Depolymerization of recovered plastic materials

US11840667B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11840667-B2
Application numberUS-202217859644-A
CountryUS
Kind codeB2
Filing dateJul 7, 2022
Priority dateJul 7, 2021
Publication dateDec 12, 2023
Grant dateDec 12, 2023

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Described herein are systems and methods for the depolymerization of polyethylene-based plastics. In one embodiment, a method is disclosed that comprises combining a polyethylene-based plastic with a solvent in a reactor to generate a plastic solvent mixture, heating the plastic solvent mixture in the reactor, and fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product. In another embodiment, a system is disclosed that comprises a solvent, and a reactor configured to receive the polyethylene-based plastic and the solvent and convert the polyethylene-based plastic into a gas phase product, a solid phase product, and a liquid phase product, the reactor being configured to operate at a temperature greater than 275° C. and at a pressure greater than 2 megapascals.

First claim

Opening claim text (preview).

What is claimed is: 1. A method for depolymerizing a polyethylene-based plastic, the method comprising: combining the polyethylene-based plastic with a solvent in a reactor to generate a plastic solvent mixture; heating the plastic solvent mixture in the reactor at a temperature no greater than 360° C. for no less than 70 minutes and no greater than 120 minutes; and fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product wherein the plastic solvent mixture is further combined with an ionic liquid catalyst prior to heating with. 2. The method according to claim 1 , wherein the solvent comprises at least one of water, methanol, ethanol, butanol, isopropyl alcohol, or acetone. 3. The method according to claim 2 , wherein the solvent comprises acetone. 4. The method according to claim 1 , wherein the ionic liquid catalyst comprises 1-butyl-3-methylimidazolium, bis[(perfluoroethyl)sulfonyl]-imide ([BMIM][PF2]), 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIM][BF4]), 1-butyl-3-methylimidazolium hexafluorophosphate ([BMIM][PF6]), or combinations thereof. 5. The method according to claim 1 , wherein the heating is performed at about 300° C. to 360° C. 6. The method according to claim 5 , wherein the heating is performed between about 340° C. to 360° C. 7. The method according to claim 1 , wherein the heating is performed at a pressure of about 2 megapascals to about 20 megapascals. 8. The method according to claim 7 , wherein the heating is performed at a pressure of about 8 megapascals to about 11 megapascals. 9. The method according to claim 1 , wherein the heating is performed for about 80 minutes to about 100 minutes. 10. The method according to claim 1 , wherein the plastic solvent mixture is combined in a weight/volume ratio of about 1 gram plastic:6 mL solvent to about 1 gram plastic:20 mL solvent. 11. The method according to claim 1 , further comprising separating the gas phase product and the liquid phase product using a combined membrane and adsorption process. 12. The method according to claim 1 , wherein at least 60% of the polyethylene-based plastic is converted into the gas phase product and the liquid phase product. 13. The method according to claim 1 , wherein at least 30% of the polyethylene-based plastic is converted into the liquid phase product. 14. The method according to claim 1 , wherein the liquid phase product has an oxygen/carbon ratio of about 0.01 to about 0.70. 15. The method according to claim 1 , wherein the liquid phase product has a hydrogen/carbon ratio of about 1.4 to about 2.0. 16. The method according to claim 1 , wherein the liquid phase product has a high heat value of about 35 MJ/kg to about 45 MJ/kg. 17. A method for depolymerizing a polyethylene-based plastic, the method comprising: combining the polyethylene-based plastic with a solvent comprising acetone in a reactor to generate a plastic solvent mixture; heating the plastic solvent mixture in the reactor at a temperature no greater than 360° C., at a pressure greater than 2 megapascals, and for no less than 70 minutes and no greater than 120 minutes; fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product; and separating the gas phase product and the liquid phase product using a combined membrane and adsorption process. 18. A method for depolymerizing a polyethylene-based plastic, the method comprising: combining the polyethylene-based plastic with a solvent comprising acetone in a reactor to generate a plastic solvent mixture; heating the plastic solvent mixture in the reactor at a temperature no greater than 360° C. for no less than 70 minutes and no greater than 120 minutes; and fractionating the plastic solvent mixture into a gas phase product, a solid phase product, and a liquid phase product.

Assignees

Inventors

Classifications

  • C10G1/10Primary

    from rubber or rubber waste · CPC title

  • One step being separation by permeation · CPC title

  • Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption) · CPC title

  • Pyrolysis reactions (of hydrocarbons C10G9/00) · CPC title

  • using selective solvents for polymer components · CPC title

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What does patent US11840667B2 cover?
Described herein are systems and methods for the depolymerization of polyethylene-based plastics. In one embodiment, a method is disclosed that comprises combining a polyethylene-based plastic with a solvent in a reactor to generate a plastic solvent mixture, heating the plastic solvent mixture in the reactor, and fractionating the plastic solvent mixture into a gas phase product, a solid phase…
Who is the assignee on this patent?
Deng Shuguang, Liu Yixin, Akula Kapil Chandra, and 2 more
What technology area does this patent fall under?
Primary CPC classification C10G1/10. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Dec 12 2023 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).