Polylactic Acid Recycling via Supercritical CO2

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Solution Overview

Problem

Current recycling methods for polylactic acid (PLA) to lactide are multi-step processes that require organic solvents, water, and catalysts, leading to high costs, environmental pollution, and inefficient separation processes, which do not provide sufficient biodegradation and high yield.

Innovation Solution

A single-step recycling method using supercritical or dense gas carbon dioxide to convert polylactic acid to lactide without organic solvents or water, facilitating high-purity lactide production and eliminating the need for separation processes by leveraging the unique properties of CO2 for efficient mass transfer and reaction conditions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If multi-step recycling processes with organic solvents and catalysts are used, then PLA can be converted to lactide, but the process becomes complex, costly, and environmentally harmful

Engineering Contradiction:
Improvelactide production yieldVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent combines multiple steps (depolymerization and purification) into a single-step process by using supercritical CO2 as both reaction medium and purification agent. The supercritical fluid facilitates the depolymerization reaction and simultaneously acts as an extraction medium to separate lactide from the reaction mixture, eliminating the need for separate purification steps and catalyst removal processes.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent extracts and eliminates harmful components (organic solvents, catalysts, water) from the recycling process by replacing them with supercritical CO2. The CO2 is introduced into the system, performs the depolymerization and extraction functions, and then is removed by depressurization, leaving no harmful residues in the final lactide product.

Inventive Principle:
Principle #2Taking out (Extraction)

2Ease of manufacture

If organic solvents and water are used in PLA recycling, then the depolymerization reaction can proceed, but separation processes become necessary and costly

Engineering Contradiction:
Improvereaction feasibilityVSAvoidseparation process time
Core Design Contradiction:
Ease of manufactureVSLoss of time

Solution Approach 1:

The supercritical CO2 serves multiple functions simultaneously: it acts as the reaction medium for depolymerization, as an extraction solvent for separating lactide from unreacted PLA and other byproducts, and as a purification agent. This self-service capability eliminates the need for separate water washing and organic solvent removal steps required in conventional methods.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The patent utilizes the phase transition of CO2 from supercritical state to gaseous state by simple depressurization. This phase change allows for easy separation of CO2 from the reaction mixture and product, eliminating the need for energy-intensive distillation or filtration processes required when using organic solvents or water.

Inventive Principle:
Principle #36Phase transitions

3Productivity

If catalysts are used for PLA depolymerization, then the reaction efficiency improves, but catalyst separation extends the recycling period

Engineering Contradiction:
Improvedepolymerization rateVSAvoidrecycling time
Core Design Contradiction:
ProductivityVSDuration of action of moving object

Solution Approach 1:

The patent removes catalysts from the system by replacing them with supercritical CO2 as the reaction medium. The CO2 facilitates the depolymerization reaction through its unique solvating properties and high diffusivity, and then is easily removed by depressurization, leaving no catalyst residues that would require separation and extending the process time.

Inventive Principle:
Principle #2Taking out (Extraction)

4Ease of manufacture

If conventional recycling methods are used, then PLA can be processed, but volatile organic components cause environmental pollution

Engineering Contradiction:
Improveprocessing capabilityVSAvoidenvironmental pollution
Core Design Contradiction:
Ease of manufactureVSObject-generated harmful factors

Solution Approach 1:

The patent converts the typically harmful role of solvents and catalysts into a beneficial process by using supercritical CO2, which is non-toxic, non-flammable, and environmentally benign. The CO2 can be easily separated from the product and reused, transforming what would be waste streams into a sustainable process cycle that eliminates volatile organic compound emissions.

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

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-yield, eco-friendly lactide production with reduced costs and environmental impact, eliminating the need for organic solvents and water, and simplifying the separation process, resulting in a more efficient and sustainable recycling process.

Implementation Method 1

conversion of polylactic acid to lactide in supercritical or dense gas carbon dioxide medium in a single step

Methodology Applied
Scientific EffectSupercritical fluid: Supercritical Fluid

Implementation Method 2

leveraging the unique properties of CO2 for efficient mass transfer and reaction conditions

Methodology Applied
Scientific EffectDiffusion: Diffusion

Data Source

PatentUS12195440B2High yield, eco-friendly recycling method of polylactic acid using supercritical or dense gas carbon dioxide
Publication Date: 2025.01.14 ORTA DOGU TEKNIK UNIVERSITESI
  • US12195440B2 patent drawing
  • US12195440B2 patent drawing

AI summary

A recycling method of polylactic acid in a single step by using supercritical or dense gas carbon dioxide is provided. The recycling method includes the steps of adjusting a temperature of a reactor to at least 120° C., and adjusting a pressure to values above or below a critical pressure of carbon dioxide, wherein the critical pressure is 73.8 bar.