Superheated Water Dechlorination for Chlorinated Plastic Recycling

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Solution Overview

Problem

Existing methods for dechlorinating chlorinated polymers in plastic waste, such as PVC, face challenges including high energy consumption, formation of corrosive gases, formation of chloride salts, incorporation of oxygen, and inefficiencies in recycling due to impurities and non-homogeneous mixtures, which hinder effective recycling and chloride recovery.

Innovation Solution

A method involving superheating an aqueous plastic mixture of chlorine-containing polymers to at least 210°C under acidic conditions, maintaining a pH of at most 4, which removes chlorine as hydrogen chloride without forming chloride salts and minimizing oxygen incorporation, allowing for efficient dechlorination and subsequent chloride recovery.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-generated harmful factors

If gasification or pyrolysis is used to break down polymer chains, then chlorine can be removed from the plastic material, but corrosive hydrogen chloride gas is released and chlorinated polycyclic aromatic hydrocarbons may form

Engineering Contradiction:
Improvechlorine removalVSAvoidcorrosive HCl gas and dioxins
Core Design Contradiction:
Object-generated harmful factorsVSObject-affected harmful factors

Solution Approach 1:

Water serves as an intermediary medium in the hydrothermal treatment process. The superheated water facilitates chlorine removal from PVC while converting it into dissolved hydrogen chloride in the aqueous phase rather than gaseous HCl, thereby preventing corrosion and dioxin formation while achieving effective dechlorination

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The process utilizes extreme temperature and pressure parameters to superheat water above its normal boiling point, creating a unique hydrothermal state where water remains liquid but exhibits enhanced solvent properties and reactivity, enabling chlorine to transfer from polymer to aqueous phase as dissolved HCl rather than gas

Inventive Principle:
Principle #35Parameter changes

2Productivity

If alkaline base is used to accelerate dechlorination reaction, then chlorine removal is enhanced, but chloride salt is formed as a side product with minimal commercial value

Engineering Contradiction:
Improvedechlorination rateVSAvoidchloride salt formation
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

Instead of using alkaline conditions that convert HCl into worthless chloride salts, the invention inverts the approach by maintaining acidic conditions where HCl remains in its molecular form dissolved in water, transforming the unwanted side product into a recoverable commodity chemical with significant commercial value

Inventive Principle:
Principle #13The other way round (Inversion)

3Speed

If alkaline base is used for dechlorination, then reaction speed increases, but oxygen is incorporated into the dechlorinated product

Engineering Contradiction:
Improvereaction rateVSAvoidproduct quality
Core Design Contradiction:
SpeedVSReliability

Solution Approach 1:

The invention changes the pH parameter from alkaline to acidic conditions, which maintains fast reaction kinetics through acid-catalyzed dechlorination while preventing oxygen incorporation into the polymer structure, thereby preserving product quality and suitability for further processing

Inventive Principle:
Principle #35Parameter changes

4Stability of the object's composition

If mechanical recycling is used to maintain polymer chains intact, then material structure is preserved, but the waste stream must be clean and homogeneous which is difficult to achieve

Engineering Contradiction:
Improvepolymer chain integrityVSAvoidwaste stream purity
Core Design Contradiction:
Stability of the object's compositionVSEase of manufacture

Solution Approach 1:

The hydrothermal treatment selectively extracts chlorine from the PVC polymer structure while leaving the polymer chains intact. This extraction approach allows processing of mixed, impure waste streams by removing the harmful chlorine component without requiring pre-sorting or cleaning, bridging the gap between mechanical and feedstock recycling

Inventive Principle:
Principle #2Taking out (Extraction)

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

Achieves high chlorine removal rates (>80%) with low oxygen incorporation, producing dechlorinated plastic suitable for further processing and enabling efficient chloride recovery through ion exchange, reducing the need for post-treatment and energy-intensive processes.

Implementation Method 1

superheating the aqueous plastic mixture to a temperature of at least 210°C

Methodology Applied
Scientific EffectHydrothermal treatment: Superheating

Implementation Method 2

The chlorine is transferred from the plastic to an alkaline aqueous phase wherein the base is used to minimize corrosion and to accelerate the dechlorination reaction

Methodology Applied
Scientific EffectDechlorination reaction: Chemical Bonding

Implementation Method 3

during the superheating, the pH of the water in the aqueous plastic mixture is maintained at at most 4

Methodology Applied
Scientific EffectpH control:

Implementation Method 4

enabling efficient chloride recovery through ion exchange

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Data Source

PatentUS20250289913A1Dechlorination of plastic materials using superheating in water
Publication Date: 2025.09.18 NEDERLANDSE ORG VOOR TOEGEPAST NATUURWETENSCHAPPELIJK ONDERZOEK TNO
  • US20250289913A1 patent drawing

AI summary

The invention is in the field of recycling plastic material. In particular, the invention is directed to a method for dechlorination of a chlorine-containing polymer comprised in plastic material using superheating. The invention is further directed to a dechlorinated polymer obtainable by the method. The method is performed in water, with a pH of at most 4 during the method.