Catalyzed Depolymerization of Complex Plastic Feedstocks

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Solution Overview

Problem

Conventional pyrolysis methods for recycling plastic waste produce a broad distribution of hydrocarbon molecular weights, leading to an undesirably high proportion of heavy waxy fractions that require additional processing, increasing costs and inefficiencies, and often necessitate extensive sorting of plastic waste.

Innovation Solution

A catalytic depolymerization process using a zeolite-based or chromia-based catalyst in a fluidized or fixed bed reactor, where a polyolefin waste feed is heated with a hydrocarbon co-feed, producing liquid and gaseous depolymerization products that can be separated into C2-C5, C6-C8, and C9+ hydrocarbon streams, allowing for the production of circular ethylene and polyethylene without the need for extensive sorting or refinery processes.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional pyrolysis methods are used to recycle plastic waste, then plastic waste can be converted into hydrocarbon products, but the products have a broad distribution of molecular weights with high proportion of heavy waxy fractions requiring additional processing

Engineering Contradiction:
Improveconversion of plastic waste to hydrocarbonsVSAvoidadditional processing requirements
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent changes the operational parameters by introducing a catalyst (zeolite, chromia, or metal oxide) into the pyrolysis process, operating at controlled temperatures (400-800°F) and residence times (0.1-5 seconds). This catalytic approach modifies the product distribution to reduce heavy waxy fractions while maintaining hydrocarbon yield, eliminating the need for extensive downstream processing.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The catalyst serves as an intermediary substance that facilitates the conversion of plastic waste to desired hydrocarbon products. The catalyst mediates the chemical reactions to produce a narrower molecular weight distribution with reduced heavy fractions, thereby simplifying the overall process by eliminating the need for complex separation and refining operations.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If conventional pyrolysis methods are used, then plastic waste can be recycled, but extensive sorting of plastic waste is required

Engineering Contradiction:
Improveplastic waste recyclingVSAvoidwaste sorting requirements
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The catalytic pyrolysis process is designed to handle multiple types of polyolefin waste (polyethylene, polypropylene, polyvinylidene fluoride) simultaneously in a single reactor system. The catalyst system provides universal applicability across different plastic waste types, eliminating the need for extensive pre-sorting operations while maintaining consistent product quality.

Inventive Principle:
Principle #6Universality (Multi-functionality)

3Productivity

If conventional pyrolysis is used, then plastic waste can be converted to pyrolysis oil, but the heavy waxy fraction forms solids at ambient temperatures increasing costs

Engineering Contradiction:
Improvepyrolysis oil productionVSAvoidsolid formation at ambient temperature
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent modifies the thermal and catalytic parameters to control the molecular weight distribution of the produced hydrocarbons. By optimizing temperature (400-800°F), residence time (0.1-5 seconds), and catalyst type/concentration, the process produces pyrolysis oil with reduced heavy waxy content that remains liquid at ambient temperatures, eliminating solid formation issues and associated handling costs.

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 process efficiently converts plastic waste into usable hydrocarbon streams, reducing the need for additional processing and sorting, and enhances the economic viability of plastic waste recycling by producing high-quality circular products.

Implementation Method 1

heating and contacting the process feed with a depolymerization catalyst under suitable depolymerization conditions

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

catalytic depolymerization process using a zeolite-based or chromia-based catalyst

Methodology Applied
Scientific EffectCatalytic cracking: Catalysis

Implementation Method 3

providing the process feed to a heating zone and heating the process feed

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 4

heating the process feed in the presence of a depolymerization catalyst

Methodology Applied
Scientific EffectThermal energy transfer: Conduction (thermal)

Implementation Method 5

the initial heating of the process feed or the subsequent heating under depolymerization conditions can be conducted in the presence of a chemically-modified solid oxide, which includes a solid oxide treated with an electron-withdrawing anion

Methodology Applied
Scientific EffectChemical modification: Chemical Bonding

Implementation Method 6

chemically-modified solid oxide... treated with an electron-withdrawing anion

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS20240140883A1Catalyzed depolymerization of a chemically complex feedstock
Publication Date: 2024.05.02 CHEVRON PHILLIPS CHEMICAL COMPANY LP
  • US20240140883A1 patent drawing

AI summary

Depolymerization processes and systems for converting polyolefin waste and other waste plastic to hydrocarbons, specifically liquid and gaseous depolymerization reaction products. A depolymerization or catalytic pyrolysis process can be conducted on a process feed which includes a polyolefin waste and a hydrocarbon co-feed under depolymerization conditions, including contacting the reactor feed with a depolymerization catalyst such as a zeolite-based catalyst, with the system described herein. The resulting reactor effluent subsequently can be used as feeds or co-feeds for making circular products such as circular ethylene and circular polyethylene.