Recycling of superabsorbent polymer via UV irradiation in flow system

US11154839B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11154839-B2
Application numberUS-201916548873-A
CountryUS
Kind codeB2
Filing dateAug 23, 2019
Priority dateAug 23, 2019
Publication dateOct 26, 2021
Grant dateOct 26, 2021

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

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Poly(acrylic acid)-based superabsorbent polymer (SAP) in a feed stream is converted with UV irradiation into poly(acrylic acid) (PAA) in a flow system. The UV total energy used to convert SAP into PAA is less than about 50 MJ/kg SAP.

First claim

Opening claim text (preview).

What is claimed is: 1. A method for degrading a superabsorbent polymer (SAP) to poly(acrylic acid) (PAA) comprising flowing a feed stream comprising said SAP into a UV irradiation zone, irradiating said feed stream with UV, and producing a product stream comprising said PAA at the end of said irradiation zone; wherein said feed stream comprises said SAP at a concentration greater than about 1 wt %; wherein said feed stream has a residence time in said UV irradiation zone of less than about 120 s; and wherein said UV used to convert SAP to PAA requires a UV total energy of less than about 50 MJ/kg SAP. 2. The method of claim 1 , wherein said residence time is less than about 60 s. 3. The method of claim 1 , wherein said UV total energy is less than about 16 MJ/kg SAP. 4. The method of claim 1 , wherein said feed stream comprises SAP and water. 5. The method of claim 1 , wherein said feed stream comprises SAP and hydrogen peroxide. 6. The method of claim 1 , wherein said SAP has degree of neutralization (DN) greater than about 50%. 7. The method of claim 1 , wherein said SAP has DN between about 65% and about 75%. 8. The method of claim 1 , wherein said feed stream has a viscosity; wherein said product stream has a viscosity; wherein the ratio of the viscosity of the product stream to the viscosity of the feed stream is the viscosity ratio; and wherein the negative logarithm of said viscosity ratio is less than about 6. 9. The method of claim 1 , wherein said feed stream has a viscosity; wherein said product stream has a viscosity; wherein the ratio of the viscosity of the product stream to the viscosity of the feed stream is the viscosity ratio; and wherein the negative logarithm of said viscosity ratio is less than about 4. 10. The method of claim 1 , wherein said feed stream has a viscosity; wherein said product stream has a viscosity; wherein the ratio of the viscosity of the product stream to the viscosity of the feed stream is the viscosity ratio; and wherein the negative logarithm of said viscosity ratio is less than about 2. 11. The method of claim 1 , wherein said PAA has a weight-average molecular weight less than about 2,000,000 g/mol. 12. The method of claim 1 , wherein said PAA has a weight-average molecular weight less than about 1,000,000 g/mol. 13. The method of claim 1 , wherein said PAA has a polydispersity index (PDI) less than about 4. 14. The method of claim 1 , wherein said PAA is used to produce a recycled SAP; said SAP comprises PAA at a concentration; and wherein said PAA concentration is less than about 30%. 15. The method of claim 1 , wherein said PAA is used to produce a recycled SAP; wherein said recycled SAP has an amount of extractables; and wherein said amount of extractables is less than about 15%. 16. The method of claim 1 , wherein said PAA is used to produce a recycled SAP; wherein said recycled SAP has a swelling ratio; and wherein said swelling ratio is greater than about 45 g/g. 17. A method for degrading a superabsorbent polymer (SAP) to poly(acrylic acid) (PAA) comprising flowing a feed stream comprising said SAP into a UV irradiation zone, irradiating said feed stream with UV, and producing a product stream comprising PAA at the end of said UV irradiation zone; wherein said feed stream comprises water and SAP at a concentration greater than about 1 wt %; wherein said feed stream has a residence time in said UV irradiation zone of less than about 120 s; wherein said UV used to convert SAP to PAA requires a UV total energy of less than about 16 MJ/kg SAP; and wherein said PAA has a weight-average molecular weight less than about 1,000,000 g/mol. 18. A method for degrading a superabsorbent polymer (SAP) to poly(acrylic acid) (PAA) comprising flowing a feed stream comprising said SAP into a UV irradiation zone, irradiating said feed stream with UV, and producing a product stream comprising PAA at the end of said UV irradiation zone; wherein said feed stream comprises water and SAP at a concentration greater than about 5 wt %; wherein said feed stream has a residence time in said UV irradiation zone of less than about 120 s; wherein said UV used to convert SAP to PAA requires a UV total energy of less than about 16 MJ/kg SAP; and wherein said PAA has a weight-average molecular weight less than about 1,000,000 g/mol. 19. The method of claim 18 , wherein said feed stream has a viscosity; wherein said product stream has a viscosity; wherein the ratio of the viscosity of the product stream to the viscosity of the feed stream is the viscosity ratio; and wherein the negative logarithm of said viscosity ratio is less than about 4. 20. The method of claim 18 , wherein said SAP has DN between about 65% and about 75%. 21. The method of claim 18 , wherein said feed stream comprises SAP and hydrogen peroxide.

Assignees

Inventors

Classifications

  • by treatment with inorganic material (C08J11/14 takes precedence) · CPC title

  • Homopolymers or copolymers of acids; Metal or ammonium salts thereof · CPC title

  • obtained by reactions only involving carbon to carbon unsaturated bonds (macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds per se C08F) · CPC title

  • Biodegradable polymers · CPC title

  • Regeneration or reactivation by electric current, ultrasound or irradiation, e.g. electromagnetic radiation such as X-rays, UV, light, microwaves · CPC title

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What does patent US11154839B2 cover?
Poly(acrylic acid)-based superabsorbent polymer (SAP) in a feed stream is converted with UV irradiation into poly(acrylic acid) (PAA) in a flow system. The UV total energy used to convert SAP into PAA is less than about 50 MJ/kg SAP.
Who is the assignee on this patent?
Procter & Gamble
What technology area does this patent fall under?
Primary CPC classification B01J20/3441. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Oct 26 2021 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 3 related publications on this page (citations in our corpus or others sharing the same primary CPC).