Recycling of Superabsorbent Polymer Via UV Irradiation In Flow System
US-2021053028-A1 · Feb 25, 2021 · US
US11396587B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11396587-B2 |
| Application number | US-202016999139-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 21, 2020 |
| Priority date | Aug 23, 2019 |
| Publication date | Jul 26, 2022 |
| Grant date | Jul 26, 2022 |
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) and H 2 O 2 in a feed is converted with microwave (MW) irradiation into poly(acrylic acid) (PAA) in the product. The MW total energy used to convert SAP into PAA is less than 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 placing a feed into a reactor, irradiating said feed with microwave (MW) at a temperature, and producing a product comprising said PAA at a carbon yield; wherein said feed comprises said SAP at a concentration greater than about 3 wt % and hydrogen peroxide (H 2 O 2 ) at a concentration greater than about 0.5 wt % of said SAP concentration; wherein said feed has a residence time in said reactor between about 2 min and about 9 min; wherein said temperature is about 200° C.; wherein said carbon yield is greater than about 90%; and wherein said MW used to convert SAP to PAA requires a MW total energy of less than about 50 MJ/kg SAP. 2. The method of claim 1 , wherein said residence time is between about 4 min and about 6 min. 3. The method of claim 1 , wherein said residence time is about 5 min. 4. The method of claim 1 , wherein said SAP concentration is greater than about 5 wt %. 5. The method of claim 1 , wherein said SAP concentration is greater than about 10 wt %. 6. The method of claim 1 , wherein said MW total energy is less than about 12 MJ/kg SAP. 7. The method of claim 1 , wherein said MW total energy is less than about 6 MJ/kg SAP. 8. The method of claim 1 , wherein said SAP has degree of neutralization (DN) greater than about 50%. 9. The method of claim 1 , wherein said SAP has DN between about 65% and about 75%. 10. The method of claim 1 , wherein said carbon yield is greater than 95%. 11. The method of claim 1 , wherein said carbon yield is about 98%. 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 weight-average molecular weight less than about 500,000 g/mol. 14. The method of claim 1 , wherein said PAA has a weight-average molecular weight less than about 200,000 g/mol. 15. The method of claim 1 , wherein said PAA has a polydispersity index (PDI) between about 4.5 and about 3. 16. The method of claim 1 , wherein said PAA has a PDI between about 4 and about 3. 17. The method of claim 1 , wherein said PAA has a PDI of about 4.2. 18. A method for degrading a superabsorbent polymer (SAP) to poly(acrylic acid) (PAA) comprising placing a feed into a reactor, irradiating said feed with microwave (MW) at a temperature, and producing a product comprising said PAA at a carbon yield; wherein said feed comprises said SAP at a concentration of about 20 wt % and H 2 O 2 at a concentration of about 0.1 wt %; wherein said feed has a residence time in said reactor of about 5 min; wherein said temperature is about 200° C.; wherein said carbon yield is about 98%; wherein said MW used to convert SAP to PAA requires a MW total energy of less than about 50 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 SAP has DN between about 65% and about 75%. 20. The method of claim 18 , wherein said PAA has a PDI of about 4.2. 21. The method of claim 18 , wherein said weight-average molecular weight of said PAA is less than about 500,000 g/mol.
of esters containing only carbon, hydrogen, and oxygen, the oxygen atom being present only as part of the carboxyl radical · CPC title
by treatment with inorganic material (C08J11/14 takes precedence) · CPC title
Water soluble or water swellable polymers, e.g. aqueous gels · CPC title
Treatment by wave energy or particle radiation (C08J7/18 takes precedence) · CPC title
Homopolymers or copolymers of acids; Metal or ammonium salts thereof · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.