Method of separating superabsorbent polymer particles from a solidified thermoplastic composition comprising polymers
A method for re-mobilizing superabsorbent polymer particles which have previously been immobilized by a solidified thermoplastic composition comprising at least 30 weight-% of a thermoplastic polymer. The superabsorbent polymer particles are separated from the solidified thermoplastic composition by using a supercritical fluid comprising carbon dioxide, propane, or mixtures thereof. Separation may be further improved by the use of one or more co-solvents.
1. A method for separating superabsorbent polymer particles from a solidified thermoplastic composition comprising at least about 30 weight percent of a thermoplastic polymer, based on the weight of the solidified thermoplastic composition, the method comprising the steps of:
a) providing agglomerates of the superabsorbent polymer particles and the solidified thermoplastic composition, wherein at least a part of the superabsorbent polymer particles are adhered to at least a part of the solidified thermoplastic composition; and
b) subjecting the agglomerates to a supercritical fluid comprising carbon dioxide, propane, or mixtures thereof.
2. The method according to claim 1 , wherein the supercritical fluid further comprises one or more co-solvents.
3. The method according to claim 2 , wherein the co-solvents are selected from the group consisting of ethanol, ethyl acetate, butane, butyl acetate, acetone, nitrous oxide, carbon dioxide, nitrogen, water, and mixtures thereof.
4. The method according to claim 2 , wherein the total amount of the one or more co-solvent is from about 0.1 weight percent to about 40 weight percent, based on the total weight of supercritical fluid.
5. The method according to claim 4 , wherein the total amount of the one or more co-solvent is from about 0.5 weight percent to about 30 weight percent, based on the total weight of supercritical fluid.
6. The method according to claim 5 , wherein the total amount of the one or more co-solvent is from about 1 weight percent to about 20 weight percent, based on the total weight of supercritical fluid.
7. The method according to claim 1 , wherein the solidified thermoplastic composition further comprises from about 1 weight percent to about 60 weight percent of resin, based on the weight of the solidified thermoplastic composition.
8. The method according to claim 7 , wherein the solidified thermoplastic composition further comprises from about 5 weight percent to about 40 weight percent of resin, based on the weight of the solidified thermoplastic composition.
9. The method according to claim 1 , wherein the solidified thermoplastic composition further comprises from about 1 weight percent to about 30 weight percent of oil, based on the weight of the solidified thermoplastic composition.
10. The method according to claim 9 , wherein the solidified thermoplastic composition further comprises from about 5 weight percent to about 30 weight percent of oil, based on the weight of the solidified thermoplastic composition.
11. The method according to claim 1 , wherein the solidified thermoplastic composition further comprises additives selected from the group of antioxidants, sand, silicone and surfactant, and wherein the overall amount of additives is not more than about 15 weight percent, based on the weight of the solidified thermoplastic composition.
12. The method according to claim 11 , wherein the overall amount of additives is not more than about 10 weight percent, based on the weight of the solidified thermoplastic composition.
13. The method according to claim 12 , wherein the overall amount of additives is not more than about 8 weight percent, based on the weight of the solidified thermoplastic composition.
14. The method according to claim 1 , wherein the agglomerates are subjected to a continuous stream of supercritical fluid.
15. The method according to claim 14 , wherein the supercritical fluid is recycled after it has been subjected to the agglomerates.
16. The method according to claim 1 , wherein the agglomerates are comprised in complete disposable absorbent articles or parts of absorbent articles, while being subjected to the supercritical fluid.
17. The method according to claim 16 , wherein the absorbent articles are diapers, training pants or sanitary napkins.
18. The method according to claim 16 , wherein the parts of the absorbent articles are absorbent cores.
19. The method according to claim 18 , wherein the absorbent cores further to the agglomerates comprise one or more nonwoven webs.
20. A method of providing a supercritical fluid for use in a method of separating superabsorbent polymer particles from a solidified thermoplastic composition comprising at least about 30% of a thermoplastic polymer, wherein at least a part of the superabsorbent polymer particles are adhered to at least a part of the composition and wherein the supercritical fluid comprises carbon dioxide, propane, or mixtures thereof.
21. A superabsorbent polymer particle produced by the method according to claim 1 .