초록 ▼

This invention relates to a method for producing a water-absorbing polymer, including the following steps: (i) mixing (α1) 0.1 to 99.999 wt % polymerizable, ethylenically unsaturated, acid-group-containing monomers; (α2) 0 to 70 wt % polymerized ethylenically unsaturated, monomers copolymerizable wi

This invention relates to a method for producing a water-absorbing polymer, including the following steps: (i) mixing (α1) 0.1 to 99.999 wt % polymerizable, ethylenically unsaturated, acid-group-containing monomers; (α2) 0 to 70 wt % polymerized ethylenically unsaturated, monomers copolymerizable with (α1); (α3) 0.00 1 to 10 wt %, cross-linking agent(s); (α4) 0 to 30 wt % water-soluble polymers; and (α5) 0 to 20 wt % additive(s), wherein the total quantity by weight of (α1) to (α5) amounts to 100 wt %, (ii) radical polymerization while cross-linking, in order to form a hydrogel polymer, (iii) drying the hydrogel polymer, (iv) grinding and sifting the water-absorbing polymer, (v) surface post-cross-linking the hydrogel polymer, and (vi) drying and processing the polymer, wherein, before the admixture of the initiator and the start of radical polymerization, 0.01 to 5 wt % of a surfactant, relative to acrylic acid, 0.01 to 5 wt % foaming agent, are added.

대표청구항 ▼

1. A process for producing a water-absorbing polymer composition, comprising the process steps of (i) mixing (α1) 0.1 to 99.999% by weight of polymerizable, ethylenically unsaturated monomers containing acid groups, or salts thereof, or polymerizable, ethylenically unsaturated monomers including a p

1. A process for producing a water-absorbing polymer composition, comprising the process steps of (i) mixing (α1) 0.1 to 99.999% by weight of polymerizable, ethylenically unsaturated monomers containing acid groups, or salts thereof, or polymerizable, ethylenically unsaturated monomers including a protonated or quaternized nitrogen, or mixtures thereof, particular preference being given to mixtures including at least ethylenically unsaturated monomers containing acid groups,(α2) 0 to 70% by weight of polymerizable, ethylenically unsaturated monomers copolymerizable with (α1),(α3) 0.001 to 10% by weight of one or more crosslinkers,(α4) 0 to 30% by weight of water-soluble polymers, and(α5) 0 to 20% by weight of one or more assistants, where the sum of the weights of (α1) to (α5) is 100% by weight,to form an aqueous monomer solution,(ii) adding an initiator to promote free-radical polymerization with crosslinking to form a water-insoluble, aqueous untreated hydrogel polymer,(iii) drying the hydrogel polymer,(iv) grinding and sieving the hydrogel polymer to size,(v) surface postcrosslinking the ground and sieved hydrogel polymer and(vi) drying and finishing the water-absorbing polymer, wherein the aqueous monomer solution, prior to the addition of the initiator and the commencement of free-radical polymerization, is admixed with 0.01 to 5% by weight of at least one surfactant, based on the monomer containing acid group, from the group of the nonionic, ionic or amphoteric surfactants which are copolymerizable with the monomers specified in (α1) and optionally 0.01 to 5% by weight of a blowing agent having a particle size of 10 μm to 900 μm, based on the water-absorbing polymer composition; the Free Swell Rate (FSR) is in the range of from 0.3 to 0.65 g/g/s and the surface tension (ST) is above 50 mN/m. 2. The process according to claim 1, characterized in that the aqueous monomer solution at least one surfactant from the group of the nonionic, ionic or amphoteric surfactants and 0.01 to 5% by weight of blowing agent with a particle size of 10 μm to 900 μm added are, based on the water-absorbing polymer. 3. The process according to claim 1, characterized in that the surfactant is preferably selected from the group of the nonionic surfactants. 4. The process according to claim 1, characterized in that the surfactant is selected from the group of R1-(EO)n-block-(PO)m—R2 where R1 or R2 is a methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, n-pentyl, 2-methylbutyl, 2,2-dimethylpropyl, —OH, acetyl or allyl radical and n=2 to 20 and m=2 to 20. 5. The process according to claim 4, characterized in that the surfactant from the group of R1-(EO)n-block-(PO)m—R2 where n is 4 to 12 and m is 3 to 12. 6. The process according to claim 4, characterized in that the surfactant from the group of R1-(EO)n-block-(PO)m—R2 where n is 5 to 8 and m is 4 to 7. 7. The process according to claim 4, characterized in that, for n and m in the formula R1-(EO)n-block-(PO)m—R2, more preferably, 2≦m≦n≦20. 8. The process according to claim 4, characterized in that the R1 or R2 radicals are allyl or acetyl and R1 and/or R2 are a methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, n-pentyl, 2-methylbutyl, 2,2-dimethylpropyl, —OH, acetyl or allyl radical. 9. The process according to claim 4, characterized in that R1 or R2 is an allyl radical and the other radical is an acetyl or —OH radical. 10. The process according to claim 1, characterized in that the surfactant and the blowing agent are added together to the monomer solution. 11. The process according to claim 1, characterized in that the blowing agents consist of a powder of inorganic particles. 12. The process according to claim 1, characterized in that the blowing agents consist of sodium carbonate particles. 13. The process according to claim 1, characterized in that the blowing agent has a particle size of 10 μm to 900 μm. 14. The process according to claim 1, characterized in that more than 35% by weight of the blowing agents have a particle size of 100-300 μm. 15. The process according to claim 1, characterized in that the permeability, as the Saline Flow Conductivity, SFC (1.5 g), is in the range from 30 to 200 units. 16. The process according to claim 4, characterized in that the R1 and/or R2 are a methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, n-pentyl, 2-methylbutyl, 2,2-dimethylpropyl, —OH, acetyl or allyl radical.