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 superabsorbent polymer particulate composition made by the process of including recycled superabsorbent polymer fines:
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 %;
c) polymerizing the mixture obtained in step b) to produce the superabsorbent polymer gel;
d) comminuting the superabsorbent polymer gel of step c) to form superabsorbent polymer particulate; and
e) coating the superabsorbent polymer particulate of step d) 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, wherein at least about 40% by weight of the superabsorbent polymer particulate has a particle size from about 300 μm to about 600 μm as measured by screening through a U.S. standard 30 mesh screen and retained on a U.S. standard 50 mesh screen wherein the superabsorbent polymer particulate composition made by the process as set forth in steps a) to e) above have values of an absorption under load at 0.9 psi and free swell gel bed permeability greater than the values of an absorption under load at 0.9 psi and free swell gel bed permeability of the superabsorbent polymer particulate composition made by the process of including recycled superabsorbent polymer fines wherein the recycled superabsorbent polymer fines are not treated with caustic solution containing from about 0.1 to about 12% caustic based on the weight of the superabsorbent polymer fines.
2. A sanitary article comprising the superabsorbent polymer particle composition made by the process of claim 1 .
3. A process for the production of a superabsorbent polymer gel based on recycling 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 monomer in which the content of the superabsorbent polymer fines relative to the total amount of the monomer is from about 0.1 to about 30 wt %;
c) polymerizing the mixture obtained in step b) to produce the polymer gel;
d) postneutralizing the polymer gel to form a superabsorbent polymer gel;
e) comminuting the superabsorbent polymer gel of step c) to form superabsorbent polymer particulate; and
f) coating the superabsorbent polymer particulate of step d) 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, wherein at least about 40% by weight of the superabsorbent polymer particulate has a particle size from about 300 μm to about 600 μm as measured by screening through a U.S. standard 30 mesh screen and retained on a U.S. standard 50 mesh screen wherein the superabsorbent polymer particulate composition made by the process as set forth in steps a) to f) above have values of an absorption under load at 0.9 psi and free swell gel bed permeability greater than the values of an absorption under load at 0.9 psi and free swell gel bed permeability of the superabsorbent polymer particulate composition made by the process of including recycled superabsorbent polymer fines wherein the recycled superabsorbent polymer fines are not treated with caustic solution containing from about 0.1 to about 12% caustic based on the weight of the superabsorbent polymer fines.
4. The process for the production of superabsorbent polymer gel of claim 3 wherein the superabsorbent polymer fines having an average particle size of less than about 150 μm.
5. The process for the production of superabsorbent polymer particulate of claim 4 , further comprising the steps of separating the superabsorbent polymer fines having a particle size of less than about 150 μm and recycling said superabsorbent polymer fines to the polymerizing step for forming said superabsorbent polymer gel.
6. The process for the production of superabsorbent polymer gel of claim 5 wherein the caustic is selected from sodium carbonate or sodium bicarbonate.