Automotive Plastic Depolymerization for Low-Contaminant Pyrolysis Oil

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Solution Overview

Problem

The recycling of mixed automotive plastic waste is challenging due to contamination from heteroatoms and halogens, which prevents the pyrolytic oil from being used as fuel or feedstock, and existing methods struggle with mechanical reprocessing and chemical recycling inefficiencies.

Innovation Solution

A process involving sorting, shredding, and depolymerization of automotive plastic waste to obtain a high-quality feedstock of polyethylene and polypropylene, followed by depolymerization at controlled temperatures with a catalyst, yielding a clean liquid and gaseous stream.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If pyrolysis is used for chemical recycling of mixed automotive plastic waste, then energy recovery and fuel production are enabled, but the pyrolysis oil becomes contaminated with heteroatoms and halogens, preventing its use as fuel or feedstock

Engineering Contradiction:
Improveenergy recoveryVSAvoidcontamination with heteroatoms and halogens
Core Design Contradiction:
Use of energy by moving objectVSObject-affected harmful factors

Solution Approach 1:

The process segments the plastic waste stream by sorting it into different polymer categories (polyolefins, polyesters, polyamides, etc.) before pyrolysis. This segmentation prevents contamination from mixed polymers and enables production of high-quality, low-contaminant pyrolysis oil suitable for fuel and feedstock applications.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The process performs preliminary sorting and separation of plastic waste into homogeneous streams before pyrolysis treatment. By pre-separating polymers and removing contaminants like halogens and heteroatoms in advance, the pyrolysis oil produced is of high quality and suitable for fuel applications without requiring extensive post-treatment.

Inventive Principle:
Principle #10Preliminary action

2Loss of substance

If mechanical reprocessing is used for recycling automotive plastics, then material recovery is achieved, but the process is inefficient due to contamination from metal composites and inorganic fillers

Engineering Contradiction:
Improvematerial recoveryVSAvoidrecycling efficiency
Core Design Contradiction:
Loss of substanceVSProductivity

Solution Approach 1:

The process replaces inefficient mechanical reprocessing with chemical recycling through pyrolysis. By converting plastic waste into pyrolysis oil and gas through thermal decomposition, the method efficiently handles contaminated plastics containing metal composites and inorganic fillers that are difficult to process mechanically.

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

Solution Approach 2:

The process changes the physical and chemical parameters of plastic waste through controlled pyrolysis at specific temperatures (300-500°C). This transformation converts solid plastic waste into liquid pyrolysis oil and gaseous products, enabling efficient recovery and utilization of materials that are difficult to recycle through conventional mechanical methods.

Inventive Principle:
Principle #35Parameter changes

3Use of energy by moving object

If incineration is used for quaternary recycling of contaminated plastic waste, then energy recovery is achieved, but the process does not enable fuel or feedstock production due to contamination

Engineering Contradiction:
Improveenergy recoveryVSAvoidfuel and feedstock applicability
Core Design Contradiction:
Use of energy by moving objectVSAdaptability or versatility

Solution Approach 1:

The process changes the chemical composition and quality parameters of pyrolysis products through controlled depolymerization conditions. By optimizing temperature, residence time, and catalyst selection, the process produces high-quality pyrolysis oil with low contaminant levels that can be used as fuel or feedstock for steam crackers, unlike conventional incineration which only recovers energy.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The process replaces simple incineration with controlled chemical recycling through pyrolysis and depolymerization. This substitution transforms the endpoint from mere energy recovery to production of valuable fuel and feedstock products, enabling multiple application pathways including steam cracker feedstock and fuel blending.

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

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

The process produces high-purity monomeric olefins and low-contaminant pyrolytic oil, suitable for steam crackers and fuel applications, while reducing energy consumption and CO2 output.

Implementation Method 1

depolymerizing the feedstock at 300-500° C. in the optional presence of a catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

depolymerizing the feedstock at 300-500° C. in the optional presence of a catalyst, thereby obtaining a depolymerization product

Methodology Applied
Scientific EffectThermal decomposition: Pyrolysis

Implementation Method 3

separating the depolymerization product into a liquid stream and a gaseous stream

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS20260049195A1Process for the depolymerization of mixed automotive plastics
Publication Date: 2026.02.19 BASELL POLIOLEFINE ITALIA SRL
  • US20260049195A1 patent drawing

AI summary

A process for the recycling of automotive plastic waste including the steps of:(i) sorting the automotive plastic waste (APW), thereby obtaining a plastic waste fraction containing at least 60% wt of a mixture of polyethylene (PE) and polypropylene (PP);(ii) shredding, pelletizing, or both the fraction, thereby obtaining a plastic feedstock having a bulk density higher than 100 g/l;(iii) depolymerizing the feedstock at 300-500° C., in the optional presence of a catalyst, thereby obtaining a depolymerization product and(iv) collecting the depolymerization product and separating the depolymerization product into a liquid stream and a gaseous stream.