Powder and granule, process for making such powder and granule, and use thereof
US-2017058239-A1 · Mar 2, 2017 · US
US12415971B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12415971-B2 |
| Application number | US-202017784573-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 1, 2020 |
| Priority date | Dec 11, 2019 |
| Publication date | Sep 16, 2025 |
| Grant date | Sep 16, 2025 |
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A process for making a granule containing (A) at least one chelating agent selected from alkali metal salts of methyl glycine diacetic acid (MGDA) and of iminodisuccinic acid (IDS), and, optionally, (B) at least one homo- or copolymer of (meth) acrylic acid, partially or fully neutralized with alkali, the process including the steps of (a) providing an aqueous solution or slurry containing chelating agent (A) and, if applicable, (co) polymer (B), (b) removing most of the water by spray granulation in a fluidized bed, (c) treating the resultant granule in a vessel of which at least one part rotates around a horizontal axis and wherein the vessel is selected from paddle mixers, free-fall mixers and plough share mixers.
Opening claim text (preview).
The invention claimed is: 1. A process for making a granule comprising (A) at least one chelating agent comprising one or more alkali metal salts of methyl glycine diacetic acid (MGDA), and, optionally, (B) at least one homo-or copolymer of (meth) acrylic acid, partially or fully neutralized with alkali, said process comprising the steps of (a) providing an aqueous solution or slurry containing chelating agent (A) and, if applicable, (co) polymer (B), (b) removing most of said water by spray granulation in a fluidized bed, thereby obtaining a granule, (c) treating the resultant granule from step (b) with air or an inert gas in a vessel of which at least one part rotates around a horizontal axis and wherein said vessel is a paddle mixer, free-fall mixer, or plough share mixer. 2. The process according to claim 1 , wherein in step (b), a gas with an inlet temperature of at least 125° C. is used. 3. The process according to claim 1 , wherein the weight ratio of chelating agent (A) and (co) polymer (B) is in the range of from 1,000:1 to 7.5:1. 4. The process according to claim 1 , wherein step (b) is performed with a two-fluid nozzle. 5. The process according to claim 1 , wherein step (c) is performed over a period of 1 minute to 5 hours. 6. The process according to claim 1 , wherein step (c) is performed in a free-fall mixer. 7. The process according to claim 1 , wherein step (c) is followed by a step (d) including the removal of fines. 8. The process according to claim 1 , wherein (co) polymer (B) is selected from copolymers of (meth) acrylic acid and a comonomer bearing at least one sulfonic acid group per molecule. 9. The process according to claim 8 , wherein the comonomer bearing at least one sulfonic acid group per molecule is 2-acrylamido-2-methylpropanesulfonic acid.
Preparation in the form of powder by spray drying · CPC title
(Co)polymerised monomers containing sulfur, e.g. sulfonate · CPC title
Carboxylic amides, alkylolamides or imides {or their condensation products with alkylene oxides} · CPC title
the liquefied ingredients being sprayed or adsorbed onto solid particles · CPC title
one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads · CPC title
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