Method for purifying reclaimed polymers
US-10961366-B2 · Mar 30, 2021 · US
US12102940B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12102940-B2 |
| Application number | US-202318470841-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 20, 2023 |
| Priority date | Apr 15, 2020 |
| Publication date | Oct 1, 2024 |
| Grant date | Oct 1, 2024 |
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.
The present invention generally relates to a method of reducing contamination from plastics. The resulting purer plastic can be used in demanding applications.
Opening claim text (preview).
What is claimed is: 1. A method to extract contaminates from a first polyolefin or polyolefin copolymer to produce a purer polyolefin or polyolefin copolymer comprising: a. providing a first polyolefin or polyolefin copolymer comprising individual contaminants, each individual contaminant having a concentration; b. extracting said individual contaminates from said first polyolefin or polyolefin copolymer at a temperature and a pressure, using a leaching solvent in extraction stages, wherein the total extraction time is less than about 6 hours, to produce a purer polyolefin or polyolefin copolymer comprising individual contaminates, each having a concentration; wherein said extraction is packed leaching wherein said temperature is between about 20 and 90° C.; wherein said extraction stages are conducted at a leaching solvent to first polyolefin or polyolefin copolymer mass ratio; wherein said leaching solvent to first polyolefin or polyolefin copolymer mass ratio per stage is less than about 5:1; wherein said pressure is about atmospheric; wherein said first polyolefin or polyolefin copolymer individual contaminants comprise at least one of 4-tertpentylphenol, bisphenol A, OCDD, PCB 118, and 2-ethylhexyl phthalate; wherein each individual contaminate concentration in said purer polyolefin or polyolefin copolymer is reduced compared to each individual contaminate concentration in said first polyolefin or polyolefin copolymer; and wherein the average of said reductions of said concentrations of said first polyolefin or polyolefin copolymer contaminants to said purer polyolefin or polyolefin copolymer contaminants is at least about 55% or LOQ; and wherein the leaching solvent does not significantly swell or dissolve the first polyolefin or polyolefin copolymer at the temperature and pressure of the process. 2. The method of claim 1 , wherein said number of stages is between about 1 and about 50. 3. The method of claim 1 , wherein said first polyolefin or polyolefin copolymer is a reclaimed polyolefin or polyolefin copolymer comprising at least one of a post-industrial or post-consumer film. 4. The method of claim 1 , wherein said first polyolefin or polyolefin copolymer has a mass average surface area to volume ratio of at least about 1 mm-1. 5. The method of claim 1 , wherein said first polyolefin or polyolefin copolymer is surface washed in a non-densified state by a surface washing process or processes prior to extraction and wherein said surface washing process or processes results in a greater than about an 80% reduction in loosely bound surface contamination; wherein said first polyolefin or polyolefin copolymer prior to surface washing has a surface area to volume ratio of greater than about 1 mm-1. 6. The method of claim 5 , wherein said surface washing process is de-inking; wherein said de-inking process results in a delta E percent change of less than about 10% between the de-inked first polyolefin or polyolefin copolymer and the first polyolefin or polyolefin copolymer without surface printed ink. 7. The method of claim 1 , wherein said period of time represented by the sum of times for the individual packed leaching stages is less than about 360 minutes. 8. The method of claim 1 , wherein said leaching solvent is purified after said packed leaching or said packed leaching stage or stages to allow re-use in the packed leaching process by a solvent purification process or processes; wherein said solvent purification process or processes comprises at least one stage of physical adsorption or absorption of the chemical contaminants from the contaminated leaching solvent. 9. The method of claim 1 , wherein said first polyolefin or polyolefin copolymer is a reclaimed polyolefin or polyolefin copolymer that is at least one of a post-industrial or post-consumer film; wherein said post-consumer film includes post-commercial film and/or post-household film. 10. The method of claim 1 , wherein said packed leaching extraction is immersion leaching; wherein the leaching solvent completely fills the void volume in the first polyolefin or polyolefin copolymer. 11. The method of claim 1 , wherein said packed leaching extraction is percolation leaching; wherein the leaching solvent does not completely fill the void volume in the first polyolefin or polyolefin copolymer.
Scrap {or recycled material} · CPC title
Dissolving the materials in gases or liquids · CPC title
Washing the materials in liquids · CPC title
Washing, rinsing · CPC title
Recovery of plastics or other constituents of waste material containing plastics; ({volume reduction of waste plastics, e.g. by mechanical compacting or melting disposal of solid waste B09B;} chemical recovery C08J11/00) · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.