle at which the wheel rotates.

Inventors

  • 👤 Donald E. Stowell
  • 👤 Larry L. Bendig
  • 👤 John F. Scamehorn

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 16:13
CPC Classifications
C; C01; C01F; C01F7/00; C01F7/02; C01F7/34; C01F7/36; C01P; C01P2004/00; C01P2004/30; C01P2004/32; C01P2006/00; C01P2006/12; C01P2006/16

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 130 words
A method for producing alumina spheres having between about 25% and 40% of all pores above 1,000 angstroms in size, comprising (a) producing alumina powder by mixing water and aluminum alkoxide at a velocity of from about 40 feet per second to about 250 feet per second, wherein velocity is determined by the formula V = F/pA wherein V is velocity, F is rate of flow in pounds per second, p is density in pounds per cubic foot, and A is orifice area in square feet; passing the admixture into a hydrolysis reactor; (b) allowing hydrolysis to occur, removing alumina and drying to obtain a high pore volume powder, and (c) dropping the dried high pore volume alumina onto a rotating wheel under a peptizing spray misted onto the wheel.
Claim 2
Independent Claim 130 words
A method for producing alumina spheres having between about 25% and 40% of all pores above 1,000 angstroms in size, comprising (a) producing alumina powder by mixing water and aluminum alkoxide at a velocity of from about 40 feet per second to about 250 feet per second, wherein velocity is determined by the formula V = F/pA wherein V is velocity, F is rate of flow in pounds per second, p is density in pounds per cubic foot, and A is orifice area in square feet; passing the admixture into a hydrolysis reactor; (b) allowing hydrolysis to occur, removing alumina and drying to obtain a high pore volume powder, and (c) dropping the dried high pore volume alumina onto a rotating wheel under a peptizing spray misted onto the wheel.
Claim 3
Dependent Claim 28 words
A method as described in claim 1 wherein the peptizing spray is an acid spray selected from the group consisting of nitric acid, acetic acid, and formic acid.
Claim 4
Dependent Claim 31 words
A method as described in claim 2 wherein the alumina powder peptizer spray ratio is by weight from about 1.7 to about 2.4 respectively (based on 3% nitric acid in spray).

References Cited (Backward Citations)

US2805920A Cited
US3317277A Cited
US3419352A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-02-19 1982-08-21 1983-02-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-02-19 1986-08-21 1987-02-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-02-19 1990-08-21 1991-02-20 $7700.00 Window Closed / Lapsed

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