Recycling superabsorbent polymer fines
A process is described for recycling superabsorbent polymer fines into a process that includes treating the superabsorbent polymer fines with caustic and a polymerization step for making the superabsorbent polymer gel. The process requires treating the superabsorbent polymer fines with a caustic, followed by mixture with polymerizable monomer solution, and polymerizing the mixture of the superabsorbent polymer fines and monomer to form the aqueous fluid absorbent polymer. In the process, the fines are incorporated into the new polymer gel and become indistinguishable there from. The gel may then be comminuted into a particulate dried and then separated into a portion having a desired minimum particle size in a fines portion having less than the desired size. The particulate may then be coated with a surface crosslinking agent and surface additives and heated for surface conversion.
1. A process for the production of a superabsorbent polymer gel with recycled superabsorbent polymer fines comprising the following steps:
a) treating the superabsorbent polymer fines with a caustic solution containing from about 0.1 to about 12% caustic based on the weight of the superabsorbent polymer fines to form caustic treated superabsorbent polymer fines;
b) mixing the caustic treated superabsorbent polymer fines obtained in step a) with a polymerization solution containing at least one cross linking agent and a partially neutralized monomer in which the content of the caustic treated superabsorbent polymer fines relative to the total amount of the monomer is from about 0.1 to about 30 wt %; and
c) polymerizing the mixture obtained in step b) to produce the superabsorbent polymer gel.
2. The process for the production of superabsorbent polymer gel of claim 1 wherein the superabsorbent polymer fines have an average particle size of less than about 150 μm.
3. The process for the production of superabsorbent polymer gel of claim 2 further comprising the steps to make a superabsorbent polymer particulate wherein the steps comprise comminuting the superabsorbent polymer gel from said polymerizing step; drying said comminuted polymer; separating said dried superabsorbent polymer particulate into a portion having a desired particle size from about 150 μm to about 850 μm as measured by screening through a U.S. standard 20 mesh screen and retained on a U.S. standard 100 mesh screen.
4. The process for the production of superabsorbent polymer particulate of claim 3 further comprising the steps to make a superabsorbent polymer composition wherein the steps comprise coating the superabsorbent polymer particulate with a surface crosslinking agent and surface additives, heating said coated polymer, separating said dried superabsorbent polymer particulate into a portion having a desired particle size from about 150 μm to about 850 μm as measured by screening through a U.S. standard 20 mesh screen and retained on a U.S. standard 100 mesh screen.
5. The process for the production of superabsorbent polymer particulate of claim 3 , further comprising the steps of separating the superabsorbent polymer fines having a particle size of less than about 150 μm, treating the superabsorbent polymer fines with a caustic solution containing from about 0.1 to about 12% caustic based on the weight of the superabsorbent polymer fines to form caustic treated superabsorbent polymer fines, and recycling said caustic treated superabsorbent polymer fines to the polymerizing step for forming said superabsorbent polymer gel.
6. The process for the production of superabsorbent polymer composition of claim 4 further comprising the steps of separating the superabsorbent polymer fines having a particle size of less than about 150 μm, treating the superabsorbent polymer fines with a caustic solution containing from about 0.1 to about 12% caustic based on the weight of the superabsorbent polymer fines to form caustic treated superabsorbent polymer fines, and recycling said caustic treated superabsorbent polymer fines to the polymerizing step for forming said superabsorbent polymer gel.
7. The process for the production of superabsorbent polymer gel of claim 1 wherein the caustic is sodium hydroxide.
8. The process for the production of superabsorbent polymer gel of claim 1 wherein the caustic is selected from sodium carbonate or sodium bicarbonate.
9. The process for the production of superabsorbent polymer particulate of claim 3 wherein the caustic is selected from sodium hydroxide, sodium carbonate or sodium bicarbonate.
10. The process for the production of superabsorbent polymer particulate of claim 3 wherein said monomer is an ethylenically unsaturated monomers selected from amide, carboxylic acid or its esters, vinyl amines or their salts or mixtures thereof.
11. The process for the production of superabsorbent polymer gel of claim 1 wherein said polymer is a cross linked polymer of polyacrylic acid, sodium polyacrylate or copolymers thereof.
12. The process for the production of superabsorbent polymer gel of claim 1 wherein said monomer solution includes an initiator.
13. A process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel, compromising the steps of:
a) treating the superabsorbent polymer fines with a caustic solution containing from about 0.1 to about 12% caustic based on the weight of the superabsorbent polymer fines to form caustic treated superabsorbent polymer fines; and
b) mixing the caustic treated superabsorbent polymer fines obtained in step a) with a polymerization solution containing at least one cross-linking-agent and a partially neutralized monomer in which the content of the caustic treated superabsorbent polymer fines relative to the total amount of the monomer is from about 0.1 to about 30 wt %; and c) polymerizing the mixture obtained in step b) to produce a superabsorbent polymer gel.
14. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 13 wherein the superabsorbent polymer fines have an average particle size of less than about 150 μm.
15. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 14 further comprising the steps to make a superabsorbent polymer particulate wherein the steps comprise comminuting the superabsorbent polymer gel from said polymerizing step; drying said comminuted polymer; separating said dried superabsorbent polymer particulate into a portion having a desired particle size from about 150 μm to about 850 μm as measured by screening through a U.S. standard 20 mesh screen and retained on a U.S. standard 100 mesh screen.
16. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 15 further comprising the steps to make a superabsorbent polymer composition wherein the steps comprise coating the superabsorbent polymer particulate with a surface crosslinking agent and surface additives, heating said coated polymer, separating said dried superabsorbent polymer particulate into a portion having a desired particle size from about 150 μm to about 850 μm as measured by screening through a U.S. standard 20 mesh screen and retained on a U.S. standard 100 mesh screen.
17. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 15 , further comprising the steps of separating the superabsorbent polymer fines having a particle size of less than about 150 μm, treating the superabsorbent polymer fines with caustic to form caustic treated superabsorbent polymer fines, and recycling said caustic treated superabsorbent polymer fines to the polymerizing step for forming said superabsorbent polymer gel.
18. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 16 further comprising the steps of separating the superabsorbent polymer fines having a particle size of less than about 150 μm treating the superabsorbent polymer fines with caustic to form caustic treated superabsorbent polymer fines, and recycling said caustic treated superabsorbent polymer fines to the polymerizing step for forming said superabsorbent polymer gel.
19. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 13 wherein the caustic is sodium hydroxide.
20. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 13 wherein the caustic is selected from sodium carbonate or sodium bicarbonate.
21. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 13 wherein said monomer solution includes water-soluble ethylenically unsaturated monomer mixtures or salts thereof.
22. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 21 wherein said ethylenically unsaturated monomer is an amide, carboxylic acid or its esters, vinyl amines or their salts or mixtures thereof.
23. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 13 wherein said polymer is a cross linked polymer of polyacrylic acid, sodium polyacrylate or copolymers thereof.
24. The process for recycling superabsorbent polymer fines in the production of superabsorbent polymer gel of claim 13 wherein said monomer solution includes an initiator.
25. A process for the production of a superabsorbent polymer gel with recycled superabsorbent polymer fines to form caustic treated superabsorbent polymer fines comprising the following steps:
a) treating the caustic treated superabsorbent polymer fines with a caustic solution selected from sodium hydroxide, or sodium carbonate, or sodium bicarbonate, to form caustic treated superabsorbent polymer fines;
b) mixing the caustic treated superabsorbent polymer fines obtained in step a) with a polymerization solution containing at least one cross linking agent and a partially neutralized monomer in which the content of the caustic treated superabsorbent polymer fines relative to the total amount of the monomer is from about 0.1 to about 30 wt %; and
c) polymerizing the mixture obtained in step b) to produce the superabsorbent polymer gel.
26. The process for the production of superabsorbent polymer gel of claim 25 wherein the superabsorbent polymer fines have an average particle size of less than about 150 μm.
27. The process for the production of superabsorbent polymer gel of claim 25 further comprising the steps to make a superabsorbent polymer particulate wherein the steps comprise comminuting the superabsorbent polymer gel from said polymerizing step; drying said comminuted polymer; separating said dried superabsorbent polymer particulate into a portion having a desired particle size from about 150 μm to about 850 μm as measured by screening through a U.S. standard 20 mesh screen and retained on a U.S. standard 100 mesh screen.
28. The process for the production of superabsorbent polymer particulate of claim 27 further comprising the steps to make a superabsorbent polymer composition wherein the steps comprise coating the superabsorbent polymer particulate with a surface crosslinking agent and surface additives, heating said coated polymer, separating said dried superabsorbent polymer particulate into a portion having a desired particle size from about 150 μm to about 850 μm as measured by screening through a U.S. standard 20 mesh screen and retained on a U.S. standard 100 mesh screen.