Waste Plastic to Polycarbonate Conversion Process

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Solution Overview

Problem

The disposal of waste plastics poses significant environmental challenges, including atmospheric carbon emissions and inefficient use of fossil carbon, as current methods such as incineration and landfills are unsustainable and socially unacceptable.

Innovation Solution

A process is developed to convert waste plastics into polycarbonates through a series of steps including hydrotreatment of pyrolysis oil, thermal cracking with steam, separation of propylene and benzene, and subsequent chemical synthesis to produce bisphenol-A and ultimately polycarbonate, optimizing carbon efficiency and sustainability.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If waste plastics are processed by incineration or landfills, then disposal is achieved, but atmospheric carbon emissions increase and environmental harm worsens

Engineering Contradiction:
Improvewaste disposal methodVSAvoidatmospheric carbon emissions
Core Design Contradiction:
Ease of manufactureVSObject-generated harmful factors

Solution Approach 1:

The patent converts waste plastics, which are harmful when incinerated or landfilled, into valuable polycarbonate materials through chemical conversion. The waste plastic feedstock is processed through pyrolysis, hydrotreatment, steam cracking, and polymerization to produce polycarbonate, thereby transforming environmental harm into beneficial resource utilization and eliminating carbon emissions associated with conventional disposal methods

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

Solution Approach 2:

The patent employs multiple parameter changes throughout the process: temperature changes during pyrolysis and steam cracking, pressure changes during hydrotreatment and polymerization, and chemical composition changes through catalytic conversions. These parameter changes enable the transformation of waste plastic into polycarbonate while optimizing carbon efficiency and eliminating harmful emissions

Inventive Principle:
Principle #35Parameter changes

2Productivity

If conventional feed materials from fossil oil are used for polycarbonate production, then production is achieved, but fossil carbon utilization increases and sustainability decreases

Engineering Contradiction:
Improvepolycarbonate productionVSAvoidfossil carbon utilization
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

Instead of discarding waste plastics through incineration or landfilling, the patent recovers and converts them into polycarbonate materials. The waste plastic feedstock is recovered through pyrolysis to produce hydrocarbon streams, which are then processed through hydrotreatment, steam cracking, and polymerization to regenerate polycarbonate, thereby closing the material loop and eliminating the need for fossil carbon extraction

Inventive Principle:
Principle #34Discarding and recovering

Solution Approach 2:

The patent creates a multi-functional process that handles waste plastic conversion into multiple valuable products including polycarbonate, propylene, and benzene. The steam cracking unit serves multiple functions: it cracks hydrocarbons into monomers, produces propylene and benzene as co-products, and maintains sustainable operation through optimized temperature and residence time parameters

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

3Productivity

If steam cracking is performed under high temperature conditions, then cracking efficiency is improved, but coke formation increases and run duration decreases

Engineering Contradiction:
Improvecracking efficiencyVSAvoidrun duration
Core Design Contradiction:
ProductivityVSDuration of action of moving object

Solution Approach 1:

The patent optimizes steam cracking parameters by operating at controlled temperatures (800-850°C) and adjusting steam-to-feed ratios to maintain optimal cracking efficiency while minimizing coke formation. The process uses optimized residence times and catalytic conditions to maximize propylene and benzene production while extending run duration before tube cleaning is required

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements feedback control in the steam cracking process by monitoring tube fouling levels and adjusting operating parameters accordingly. The system tracks coke formation rates and modifies temperature, steam ratio, and flow velocities to maintain optimal cracking efficiency while extending run duration before maintenance is required

Inventive Principle:
Principle #23Feedback

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 enhances the circular utilization of plastics, increases the efficiency of polycarbonate production by maximizing propylene and benzene yields, and reduces environmental impact by reusing waste plastics instead of relying on fossil oil derivatives.

Implementation Method 1

providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 2

providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 3

performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D

Methodology Applied
Scientific EffectThermal cracking: Thermolysis

Data Source

PatentUS12215188B2Process for the preparation of polycarbonates from waste plastic feedstocks
Publication Date: 2025.02.04 SABIC GLOBAL TECHNOLOGIES BV

AI summary

Process for the production of polycarbonates comprising: providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; supplying a feed C comprising a fraction of the hydrocarbon stream A to a thermal cracker furnace comprising cracking coil(s); thermally cracking in the presence of steam to obtain a cracked hydrocarbon stream D; separating a product stream E comprising propylene and a product stream F comprising benzene from the cracked hydrocarbon stream D; performing a reaction and one or more separation step to obtain a product stream G comprising phenol; supplying the product stream G and acetone to a reactor and performing a reaction and one or more separation step to obtain a product stream H comprising bisphenol-A; and supplying the product stream H with phosgene or diphenyl carbonate to a reactor and performing a polymerisation reaction to obtain a polycarbonate.