IP Library › Granted Patent US 12,649,115
Granted Patent B2
US 12,649,115 · App. 18/643,339 · Granted Jun 9, 2026

Reducing surface and bulk contamination in plastic

Inventors: Norman Scott Broyles (Hamilton, OH); Dimitris Ioannis Collias (Mason, OH); Anthony Frederick Cappel (Cincinnati, OH)
Assignee: The Procter & Gamble Company
B01D11/0288B01D11/0203B08B3/04B29B17/00C08J11/08B01D11/0292B08B2220/00B08B2240/00B29B2017/0015B29B2017/0289B29B2017/0293B29K2105/26C08J7/02C08J2300/30
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Quick Facts
Patent No.
US 12,649,115
App. No.
18/643,339
Granted
Jun 9, 2026
Kind
B2
Abstract

The present invention generally relates to a method of reducing contamination from plastics. The resulting purer plastic can be used in demanding applications.

Claims (19)

1 . A method to extract contaminates from a first plastic to produce a purer plastic comprising:

a. providing a first plastic comprising individual contaminants, each individual contaminant having a concentration;

b. extracting said individual contaminates from said first plastic at a temperature and a pressure, using a solvent that comprises an organic solvent or mixture of organic solvents, in extraction stages, wherein the total extraction time is less than about 6 hours, to produce a purer plastic comprising individual contaminates, each having a concentration;

wherein said extraction stages are conducted at a solvent to first plastic mass ratio; wherein said solvent to first plastic mass ratio per stage at any time is less than 100:1; wherein said pressure is less than about 1,000 atm; wherein said first plastic individual contaminants comprise at least one of 4-tertpentylphenol, bisphenol A, OCDD, PCB 118, and 2-ethylhexyl phthalate; wherein at least one of the individual contaminants concentration in said purer plastic is reduced compared to its concentration in said first plastic by at least about 55% or LOQ; and

wherein the solvent should not significantly dissolve the first plastic at the temperature and pressure of the process; and

wherein the first plastic is a polyolefin.

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 plastic is a reclaimed plastic comprising at least one of a post-industrial or post-consumer film.

4 . The method of claim 1 , wherein said first plastic 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 plastic 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 plastic 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 plastic and the first plastic without surface printed ink.

7 . The method of claim 1 , wherein said solvent is purified after said stage or stages to allow re-use in the 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 solvent.

8 . The method of claim 1 , wherein said first plastic is a reclaimed plastic 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.

9 . The method of claim 1 , wherein said pressure is about atmospheric.

10 . The method of claim 9 , wherein said temperature is about the normal boiling point of ethyl acetate.

11 . The method of claim 1 , wherein said pressure is above atmospheric.

12 . The method of claim 11 , wherein said temperature is above the critical temperature of ethyl acetate.

13 . The method of claim 1 ; wherein said first plastic 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 comprising at least one of 4-tertpentylphenol, bisphenol A, OCDD, PCB 118, and 2-ethylhexyl phthalate; wherein said first plastic prior to surface washing has a surface area to volume ratio of greater than about 1 mm-1.

14 . The method of claim 1 ; wherein said first plastic 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 comprising at least one of 4-tertpentylphenol, bisphenol A, OCDD, PCB 118, and 2-ethylhexyl phthalate; wherein said first plastic prior to surface washing has a surface area to volume ratio of greater than about 1 mm-1; 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 plastic and the first plastic without surface printed ink.

Continuity (5)
Continuation 18127086 · Mar 28, 2023
Continuation 18114412 · Feb 27, 2023
Continuation 17229903 · Apr 14, 2021
Provisional Application 63010078 · Apr 15, 2020
Related Publication 20240299863A1 · Sep 12, 2024
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