Multistage processes for plastic functionalization using metal oxide catalysts

Patent metadata

Field	Value
Publication number	US-2025297373-A1
Application number	US-202519223947-A
Country	US
Kind code	A1
Filing date	May 30, 2025
Priority date	Jun 18, 2020
Publication date	Sep 25, 2025
Grant date	—

Abstract

Methods and systems for functionalizing polymers using a multistage packed bed reactor and transition metal oxide catalysts. A slurry comprising a mixture of plastic particles and a carrier fluid flows through the multistage packed bed reactor, which includes one or more catalyst beds containing metal oxide catalysts such as CuO, Cu 2 O, NiO, Fe 2 O 3 , MnO 2 , COO, CrO, VO, transition metal oxides, and combinations thereof. An applied potential between the anode and cathode of the reactor generates in-situ metal oxide catalysts, promoting the introduction of functional groups, including C—O, C═C, C═O, and OH bonds to create functionalized polymers. The functionalized polymers exhibit enhanced chemical reactivity and are suitable for various applications, including biomedical uses and membrane analytical devices. The process also allows catalyst recovery through electrodeposition, enabling sustainable and efficient plastic upcycling into high-value products.

First claim

What is claimed is:

1 . A method for functionalizing polymers, comprising:
(a) preparing a slurry comprising a mixture of plastic particles and a carrier fluid; (b) flowing the slurry into a multistage packed bed reactor, wherein:
(i) the multistage packed bed reactor comprises:
(A) one or more catalyst beds, wherein the one or more catalyst beds comprise a transition metal oxide catalyst selected from CuO, Cu 2 O, NiO, Fe 2 O 3 , MnO 2 , CoO, CrO, VO, transition metal oxides, and combinations thereof,
(B) an anode and a cathode, and
(C) in some embodiments a separator positioned between the anode and the cathode, and

(ii) the slurry is flown through at least one of the one or more catalyst beds;
(c) applying a voltage between the anode and the cathode to generate metal oxide catalysts in situ within the reactor; (e) oxidizing the plastic particles in the slurry, (f) introducing one or more functional groups comprising C—O, C═C, C═O, OH, and combinations thereof to create a functionalized polymer; and (f) recovering the functionalized polymer.

2 . The method of claim 1 , wherein the carrier fluid is an electrolyte.

3 . The method of claim 1 further comprising controlling the temperature within a range of 20° C. to 130° C. during the step of oxidizing the plastic particles in the slurry.

4 . The method of claim 1 , wherein the voltage is a pulsed potential modulated between −0.45 V and −0.25 V.

5 . The method of claim 1 , where the voltage controller is configured to use switching frequencies of about 5, 10, and 30 seconds.

6 . The method of claim 1 , wherein the functionalized polymer is further processed using electro-Fenton techniques to generate fatty acids, fuels, or monomers.

7 . The method of claim 1 , wherein the one or more functional groups comprise both the C═C and the C═O.

8 . The method of claim 1 , wherein the catalyst bed is in the form of a porous mesh or foam.

9 . The method of claim 1 further comprising the step of recovering dissolved catalysts from the carrier fluid using electrodeposition.

10 . The method of claim 1 , wherein the plastic particles comprise low-density polyethylene (LDPE), polypropylene (PP), polyester, nylon, acrylic, polyvinyl chloride.

11 . The method of claim 1 , wherein the plastic particles have a particle size in the range of about 10 microns to about 2000 microns.

12 . The method of claim 1 , wherein the carrier fluid comprises an aqueous medium selected from the group consisting of potassium hydroxide, sodium hydroxide, sulfuric acid, copper sulfate, nickel sulfate, and combinations thereof.

13 . The method of claim 1 , wherein the carrier fluid further comprises an additive selected from the group consisting of lactic acid, ethylenediaminetetraacetic acid (EDTA), and surfactants.

14 . A system for functionalizing polymers, comprising:
(a) a slurry reservoir configured to contain a slurry comprising plastic particles and a carrier fluid; (b) a multistage packed bed reactor comprising:
(i) a plurality of stages, each stage containing:
(A) a catalyst bed containing a metal oxide catalyst selected from a group consisting of CuO, Cu 2 O, NiO, Fe 2 O 3 , MnO 2 , CoO, CrO, VO, transition metal oxides, and combinations thereof,
(B) an anode and a cathode, and
(C) in certain embodiments a separator positioned between the anode and cathode;

(c) a voltage controller operable to apply a voltage between the anode and cathode to generate in-situ metal oxide catalysts; (d) a temperature controller operable to maintain a reaction temperature between 20° C. and 130° C.; (e) a pump configured to flow the slurry through the reactor; and (f) one or more product reservoirs operatively connected to the reactor to collect a functionalized polymer.

15 . The system of claim 14 , wherein the carrier fluid is an electrolyte.

13 . The system of claim 14 , wherein the voltage controller is configured to supply a pulsed potential modulated between −0.45 V and −0.25 V.

14 . The system of claim 14 , where the voltage controller is configured to use switching frequencies of about 5, 10, and 30 seconds.

15 . The system of claim 14 , wherein the catalyst bed is in the form of a porous mesh or foam.

16 . The system of claim 14 , wherein the plastic particles comprise low-density polyethylene (LDPE), polypropylene (PP), polyester, nylon, acrylic, polyvinyl chloride, or combinations thereof.

17 . The system of claim 14 , wherein the plastic particles have a particle size in the range of about 10 microns to about 2000 microns.

18 . The system of claim 14 , wherein the carrier fluid comprises an aqueous medium selected from the group consisting of potassium hydroxide, sodium hydroxide, sulfuric acid, copper sulfate, nickel sulfate, and combinations thereof.

19 . The system of claim 14 , wherein the carrier fluid further comprises an additive selected from the group consisting of lactic acid, ethylenediaminetetraacetic acid (EDTA), and surfactants.

20 . A functionalized polymer product, produced by the method of claim 1 , comprising:
(a) a polymer backbone comprising one or more functional groups selected from a group consisting of C—O, C═C, C═O, OH, and combinations thereof, (b) wherein the one or more functional groups are introduced into the polymer backbone through an electrochemical process utilizing metal oxide catalysts selected from a group consisting of CuO, Cu 2 O, NiO, Fe 2 O 3 , MnO 2 , CoO, CrO, VO, transition metal oxides, and combinations thereof.

Assignees

• Univ Texas Tech System

Inventors

• Botte Gerardine G
• Haque Zenifar

Classifications

• C08J11/16 Primary

  by treatment with inorganic material (C08J11/14 takes precedence) · CPC title

• C25B15/00

  Operating or servicing cells · CPC title

• C25B9/17

  Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof · CPC title

• C25B11/081

  the element being a noble metal · CPC title

• C25B11/061

  Metal or alloy · CPC title