Recycling of Superabsorbent Polymer Via Hydrothermal Microwave Processing
US-2021054164-A1 · Feb 25, 2021 · US
US11154839B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11154839-B2 |
| Application number | US-201916548873-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 23, 2019 |
| Priority date | Aug 23, 2019 |
| Publication date | Oct 26, 2021 |
| Grant date | Oct 26, 2021 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
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.
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.
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
Related publications grouped by family.
Answers are generated from the same data shown on this page.