Method for the production of superabsorbers

Patent metadata

Field	Value
Publication number	US-11535719-B2
Application number	US-201816649793-A
Country	US
Kind code	B2
Filing date	Oct 9, 2018
Priority date	Oct 18, 2017
Publication date	Dec 27, 2022
Grant date	Dec 27, 2022

Abstract

A process for producing superabsorbents, comprising the steps of i) classifying the superabsorbent particles by means of one or more sieves and ii) removing metallic impurities by means of one or more magnetic separators, wherein classification is accomplished using sieves made of a wire mesh, the wires of the wire mesh consist of a steel composed of at least 70% by weight of iron, at least 10% by weight of chromium and less than 2.5% by weight of nickel, and the throughput of superabsorbent particles in the magnetic separator is in the range from 2.0 to 6.5 g/s per cm2 of free cross-sectional area.

First claim

The invention claimed is:

1. A process for producing superabsorbent particles by polymerizing a monomer solution or suspension comprising
a) at least one ethylenically unsaturated monomer which bears an acid group and optionally 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,
comprising
i) classifying the superabsorbent particles by one or more sieves, and
ii) removing metallic impurities by one or more magnetic separators,
wherein step i) is conducted before step ii), which comprises classifying using sieves made of a wire mesh, wherein the wires of the wire mesh consist of a steel composed of at least 70% by weight of iron, at least 10% by weight of chromium, and less than 2.5% by weight of nickel, and throughput of superabsorbent particles in the magnetic separator is in the range from 2.0 to 6.5 g/s per cm 2 of free cross-sectional area.

2. The process according to claim 1 , wherein the wires of the wire mesh consist of a steel composed of at least 75% by weight of iron, at least 12% by weight of chromium, and less than 1.0% by weight of nickel.

3. The process according to claim 1 or 2 , wherein the wires of the wire mesh consist of a steel composed of at least 78% by weight of iron, at least 14% by weight of chromium, and less than 0.5% by weight of nickel.

4. The process according to claim 1 , wherein the wires of the wire mesh consist of a steel composed of at least 80% by weight of iron, at least 16% by weight of chromium, and less than 0.1% by weight of nickel.

5. The process according to claim 1 , wherein the throughput of superabsorbent particles in the magnetic separator is from 2.5 to 6.0 g/s per cm 2 of free cross-sectional area.

6. The process according to claim 1 , wherein the throughput of superabsorbent particles in the magnetic separator is from 3.0 to 5.5 g/s per cm 2 of free cross-sectional area.

7. The process according to claim 1 , wherein the throughput of superabsorbent particles in the magnetic separator is from 3.5 to 5.0 g/s per cm 2 of free cross-sectional area.

8. The process according to claim 1 , wherein the superabsorbent particles have a temperature of 40 to 90° C. in the classification and/or in the magnetic separator.

9. The process according to claim 1 , wherein the superabsorbent particles have a moisture content of 1% to 20% by weight in the classification and/or in the magnetic separator.

10. The process according to claim 1 , wherein the magnetic separator consists of individual bar magnets.

11. The process according to claim 10 , wherein the bar magnets have a diameter of 15 to 45 mm.

12. The process according to claim 10 , wherein the bar magnets are in a parallel grid arrangement.

13. The process according to claim 12 , wherein a horizontal distance between the bar magnets is from 10 to 35 mm.

14. The process according to claim 12 , wherein a vertical distance between the bar magnets is from 30 to 75 mm.

15. The process according to claim 1 , wherein step i) is the last classification in the process.

Assignees

• Basf Se

Inventors

• Stephan Oskar
• Gruenewald Gerald
• Weismantel Matthias
• Possemiers Karl
• Peterson Monte Alan
• Funk Ruediger
• Bertha Sylvia
• Catternan Tom

Classifications

• C08F220/06 Primary

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

• C08J2423/02

  not modified by chemical after treatment · CPC title

• C08F6/24

  Treatment of polymer suspensions {(C08F6/001, C08F6/006, C08F6/008, C08F6/02, C08F6/04 take precedence)} · CPC title

• C08J5/02 Primary

  Direct processing of dispersions, e.g. latex, to articles · CPC title

• C08J2429/04

  Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids · CPC title