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US-9453133-B2 · Sep 27, 2016 · US
US10835634B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10835634-B2 |
| Application number | US-201615564212-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 24, 2016 |
| Priority date | Apr 7, 2015 |
| Publication date | Nov 17, 2020 |
| Grant date | Nov 17, 2020 |
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A process for agglomerating superabsorbent particles, wherein polymer particles having a particle size of 250 μm or less are dispersed in a hydrophobic organic solvent, the dispersed polymer particles are mixed with an aqueous monomer solution, the total amount of water applied to the dispersed polymer particles being at least 100% by weight, based on the dispersed polymer particles, and the monomer solution is polymerized.
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The invention claimed is: 1. A process for agglomerating superabsorbent particles comprising (A) polymerizing a first aqueous monomer solution comprising a) at least one ethylenically unsaturated monomer which bears an acid group and optionally at least partly neutralized, b) optionally one or more 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 to provide polymer particles, optionally drying and/or comminuting the polymer particles, removing polymer particles having a particle size of 250 μm or less, dispersing the polymer particles having a particle size of 250 μm or less in a hydrophobic organic solvent, mixing the dispersed polymer particles with a second aqueous monomer solution comprising a) at least one ethylenically unsaturated monomer which bears an acid group and optionally at least partly neutralized, b) optionally one or more 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, wherein the first aqueous monomer solution and the second aqueous monomer solution may be the same or different and a total amount of water applied to the dispersed polymer particles with the second aqueous monomer solution being at least 100% by weight, based on the dispersed polymer particles, and polymerizing the second aqueous monomer solution to provide agglomerated particle superabsorbent. 2. The process according to claim 1 , wherein polymer particles having a particle size of 200 μm or less are removed and dispersed in the hydrophobic organic solvent. 3. The process according to claim 1 , wherein polymer particles having a particle size of 150 μm or less are removed and dispersed in the hydrophobic organic solvent. 4. The process according to claim 1 , wherein the amount of water applied with the second monomer solution is at least 150% by weight, based on the dispersed polymer particles. 5. The process according to claim 1 , wherein the amount of water applied with the second monomer solution is at least 175% by weight, based on the dispersed polymer particles. 6. The process according to claim 1 , wherein the second monomer solution comprises from 0.01 to 0.50 mmol of crosslinker b), based on 1 mol of monomer a). 7. The process according to claim 1 , wherein the second monomer solution comprises from 0.02 to 0.25 mmol of crosslinker b), based on 1 mol of monomer a). 8. The process according to claim 1 , wherein the second monomer solution comprises from 0.05 to 0.15 mmol of crosslinker b), based on 1 mol of monomer a). 9. The process according to claim 1 , wherein the first monomer solution is polymerized by dropletizing polymerization. 10. The process according to claim 9 , wherein the polymer particles are removed from an offgas of the dropletizing polymerization by means of a filter or cyclone. 11. The process according to claim 1 , wherein the first monomer solution is polymerized by suspension polymerization and the resulting polymer particles are dried. 12. The process according to claim 1 , wherein the first monomer solution is polymerized by solution polymerization and the resulting polymer particles are dried and comminuted. 13. The process according to claim 11 , wherein the polymer particles are removed by means of a sieve having a mesh size of 250 μm or less. 14. The process according to claim 11 , wherein the polymer particles are removed by means of a sieve having a mesh size of 200 μm or less. 15. The process according to claim 11 , wherein the polymer particles are removed by means of a sieve having a mesh size of 150 μm or less. 16. The process according to claim 12 , wherein the polymer particles are removed by means of a sieve having a mesh size of 250 μm or less. 17. The process according to claim 12 , wherein the polymer particles are removed by means of a sieve having a mesh size of 200 μm or less. 18. The process according to claim 12 , wherein the polymer particles are removed by means of a sieve having a mesh size of 150 μm or less. 19. A process for agglomerating superabsorbent particles comprising: (a) providing superabsorbent particles having a particle size of 250 μm or less; (b) dispersing superabsorbent particles in a hydrophobic organic solvent; (c) mixing the dispersed superabsorbent particles with an aqueous monomer solution comprising: i) at least one ethylenically unsaturated monomer which bears an acid group and optionally at least partly neutralized, ii) optionally one or more crosslinker, iii) at least one initiator, iv) optionally one or more ethylenically unsaturated monomer copolymerizable with the monomer mentioned under i), and v) optionally one or more water-soluble polymer, wherein a total amount of water applied to the dispersed superabsorbent particles with the aqueous monomer solution being at least 100% by weight, based on the dispersed polymer superabsorbent particles, and polymerizing the second monomer solution to provide agglomerated superabsorbent particles. 20. The process of claim 19 comprising providing superabsorbent particles having a particle size of 200 μm or less.
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