US4451386A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Detergent tablet
Assignee: Colgate Palmolive Co
•
Filing: 1982-09-29
•
Granted: 1984-05-29
•
Expires: 2002-09-29
Abstract
Abstract A process for producing detergent tablets from free flowing spray dried base builder beads comprising inorganic detergent builders. The builder beads comprise alkali metal phosphate, alkali metal silicate and water. The alkali metal phosphate, component includes a hydrated and an anhydrous portion. Relatively large amounts of liquid or liquifiable detergent ingredients such as surface active agents etc. can be applied to the base beads after spray drying, without destroying their free flowing properties. The base beads are suitable for compression into coherent tablets. The resulting tablets are of improved detergency, physical integrity and solubility.
Inventors
- 👤 David P. Joshi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 22:49
CPC Classifications
C; C11; C11D; C11D3/00; C11D3/02; C11D3/04; C11D3/06; C11D1/00; C11D1/66; C11D1/72; C11D11/00; C11D17/00; C11D17/0047; C11D17/0065; C11D17/0073; C11D3/08
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
448 words
A cleaning tablet comprising a detergent composition produced by: (a) hydrating a first quantity of anhydrous phosphate builder salt to the maximum in the presence of an alkali metal silicate using sufficient water to form a hydrated slurry; (b) adding a second quantity of anhydrous phosphate builder salt to said hydrated slurry to form a crutcher mix; (c) spray drying said crutcher mix to form a particulate material, the weight ratio of said first quantity of builder salt to said alkali metal silicate being from about 1.5 to about 5 and the weight ratio of said first quantity of builder salt to said second quantity of builder salt being from about 0.3 to about 0.7; (d) combining said particulate material with from about 2 to about 40 percent by weight of an organic material chosen from the group consisting of, nonionic surface active agents and mixtures thereof; (e) compressing said particulate material to form coherent tablets said particulate material prior to tableting having a flowability of at least about 70% that of clean dry sand, said particulate material comprising: from about 60 to 88 percent by weight of spray dried base beads having detergent building properties, comprising from about 45 to about 85% bt weight of an alkali metal phosphate wherein from about 30 to about 60 percent of the phosphate is hydrated and the remainder is anhydrous, from about 5 to about 15 percent by weight of a sodium silicate having an Na 2 O:SiO 2 ratio of from about 1:1.6 to about 1:3.4 and from about 5 to about 15% water, wherein a portion of the water is present as water of hydration in the hydrated phosphate, the beads being essentially free of organic surfactant, organic detergent or soap, when spray dried; from about 12 to about 40 percent by weight of a nonionic polyethoxylated synthetic organic detergent; said beads having a structure of microcrystals and amorphous solid interconnected as an irregular network within the beads, the network defining interconnected irregularly shaped passageways, said passageways comprising a reticular void space within the beads and interconnecting to discrete openings on the external surface of the beads; the nonionic detergent being applied to the external surfaces of the spray dried beads and being substantially absorbed into the internal passageways of the beads to produce the granular detergent; the beads, before tableting, having a specific gravity of from about 0.5 to about 0.8; at least 90% of the beads and the granular detergent having a particle size distributed between 20 mesh and 200 mesh U.S. sieve series, and the beads, during tableting, being subjected to compression forces of between about 3/4 ton to about 3 tons per square inch.
Claim 2
Dependent Claim
448 words
A cleaning tablet comprising a detergent composition produced by: (a) hydrating a first quantity of anhydrous phosphate builder salt to the maximum in the presence of an alkali metal silicate using sufficient water to form a hydrated slurry; (b) adding a second quantity of anhydrous phosphate builder salt to said hydrated slurry to form a crutcher mix; (c) spray drying said crutcher mix to form a particulate material, the weight ratio of said first quantity of builder salt to said alkali metal silicate being from about 1.5 to about 5 and the weight ratio of said first quantity of builder salt to said second quantity of builder salt being from about 0.3 to about 0.7; (d) combining said particulate material with from about 2 to about 40 percent by weight of an organic material chosen from the group consisting of, nonionic surface active agents and mixtures thereof; (e) compressing said particulate material to form coherent tablets said particulate material prior to tableting having a flowability of at least about 70% that of clean dry sand, said particulate material comprising: from about 60 to 88 percent by weight of spray dried base beads having detergent building properties, comprising from about 45 to about 85% bt weight of an alkali metal phosphate wherein from about 30 to about 60 percent of the phosphate is hydrated and the remainder is anhydrous, from about 5 to about 15 percent by weight of a sodium silicate having an Na 2 O:SiO 2 ratio of from about 1:1.6 to about 1:3.4 and from about 5 to about 15% water, wherein a portion of the water is present as water of hydration in the hydrated phosphate, the beads being essentially free of organic surfactant, organic detergent or soap, when spray dried; from about 12 to about 40 percent by weight of a nonionic polyethoxylated synthetic organic detergent; said beads having a structure of microcrystals and amorphous solid interconnected as an irregular network within the beads, the network defining interconnected irregularly shaped passageways, said passageways comprising a reticular void space within the beads and interconnecting to discrete openings on the external surface of the beads; the nonionic detergent being applied to the external surfaces of the spray dried beads and being substantially absorbed into the internal passageways of the beads to produce the granular detergent; the beads, before tableting, having a specific gravity of from about 0.5 to about 0.8; at least 90% of the beads and the granular detergent having a particle size distributed between 20 mesh and 200 mesh U.S. sieve series, and the beads, during tableting, being subjected to compression forces of between about 3/4 ton to about 3 tons per square inch.
Claim 3
Dependent Claim
34 words
A cleaning tablet according to claim 1 wherein said hydrated slurry is heated to a temperature from about 170° F. to about 200° F. after maximum hydration of the first quantity of builder salt.
Claim 4
Dependent Claim
26 words
A cleaning tablet according to claim 1 wherein additional water is added to said aqueous slurry with the addition of said second quantity of anhydrous phosphate.
Claim 5
Dependent Claim
52 words
A cleaning tablet according to claim 1 wherein said hydrating step is performed at a temperature suitable for hydrating said first quantity of phosphate builder salt to a maximum and said slurry is then raised to a temperature that would prevent any significant hydration of said second quantity of phosphate builder salt.
Claim 6
Dependent Claim
22 words
A cleaning tablet according to claim 1 wherein the weight ratio of said first quantity to said second quantity is about 0.5.
Claim 7
Dependent Claim
20 words
A cleaning tablet according to claim 1 wherein said crutcher mix contains from about 40 to about 55 percent solids.
Claim 8
Dependent Claim
43 words
A cleaning tablet according to claim 1 wherein said spray drying takes place in a countercurrent spray tower at a spray pressure from about 200 psig to about 1000 psig and an inlet air temperature from about 500° F. to about 700° F.
Claim 9
Dependent Claim
48 words
A cleaning tablet according to claim 1 wherein up to 10 percent by weight based on the crutcher solids, of builder salts is added to said crutcher mix, said builder salts being chosen from the group consisting of carbonates, citrates, silicates or combinations thereof having detergent building properties.
Claim 10
Dependent Claim
48 words
A cleaning tablet according to claim 1 wherein a quantity of a liquid or semi-solid nonionic detergent material is sprayed onto said bead such that said nonionic detergent impregnates said bead, said quantity of nonionic being about 10 to about 40 percent by weight of said based bead.
Claim 11
Dependent Claim
27 words
A cleaning tablet according to claim 1 further includes mixing with the particulate material and organic material about 1 to about 5 percent of a disintegrating aide.
Claim 12
Dependent Claim
33 words
A cleaning tablet according to claim 1 wherein said compressing step is performed in a tableting press with the application of from about 3/4 to about 1 ton per square inch of pressure.
Claim 13
Dependent Claim
95 words
A cleaning tablet according to claim 1 wherein said hydrating step (a) is performed in an aqueous medium and at a temperature of at least about 140° F. and not greater than about 170° F.; the temperature of said hydrated slurry is raised to more than about 170° F. and less than about 200° F.; and said hydrated slurry and said crutcher mix are maintained at temperatures of at least about 170° F. through the steps of adding the second quantity of anhydrous sodium tripolyphosphate and supplying said crutcher mix to a spray drying tower.
Claim 14
Independent Claim
170 words
A method for producing cleaning tablets comprising hydrating a first quantity of anhydrous phosphate builder salt in the presence of a second quantity of alkali metal silicate to form a hydrated aqueous slurry; adding a third quantity of anhydrous phosphate builder salt to said hydrated slurry to form a crutcher mix; spray drying said crutcher mix to form a particulate material, the weight ratio of said first quantity to said second quantity being from about 1.5 to about 5, the weight ratio of said first quantity to said third quantity being from about 0.3 to about 0.7, combining said particulate with from about 2 to about 40 percent by weight of a liquid or liquifiable organic surface active agent to form detergent beads, compressing said material to form coherent tablets and wherein said hydrating step is performed at a temperature suitable for hydrating said first quantity of phosphate builder salt and said slurry is raised to a temperature that would inhibit hydration of said third quantity of phosphate builder salt.
Claim 15
Independent Claim
170 words
A method for producing cleaning tablets comprising hydrating a first quantity of anhydrous phosphate builder salt in the presence of a second quantity of alkali metal silicate to form a hydrated aqueous slurry; adding a third quantity of anhydrous phosphate builder salt to said hydrated slurry to form a crutcher mix; spray drying said crutcher mix to form a particulate material, the weight ratio of said first quantity to said second quantity being from about 1.5 to about 5, the weight ratio of said first quantity to said third quantity being from about 0.3 to about 0.7, combining said particulate with from about 2 to about 40 percent by weight of a liquid or liquifiable organic surface active agent to form detergent beads, compressing said material to form coherent tablets and wherein said hydrating step is performed at a temperature suitable for hydrating said first quantity of phosphate builder salt and said slurry is raised to a temperature that would inhibit hydration of said third quantity of phosphate builder salt.
Claim 16
Dependent Claim
24 words
The method of claim 13 further including the steps of heating said hydrated slurry to a temperature from about 170° to about 200° F.
Claim 17
Dependent Claim
15 words
The method of claim 13 further including the addition of water to said hydrated slurry.
Claim 18
Dependent Claim
20 words
The method of claim 13 wherein the weight ratio of said first quantity to said third quantity is about 0.5.
Claim 19
Dependent Claim
18 words
The method of claim 13 wherein said crutcher mix contains from about 40 to about 55 percent solids.
Claim 20
Dependent Claim
41 words
The method of claim 13 wherein said spray drying takes place in a countercurrent spray tower at a spray pressure from about 200 psig to about 1000 psig and an inlet air temperature from about 500° F. to about 700° F.
Claim 21
Dependent Claim
40 words
The method of claim 13 including the addition of up to 10 percent by weight based on the crutcher solids, of builder salts chosen from the group consisting of carbonates, citrates and silicates having detergent building properties or combinations thereof.
Claim 22
Dependent Claim
21 words
The method of claim 13 further including the step of mixing said particulate material and organic material with a disintegrating aide.
Claim 23
Dependent Claim
31 words
The method of claim 13 wherein said compressing step is performed in a tableting press with the application of from about 3/4 to about 1 ton per square inch of pressure.
References Cited (Backward Citations)
US3081267A
Cited
US3344076A
Cited
US3247123A
Cited
US3331780A
Cited
US3417024A
Cited
US3338836A
Cited
US3367880A
Cited
US3329615A
Cited
US3423322A
Cited
US3383321A
Cited
US4276326A
Cited
US4310431A
Cited
US4370250A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-05-29 | 1987-11-28 | 1988-05-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-05-29 | 1991-11-28 | 1992-05-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-05-29 | 1995-11-28 | 1996-05-29 | $7700.00 | Window Closed / Lapsed |