US2009239071A1PendingUtilityA1
Method for Producing Water-Absorbent Polymer Particles with a Higher Permeability by Polymerising Droplets of a Monomer Solution
Est. expiryJul 19, 2026(~0 yrs left)· nominal 20-yr term from priority
Inventors:Uwe StuevenMatthias WeismantelHeide WilfriedMarco KrügerVolker SeidiStefan BleiDennis LöschRüdiger FunkAnnemarie Hillebrecht
B29K 2033/04A61L 15/24B29K 2995/0092C08F 2/34C08F 2500/24C08F 2400/00C08F 222/385B29B 9/10C08F 220/06C08F 222/103Y10T428/2982C08F 222/10A61L 15/60
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Claims
Abstract
A process for preparing water-absorbing polymer beads with high permeability by polymerizing droplets of a monomer solution, comprising monomers bearing acid groups, in a gas phase surrounding the droplets, wherein the monomer solution comprises polyvalent cations and the polymer beads have a mean diameter of at least 150 μm.
Claims
exact text as granted — not AI-modified1 . A process for preparing water-absorbing polymer beads comprising polymerizing droplets of a monomer solution comprising
a) at least one ethylenically unsaturated monomer bearing acid groups, b) at least one crosslinker, c) at least one initiator, and d) water,
in a gas phase surrounding the droplets, wherein the monomer solution comprises polyvalent cations and the polymer beads have a mean diameter of at least 150 μm.
2 . The process according to claim 1 , wherein the monomer solution comprises from 0.001 to 0.25% by weight of polyvalent cations, based on monomer a).
3 . The process according to claim 1 , wherein the polyvalent cation is at least trivalent.
4 . The process according to claim 1 , wherein monomer a) is acrylic acid to an extent of at least 50 mol %.
5 . The process according to claim 1 , wherein the polymer beads have a mean diameter of at least 200 μm.
6 . The process according to claim 1 , wherein at least 90% by weight of the polymer beads have a diameter of from 100 to 800 μm.
7 . The process according to claim 1 , wherein a carrier gas flows through a reaction chamber.
8 . The process according to claim 7 , wherein the carrier gas leaving the reaction chamber is recycled at least partly after one pass.
9 . The process according to any of claim 7 , wherein an oxygen content of the carrier gas is from 0.001 to 0.15% by volume.
10 . The process according to claim 1 , wherein the polymer beads are dried and/or postcrosslinked in at least one further process step.
11 . Water-absorbing polymer beads prepared according to the process of claim 1 .
12 . Water-absorbing polymer beads having a mean sphericity of at least 0.84, a content of hydrophobic solvents of less than 0.005%, by weight, and a permeability of at least 5×10−7 cm 3 s/g.
13 . Polymer beads according to claim 12 , having a centrifuge retention capacity of at least 10 g/g.
14 . Polymer beads according to claim 12 , having a mean diameter of at least 200 μm.
15 . Polymer beads according to claim 12 , wherein at least 90%, by weights of the polymer beads have a diameter of from 100 to 800 μm.
16 . Polymer beads according to claim 12 , comprising at least partly of polymerized ethylenically unsaturated acid-bearing monomers.
17 . Polymer beads according to claim 16 , wherein the acid groups of the polymerized ethylenically unsaturated monomer are at least partly neutralized.
18 . Polymer beads according to claim 16 , wherein the ethylenically unsaturated monomer is acrylic acid to an extent of at least 50 mol %.
19 . Polymer beads according to claim 12 , which comprise polyvalent cations.
20 . (canceled)
21 . A hygiene article comprising polymer beads according to claim 12 .
22 . A hygiene article comprising polymer beads prepared according to the process of claim 1 .Cited by (0)
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