Method for producing water-absorbing polymer particles with high swelling rate and high centrifuge retention capacity with simultaneously high permeability of the swollen gel bed
A process for producing water-absorbing polymer particles having high free swell rate and high centrifuge retention capacity with simultaneously high permeability of the swollen gel bed by polymerization of an aqueous monomer solution in a polymerization reactor having at least two shafts (kneaders) which rotate in an axially parallel manner, subsequent extrusion at high temperatures and thermal surface postcrosslinking.
1. A process for producing water-absorbing polymer particles by polymerizing a monomer solution or suspension comprising
a) an ethylenically unsaturated monomer which bears an acid group and may be at least partly neutralized,
b) at least one crosslinker,
c) at least one initiator,
d) optionally an ethylenically unsaturated monomer copolymerizable with the monomer mentioned under a), and
e) optionally one or more water-soluble polymer,
in a polymerization reactor having at least two shafts rotating in an axially parallel manner, drying the resulting polymer gel, grinding the dried polymer gel, classifying and thermally surface postcrosslinking, which process comprises using at least 0.25% by weight of the crosslinker b), based on the unneutralized monomer a), extruding the polymer gel through a perforated plate prior to drying, the polymer gel during the extrusion having a temperature greater than 80° C. and less than 60 kWh/t of specific mechanical energy being introduced in the course of extrusion, wherein the extruder has a ratio of length to diameter of less than 5.
2. The process according to claim 1 , wherein the polymer gel during the extrusion has a temperature of greater than 90° C.
3. The process according to claim 1 , wherein an orifice ratio of the perforated plate of the extruder is in the range from 10 to 20%.
4. The process according to claim 1 , wherein a pressure bearing on the perforated plate of the extruder is in the range from 15 to 35 bar.
5. The process according to claim 1 , wherein at least 0.4% by weight of the crosslinker b), based on the unneutralized monomer a), is used.
6. The process according to claim 1 , wherein extrusion is effected through holes having a diameter of 8 to 12 mm.
7. The process according to claim 1 , wherein the extruder is trace-heated.
8. The process according to claim 1 , wherein at least 50 mol % of monomer a) is partly neutralized acrylic acid.
9. The process according to claim 1 , wherein monomer a) has been neutralized to an extent of 25 to 85 mol %.
10. A process for producing water-absorbing polymer particles by polymerizing a monomer solution or suspension comprising
a) an ethylenically unsaturated monomer which bears an acid group and may be at least partly neutralized,
b) at least one crosslinker,
c) at least one initiator,
d) optionally an ethylenically unsaturated monomer copolymerizable with the monomer mentioned under a), and
e) optionally one or more water-soluble polymer,
in a polymerization reactor having at least two shafts rotating in an axially parallel manner, drying the resulting polymer gel, grinding the dried polymer gel, classifying and thermally surface postcrosslinking, which process comprises using at least 0.25% by weight of the crosslinker b), based on the unneutralized monomer a), extruding the polymer gel through a perforated plate prior to drying, the polymer gel during the extrusion having a temperature greater than 80° C. and less than 60 kWh/t of specific mechanical energy being introduced in the course of extrusion, wherein an orifice ratio of the perforated plate of the extruder is in the range from 10 to 20%.
11. The process according to claim 10 , wherein the polymer gel during the extrusion has a temperature of greater than 90° C.
12. The process according to claim 10 , wherein a pressure bearing on the perforated plate of the extruder is in the range from 15 to 35 bar.
13. The process according to claim 10 , wherein extrusion is effected through holes having a diameter of 8 to 12 mm.
14. The process according to claim 10 , wherein the extruder is trace-heated.
15. The process according to claim 10 , wherein at least 50 mol % of monomer a) is partly neutralized acrylic acid.
16. A process for producing water-absorbing polymer particles by polymerizing a monomer solution or suspension comprising
a) an ethylenically unsaturated monomer which bears an acid group and may be at least partly neutralized,
b) at least one crosslinker,
c) at least one initiator,
d) optionally an ethylenically unsaturated monomer copolymerizable with the monomer mentioned under a), and
e) optionally one or more water-soluble polymer,
in a polymerization reactor having at least two shafts rotating in an axially parallel manner, drying the resulting polymer gel, grinding the dried polymer gel, classifying and thermally surface postcrosslinking, which process comprises using at least 0.25% by weight of the crosslinker b), based on the unneutralized monomer a), extruding the polymer gel through a perforated plate prior to drying, the polymer gel during the extrusion having a temperature greater than 80° C. and less than 60 kWh/t of specific mechanical energy being introduced in the course of extrusion, wherein a pressure bearing on the perforated plate of the extruder is in the range from 15 to 35 bar.
17. The process according to claim 16 , wherein the polymer gel during the extrusion has a temperature of greater than 90° C.
18. The process according to claim 16 , wherein extrusion is effected through holes having a diameter of 8 to 12 mm.
19. The process according to claim 16 , wherein the extruder is trace-heated.
20. A process for producing water-absorbing polymer particles by polymerizing a monomer solution or suspension comprising
a) an ethylenically unsaturated monomer which bears an acid group and may be at least partly neutralized,
b) at least one crosslinker,
c) at least one initiator,
d) optionally an ethylenically unsaturated monomer copolymerizable with the monomer mentioned under a), and
e) optionally one or more water-soluble polymer,
in a polymerization reactor having at least two shafts rotating in an axially parallel manner, drying the resulting polymer gel, grinding the dried polymer gel, classifying and thermally surface postcrosslinking, which process comprises using at least 0.25% by weight of the crosslinker b), based on the unneutralized monomer a), extruding the polymer gel through a perforated plate prior to drying, the polymer gel during the extrusion having a temperature greater than 80° C. and less than 60 kWh/t of specific mechanical energy being introduced in the course of extrusion, wherein extrusion is effected through holes having a diameter of 8 to 12 mm.