MXene-Supported Metal Catalyst for Plastic Hydrogenolysis

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Solution Overview

Problem

Current methods for managing plastic waste, particularly polyolefins, are inefficient and environmentally harmful, with low recycling rates and high costs associated with incineration and pyrolysis, while also failing to effectively convert plastic waste into valuable products.

Innovation Solution

A catalytic hydrogenolysis method is developed to convert polyethylene (PE) into gasoline- and diesel-range fuels using a catalyst comprising a MXene support and a supported metal, such as copper, with a narrow carbon number distribution.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional treatment methods (incineration, mechanical recycling, pyrolysis) are used for polyolefin waste, then waste management is attempted, but conversion to valuable products is ineffective and environmental harm persists

Engineering Contradiction:
Improveconversion efficiency of plastic waste to valuable productsVSAvoidgreenhouse gas emissions and toxic gas release
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent employs catalyst composition optimization (specific metal ratios, support material selection) and reaction condition parameter tuning (temperature, pressure, hydrogen flow rate) to transform the hydrogenolysis process, achieving high-selectivity conversion of polyolefins to valuable liquid fuels and chemicals while minimizing harmful emissions

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention converts polyolefin plastic waste, which is notoriously difficult to recycle due to its inertness and long degradation time, into valuable liquid fuels and chemical feedstocks through catalytic hydrogenolysis, transforming an environmental burden into an economic resource

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

2Use of energy by moving object

If incineration is used for plastic waste treatment, then energy recovery is achieved, but greenhouse gases and toxic gases are released

Engineering Contradiction:
Improveenergy recovery from wasteVSAvoidgreenhouse gas and toxic gas emissions
Core Design Contradiction:
Use of energy by moving objectVSObject-generated harmful factors

Solution Approach 1:

The patent replaces the thermal combustion process (incineration) with a catalytic hydrogenolysis process that uses hydrogen gas and metal catalysts to convert polyolefins into liquid fuels, substituting a high-emission thermal process with a lower-emission catalytic chemical transformation

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Productivity

If pyrolysis is used for plastic waste treatment, then fuel production is achieved, but conversion efficiency to valuable products remains low

Engineering Contradiction:
Improveconversion rate of plastic to fuelVSAvoidcarbon number distribution control in fuel products
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent employs catalyst composition optimization (specific metal ratios, support material selection) and reaction condition parameter tuning (temperature, pressure, hydrogen flow rate) to transform the hydrogenolysis process, achieving high-selectivity conversion of polyolefins to valuable liquid fuels and chemicals with controlled carbon number distributions

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention uses composite catalyst systems combining metal nanoparticles (Ru, Rh, Pt, Pd, Ir) with specific support materials (alumina, silica, titania, zirconia, carbon) to achieve synergistic effects that enhance both conversion efficiency and product selectivity, overcoming the limitations of single-component catalysts

Inventive Principle:
Principle #40Composite materials

4Productivity

If mechanical recycling is used for plastic waste, then some material recovery is achieved, but the process is ineffective for polyolefins and recycling rates remain low

Engineering Contradiction:
Improverecycling rate of plastic wasteVSAvoidprocess complexity and economic viability
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent transforms the approach to polyolefin recycling by changing the chemical parameters through catalytic hydrogenolysis, converting the chemically inert polyolefin chains into valuable liquid fuels and chemicals, thereby improving both recycling rate and economic viability simultaneously

Inventive Principle:
Principle #35Parameter changes

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This method achieves high conversion rates of polyethylene to fuels with specific carbon number distributions, offering a more efficient and economically viable solution for plastic waste management compared to existing technologies.

Implementation Method 1

a catalytic hydrogenolysis conversion of polyethylene (PE) to gasoline- and diesel-range fuels

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

contacting a mixture of the activated catalyst, hydrogen gas, and a polymer at a temperature of at least about 200° C., optionally in the presence of an inert gas, for a period of time that is sufficient for catalytic hydrogenolysis of the polymer

Methodology Applied
Scientific EffectHydrogenolysis: Chemical Bonding

Data Source

PatentUS20250122430A1Metal carbide-based catalyst systems for plastic recycling
Publication Date: 2025.04.17 IOWA STATE UNIV RES FOUND INC
  • US20250122430A1 patent drawing
  • US20250122430A1 patent drawing
  • US20250122430A1 patent drawing

AI summary

Catalysts and methods for catalytic hydrogenolysis of a polymer. The method comprises a) activating a catalyst with a hydrogen source to provide an activated catalyst, wherein the catalyst comprises: i) a MXene support of Formula I: Mn+1XnTx (I); wherein each M is independently an early transition metal; X is carbon or nitrogen; Tx is a surface functional group wherein x is 0-10; and n is 1, 2, 3, or 4; and ii) a supported metal, wherein loading of the supported metal on the MXene support is less than 5% w/w based on the weight of the catalyst; and b) contacting a mixture of the activated catalyst, hydrogen gas, and a polymer at a temperature of at least about 200° C. for a period of time that is sufficient for catalytic hydrogenolysis of the polymer; thereby converting the polymer to a fuel.