Ultrathin fluid-absorbent cores comprising adhesive and having very low dry SAP loss
US-9089624-B2 · Jul 28, 2015 · US
US9550213B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9550213-B2 |
| Application number | US-201414779990-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 18, 2014 |
| Priority date | Mar 28, 2013 |
| Publication date | Jan 24, 2017 |
| Grant date | Jan 24, 2017 |
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A process for classifying water-absorbing polymer particles, wherein screens having different mesh sizes are used before and after surface postcrosslinking to remove the undersize (fines).
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The invention claimed is: 1. A process for preparing water-absorbing polymer particles, comprising i) classifying the water-absorbing polymer particles, undersize being removed using a screen having the mesh size m 1 , ii) surface postcrosslinking the classified polymer particles, iii) classifying the surface postcrosslinked polymer particles, undersize being removed using a screen having the mesh size m 2 , and iv) recycling the undersize from step i) and iii), wherein a throughput per hour of the water-absorbing polymer particles in the course of classification in step i) is at least 100 kg/h per m 2 of screen area and the mesh size m 1 in step i) is greater than the mesh size m 2 in step iii). 2. The process according to claim 1 , wherein a product fraction is removed in step i) and/or step iii) using at least two screens of different mesh sizes. 3. The process according to claim 1 , wherein oversize is removed in step i) and/or step iii) using at least two screens of different mesh sizes. 4. The process according to claim 1 , wherein the mesh size m 1 in step i) is at least 180 μm. 5. The process according to claim 1 , wherein the mesh size m 2 in step iii) is not more than 150 μm. 6. The process according to claim 1 , wherein the mesh size m 1 in step i) is at least 30 μm greater than the mesh size m 2 in step iii). 7. The process according to claim 1 , wherein the water-absorbing polymer particles, during the classification in step i) and/or step iii), have a temperature of from 40 to 120° C. 8. The process according to claim 1 , wherein classification in step i) and/or step iii) is effected under reduced pressure. 9. The process according to claim 1 , wherein the water-absorbing polymer particles are flowed over by a gas stream during the classification in step i) and/or step iii). 10. The process according to claim 9 , wherein the gas stream has a temperature of from 40 to 120° C. 11. The process according to claim 9 , wherein the gas stream has a steam content of less than 5 g/kg. 12. The process according to claim 1 , wherein the water-absorbing polymer particles have been obtained by polymerizing an aqueous monomer solution. 13. The process according to claim 1 , wherein the water-absorbing polymer particles comprise at least 50 mol % of at least partly neutralized polymerized acrylic acid. 14. The process according to claim 1 , wherein the water-absorbing polymer particles, before step ii), have a centrifuge retention capacity of at least 15 g/g.
Homopolymers or copolymers of acids; Metal or ammonium salts thereof · CPC title
Constructional details of screens in general; Cleaning or heating of screens · CPC title
Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof · CPC title
Homopolymers or copolymers of acids; Metal or ammonium salts thereof · CPC title
Liquid-swellable gel-forming materials, e.g. super-absorbents · CPC title
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