Method for formation of micro-prilled polymers
US-2015374629-A1 · Dec 31, 2015 · US
US10683371B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10683371-B2 |
| Application number | US-201615773591-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 15, 2016 |
| Priority date | Nov 17, 2015 |
| Publication date | Jun 16, 2020 |
| Grant date | Jun 16, 2020 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to an apparatus for producing pulverulent poly(meth)acrylate, comprising a reactor for droplet polymerization having an apparatus for dropletization of a monomer solution for the preparation of the poly(meth)acrylate having holes through which the monomer solution is introduced, an addition point for a gas above the apparatus for dropletization, at least one gas withdrawal point on the circumference of the reactor, a fluidized bed and an apparatus for product discharge from the fluidized bed. The apparatus for product discharge comprises a discharge apparatus, with a backup segment (39) disposed above the discharge apparatus.
Opening claim text (preview).
The invention claimed is: 1. An apparatus for producing pulverulent poly(meth)acrylate, comprising a reactor for droplet polymerization having an apparatus for dropletization of a monomer solution for the preparation of the poly(meth)acrylate having holes through which the monomer solution is introduced, an addition point for a gas above the apparatus for dropletization, at least one gas withdrawal point on the circumference of the reactor, a fluidized bed and an apparatus for product discharge from the fluidized bed, wherein the apparatus for product discharge comprises a discharge apparatus, with a backup segment disposed above the discharge apparatus, the backup segment serving as a gas barrier in that by accumulation of product a compaction results. 2. The apparatus according to claim 1 , wherein the backup segment has an upper sensor for detecting a maximum fill level and a lower sensor for detecting a minimum fill level. 3. The apparatus according to claim 2 , wherein a closed-loop fill level control system is included, in which the upper sensor detects a first upper fill level and, when the latter is attained, a feed is reduced, and detects a second upper fill level and, when the latter is attained, the feed is closed, and the lower sensor detects a first lower fill level and, when the latter is attained, the product flow out of the apparatus for product discharge is reduced, and detects a second lower fill level and, when the latter is attained, the apparatus for product discharge is closed, such that no product is withdrawn. 4. The apparatus according to claim 1 , wherein a closure element is disposed above the backup segment. 5. The apparatus according to claim 1 , wherein a solids comminutor is disposed above the backup segment. 6. The apparatus according to claim 5 , wherein the solids comminutor is a lump breaker. 7. The apparatus according to claim 6 , wherein the lump breaker is a finger breaker having a breaking grid and a rotating breaking tool. 8. The apparatus according to claim 1 , wherein the discharge apparatus is a star feeder, a flap, a screw conveyor or a segmented ball valve. 9. The apparatus according to claim 1 , wherein a gas supply is disposed in the backup segment in order to introduce gas into the backup segment. 10. The apparatus according to claim 1 , wherein the apparatus for product discharge is heatable. 11. The apparatus according to claim 10 , wherein the apparatus for product discharge is heated by virtue of a solids comminutor, the backup segment and/or the discharge apparatus having electrical heating, a jacket or externally mounted heating coils, it being possible for a heating medium to flow through the jacket or the heating coils. 12. The apparatus according to claim 1 , wherein the gas withdrawal point is connected to an apparatus for fine dust removal and the apparatus for fine dust removal has a solids discharge comprising a discharge apparatus and, above the discharge apparatus, a closure element. 13. The apparatus according to claim 12 , wherein the discharge apparatus from the solids discharge of the apparatus for fine dust separation is a star feeder, a flap, a conveying screw or a segmented ball valve. 14. The apparatus according to claim 12 , wherein the closure element in the solids discharge of the apparatus for fine dust separation is a flap, a slide vane, a segmented ball valve or another valve. 15. The apparatus according to claim 12 , wherein at least one fill level sensor is positioned above the closure element. 16. The apparatus according to claim 1 , wherein the apparatus for product discharge and/or the solids discharge of an apparatus for fine dust removal open(s) into a suction line which pneumatically conveys the pulverulent poly(meth)acrylate onward.
in a gaseous medium {(if combined with suspending the material in a gas, e.g. fluidised beds B01J2/16)} · CPC title
Polymerisation in gaseous state · CPC title
Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title
using suction · CPC title
with acrylic or methacrylic acids · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.