Inhibitors of tyk2
US-2024425484-A1 · Dec 26, 2024 · US
US9422270B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9422270-B2 |
| Application number | US-201113703479-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 7, 2011 |
| Priority date | Jun 11, 2010 |
| Publication date | Aug 23, 2016 |
| Grant date | Aug 23, 2016 |
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Official abstract text for this publication.
The invention relates to a method for producing a free flowing flame retardant material, comprising steps of i. preparing an aqueous slurry from a freshly prepared moist melam having a water content of at least 8 wt. %, relative to the total weight of the moist melam, the slurry comprising water, melam and a water soluble polymeric binding agent, wherein the melam is present in an amount of 5-35 wt. % relative to the total weight of the slurry, and the water soluble polymeric binding agent is present in an amount of 0.5-8 wt. % relative to the total amount of melam and the water soluble polymeric binding agent; ii. drying the slurry in a fluid bed to form a granulate material; and iii. collecting the resulting granulate material. The invention also relates to a melam granulate material, obtainable by said process.
Opening claim text (preview).
The invention claimed is: 1. A process for the preparation of a melam granulate material, the process comprising steps of: (i) preparing an aqueous slurry from a freshly prepared moist melam having a water content of at least 8 wt. %, relative to the total weight of the moist melam, the slurry comprising water, melam and a water soluble polymeric binding agent, wherein the melam is present in an amount of 5-35 wt. % relative to the total weight of the slurry, and the water soluble polymeric binding agent is present in an amount of 0.5-8 wt. % relative to the total amount of melam and the water soluble polymeric binding agent; (ii) drying the slurry in fluid bed to form a granulate material consisting of granules comprised of melam particles bonded to each other with the polymeric binding agent, wherein the granules have a median particle size (d50) in a range of 100-1000 μm; and (iii) collecting the resulting granulate material. 2. The process according to claim 1 , wherein step (ii) comprises drying the granulate material to a water content of at most 12 wt. %, relative to the total weight of the granulate material. 3. The process according to claim 2 , wherein step (ii) comprises drying the granulate material to a water content of 0-6 wt. %, relative to the total weight of the granulate material. 4. The process according to claim 1 , wherein the median particle size (d50) of the granules is in the range of 200-900 μm. 5. The process according to claim 1 , wherein the granulate material has a mean particle size (d10) of at least 10 μm and/or a mean particle size (d90) of at most 3000 μm. 6. The process according to claim 1 , wherein the amount of the polymeric binding agent is in the range of 1-6 wt. %, relative to the total weight of the granulate material. 7. The process according to claim 1 , wherein the polymeric binding agent is at least one selected from the group consisting of polyvinyl alcohol, polyvinylpyrrolidone and polyvinylcaprolactam. 8. The process according to claim 1 , wherein the melam particles of the granulate material have a median primary particle size (d50) in a range of 0.1-50 μm. 9. The process according to claim 1 , wherein the granulate material obtained in step (ii) has a Carr-P bulk density in the range of 400-1000 kg/m 3 .
Solid polymers with solid and/or liquid additives · CPC title
by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain · CPC title
using agents to prevent the granules sticking together; Rendering particulate materials free flowing in general, e.g. making them hydrophobic · CPC title
in aqueous media · CPC title
Ingredients agglomerated by treatment with a binding agent · CPC title
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