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US4711748A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of bleach catalyst aggregates of manganese cation impregnated aluminosilicates by high velocity granulation

Assignee: Lever Brothers Co
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Filing: 1986-11-12
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Granted: 1987-12-08
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Expires: 2006-11-12
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Abstract

Abstract A process is disclosed for the preparation of bleach catalysts in aggregate form. The steps comprise adsorbing a manganese (II) salt onto an aluminosilicate support; granulating with a high disrupting force an aqueous slurry of the aluminosilicate bearing manganese (II), and drying the resultant aggregates. At least 70% of the dried aggregates resulting from the process must have a diameter size from at least 250 to about 2000 microns.

Inventors

  • 👤 Charles F. Irwin
  • 👤 William Karpusiewicz
  • 👤 Patricia Liberati

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 18:26
CPC Classifications
C; C11; C11D; C11D3/00; C11D3/39; C11D3/3902; C11D3/3905; C11D3/3935; C11D17/00; C11D17/0034; C11D3/3932

Claims Analysis

Total Claims: 22
Claim 1
Independent Claim 181 words
A process for the preparation of bleach catalysts in aggregate form, exclusive of any peroxide compound within the aggregate, comprising the steps of: (i) adsorbing a manganese (II) cation onto an aluminosilicate support material having an average diameter size of about 2 to 10 microns, the ratio of manganese (II) cations to aluminosilicate ranging from about 1:1000 to 1:10, the combined weight of manganese (II) cation and aluminosilicate support material being from 1 to 99% of the total catalyst; (ii) granulating a wet mass by subjecting aggregates of said wet mass to collisions having a velocity greater than I0 meters/sec said wet mass comprising aluminosilicate support material, with manganese (II) cations adsorbed thereon, in the presence of from about 0.1 to 40% of a binder, the amount based on a dry solids weight content of the total aggregate, and wherein neither the aggregates nor their components have a pH of more than 10; and (iii) drying the resultant aqqreqates and wherein at least 70% of said dried aggregates have a diameter size ranging from at least 250 to about 2000 microns.
Claim 2
Dependent Claim 181 words
A process for the preparation of bleach catalysts in aggregate form, exclusive of any peroxide compound within the aggregate, comprising the steps of: (i) adsorbing a manganese (II) cation onto an aluminosilicate support material having an average diameter size of about 2 to 10 microns, the ratio of manganese (II) cations to aluminosilicate ranging from about 1:1000 to 1:10, the combined weight of manganese (II) cation and aluminosilicate support material being from 1 to 99% of the total catalyst; (ii) granulating a wet mass by subjecting aggregates of said wet mass to collisions having a velocity greater than I0 meters/sec said wet mass comprising aluminosilicate support material, with manganese (II) cations adsorbed thereon, in the presence of from about 0.1 to 40% of a binder, the amount based on a dry solids weight content of the total aggregate, and wherein neither the aggregates nor their components have a pH of more than 10; and (iii) drying the resultant aqqreqates and wherein at least 70% of said dried aggregates have a diameter size ranging from at least 250 to about 2000 microns.
Claim 3
Dependent Claim 17 words
A process according to claim 1, wherein the particle diameter size ranges from 900 to 1500 microns.
Claim 4
Dependent Claim 22 words
A process according to claim 1, wherein the binder is selected from the group consisting of starches, cellulose ethers, gums and sugars.
Claim 5
Dependent Claim 22 words
A process according to claim 1, wherein the binder is a long chain C 10 -C 22 fatty acid or soap thereof.
Claim 6
Dependent Claim 13 words
A process according to claim 1, wherein the binder is a modified starch.
Claim 7
Dependent Claim 11 words
A process according to claim 1, wherein the binder is polyvinylpyrrolidone.
Claim 8
Dependent Claim 27 words
A process according to claim 1, wherein the aluminosilicate support material is a synthetic zeolite having a pore size of from about 4 to about 10 Angstroms.
Claim 9
Dependent Claim 15 words
A process according to claim 1, wherein the aluminosilicate support material is a silicoalumino phosphate.
Claim 10
Dependent Claim 27 words
A process according to claim 1, wherein the amount of manganese (II) cation is present from about 1 to about 2.5% by weight of aluminosilicate support material.
Claim 11
Dependent Claim 15 words
A process according to claim 1 wherein said velosity is at least about 20 meter/seconds.
Claim 12
Dependent Claim 174 words
A process for the prepartation for the preparation of bleach catalysts in aggregate form, exclusive of any peroxy compound within the aggregate, comprising the steps of: (i) granulating a wet mass by subjecting aggregates of said wet mass to collisions having a velocity greater than 10 meters/second, said wet mass comprising: (a) an aluminosilicate support material having an average diameter size of about 2 to 10 microns; (b) a manganese (II) cation, the ratio of manganese (II) cation to aluminosilicate support material ranging from about 1:1000 to 1:10, and the combined weight of manganese (II) cation and aluminosilicate support material being from 1 to 99% of the total catalyst; (c) from about 0.1 to about 40% of a binder, the amount based on a dry solids weight content of the total aggregate, and wherein neither the aggregates nor their components have a pH of more than 10; (ii) drying the resultant aggregates and wherein at least 70% of said dried aggregates have a diameter size ranging from at least 250 to about 2000 microns.
Claim 13
Dependent Claim 174 words
A process for the prepartation for the preparation of bleach catalysts in aggregate form, exclusive of any peroxy compound within the aggregate, comprising the steps of: (i) granulating a wet mass by subjecting aggregates of said wet mass to collisions having a velocity greater than 10 meters/second, said wet mass comprising: (a) an aluminosilicate support material having an average diameter size of about 2 to 10 microns; (b) a manganese (II) cation, the ratio of manganese (II) cation to aluminosilicate support material ranging from about 1:1000 to 1:10, and the combined weight of manganese (II) cation and aluminosilicate support material being from 1 to 99% of the total catalyst; (c) from about 0.1 to about 40% of a binder, the amount based on a dry solids weight content of the total aggregate, and wherein neither the aggregates nor their components have a pH of more than 10; (ii) drying the resultant aggregates and wherein at least 70% of said dried aggregates have a diameter size ranging from at least 250 to about 2000 microns.
Claim 14
Dependent Claim 17 words
A process according to claim 11, wherein the particle diameter size ranges from 900 to 1500 microns.
Claim 15
Dependent Claim 22 words
A process according to claim 11, wherein the binder is selected from the group consisting of starches, cellulose ethers, gums and sugars.
Claim 16
Dependent Claim 22 words
A process according to claim 11, wherein the binder is a long chain C 10 -C 22 fatty acid or soap thereof.
Claim 17
Dependent Claim 13 words
A process according to claim 11, wherein the binder is a modified starch.
Claim 18
Dependent Claim 11 words
A process according to claim 11, wherein the binder is polyvinylpyrrolidone.
Claim 19
Dependent Claim 27 words
A process according to claim 11, wherein the aluminosilicate support material is a synthetic zeolite having a pore size of from about 4 to about 10 Angstroms.
Claim 20
Dependent Claim 15 words
A process according to claim 11, wherein the aluminosilicate support material is a silicoalumino phosphate.
Claim 21
Dependent Claim 27 words
A process according to claim 11, wherein the amount of manganese (II) cation is present from about 1 to about 2.5% by weight of aluminosilicate support material.
Claim 22
Dependent Claim 14 words
A process according to claim 11, wherein said velocity is at least 20 meter/second.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-12-07 1991-06-08 1991-12-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-12-07 1995-06-08 1995-12-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-12-07 1999-06-08 1999-12-08 $7700.00 Window Closed / Lapsed

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