Method for the production of superabsorbents

Patent metadata

Field	Value
Publication number	US-12059504-B2
Application number	US-201917272364-A
Country	US
Kind code	B2
Filing date	Sep 17, 2019
Priority date	Sep 28, 2018
Publication date	Aug 13, 2024
Grant date	Aug 13, 2024

Abstract

A process for producing superabsorbent particles by polymerizing a monomer solution or suspension, comprising drying of the resultant aqueous polymer gel in an air circulation belt drier, grinding, classifying, and optionally thermal surface postcrosslinking, wherein the aqueous polymer gel is introduced into the air circulation belt drier by means of an oscillating conveyor belt, the underside of the revolving conveyor belt is freed of adhering polymer gel by means of at least one stripper device, and the underside of the revolving conveyor belt is sprayed with water.

First claim

The invention claimed is:

1. A process for producing superabsorbent particles comprising polymerizing a monomer solution or suspension comprising
a) at least one ethylenically unsaturated monomer which bears an acid group and is at least partly neutralized,
b) at least one crosslinker,
c) at least one initiator,
d) optionally one or more ethylenically unsaturated monomer copolymerizable with the monomer mentioned under a), and
e) optionally one or more water-soluble polymer,
drying a resultant aqueous polymer gel in an air circulation belt drier, grinding, classifying, and optionally thermal surface postcrosslinking, wherein the aqueous polymer gel is introduced into the air circulation belt drier by an oscillating conveyor belt, the underside of the revolving oscillating conveyor belt is freed of adhering polymer gel by at least one stripper device, and the underside of the revolving oscillating conveyor belt is sprayed with 2 to 20 kg/h water by at least one spray nozzle.

2. The process according to claim 1 , wherein the distance of the stripper device from a discharge end of the oscillating conveyor belt is less than 20% of the length of the oscillating conveyor belt, where the length of the oscillating conveyor belt is a distance of a pivot axis from the discharge end.

3. The process according to claim 1 , wherein the stripper device mounted on the underside of the revolving oscillating conveyor belt is a scraper.

4. The process according to claim 3 , wherein the scraper is inclined at 5° to 45° relative to the horizontal counter to the running direction of the oscillating conveyor belt.

5. The process according to claim 3 , wherein a distance of the scraper from the underside of the revolving oscillating conveyor belt is from 0.1 to 5 mm.

6. The process according to claim 1 , wherein a distance of the at least one spray nozzle from the discharge end of the oscillating conveyor belt is 1% to 50% of the length of the conveyor belt, where the length of the oscillating conveyor belt is a distance of a pivot axis from a discharge end.

7. The process according to claim 1 , wherein a distance of the at least one spray nozzle from the conveyor belt is from 5 to 50 cm.

8. The process according to claim 1 , wherein the water is sprayed onto the underside of the revolving oscillating conveyor belt by at least one two-phase nozzle.

9. The process according to claim 1 , wherein the water is sprayed onto the underside of the revolving oscillating conveyor belt by at least one two-phase nozzle, and a weight ratio of atomizer gas to water is from 2 to 20.

10. The process according to claim 1 , wherein the water is sprayed onto the underside of the revolving oscillating conveyor belt by at least two two-phase nozzles.

11. The process according to claim 1 , wherein the at least one spray nozzle is beyond the stripper device in the running direction of the oscillating conveyor belt.

12. The process according to claim 1 , wherein the conveyor belt has a length of 2 to 10 m, where the length of the oscillating conveyor belt is the distance of a pivot axis from a discharge end.

13. The process according to claim 1 , wherein the surface of the oscillating conveyor belt at 23° C. has a contact angle with respect to water of at least 60°.

Assignees

• Basf Se

Inventors

• Callot Rene
• Funk Ruediger
• Krueger Marco
• Pfeiffer Thomas
• Possemiers Karl
• Schroeder Juergen
• Weismantel Matthias

Classifications

• C08F6/008

  Treatment of solid polymer wetted by water or organic solvents, e.g. coagulum, filter cakes · CPC title

• B08B1/165

  Scrapers · CPC title

• B08B1/20

  Cleaning of moving articles, e.g. of moving webs or of objects on a conveyor · CPC title

• C08J3/245 Primary

  Differential crosslinking of one polymer with one crosslinking type, e.g. surface crosslinking · CPC title

• C08F220/06 Primary

  Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof · CPC title