Improving rPET L* Color via Catalyst Timing and Glycol Removal

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Solution Overview

Problem

Recycled PET (rPET) made from rBHET tends to have lower reactivity and a darker, yellower color due to impurities, making it less competitive compared to virgin PET (vPET) in terms of brightness and color quality, as measured by the L* value in the CIELAB color space.

Innovation Solution

A method involving the use of an antimony-containing catalyst, added at a temperature between the melting point of BHET and 220°C, and exposing BHET in a molten state to glycol removal below 10% free glycol prior to catalyst addition, or employing non-antimony-containing catalysts like titanium, zinc, or manganese, to improve the L* color of polyethylene terephthalate polymer during the PET manufacturing process.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-affected harmful factors

If recycled PET (rPET) is made from rBHET, then the amount of petrochemicals required is reduced and carbon footprint is lowered, but the L* color value decreases and the material becomes darker and yellower

Engineering Contradiction:
Improvecarbon footprintVSAvoidL* color value
Core Design Contradiction:
Object-affected harmful factorsVSIllumination intensity

Solution Approach 1:

The patent applies parameter changes by optimizing the catalyst addition temperature to a specific range (below the melting point of BHET or 150-200°C) and controlling the degree of polymerisation conditions. These parameter adjustments modify the chemical reaction pathways to minimize the formation of colored impurities while maintaining the recycling benefit, thus improving L* color value without sacrificing the environmental advantage of using rBHET

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite catalyst systems combining antimony compounds with alternative catalysts (such as germanium, titanium, zinc, or manganese compounds) at controlled ratios. This composite approach leverages the synergistic effects of different catalysts to achieve both high L* color values and effective polymerization of rBHET, resolving the contradiction between recycling benefits and color quality

Inventive Principle:
Principle #40Composite materials

2Quantity of substance

If rBHET is used in the PET manufacturing process, then recycled content is increased, but the reactivity of the polymerisation process decreases

Engineering Contradiction:
Improverecycled contentVSAvoidpolymerisation reactivity
Core Design Contradiction:
Quantity of substanceVSProductivity

Solution Approach 1:

The patent applies preliminary action by conducting a pre-polymerisation step before the main polymerisation process. During this preliminary stage, rBHET is partially converted to oligomers under controlled conditions (temperature 150-250°C, reduced pressure) to activate the material and improve its reactivity for subsequent polymerisation, thereby enabling higher recycled content while maintaining productivity

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent uses composite catalyst systems that combine antimony compounds with alternative catalysts specifically optimized for rBHET polymerisation. This composite approach enhances the overall catalytic activity and reactivity of the system, allowing efficient processing of high recycled content materials while maintaining productive polymerisation rates

Inventive Principle:
Principle #40Composite materials

3Object-affected harmful factors

If rPET is produced from rBHET, then environmental benefits are achieved, but the brightness and color quality become inferior to virgin PET

Engineering Contradiction:
Improveenvironmental impactVSAvoidbrightness
Core Design Contradiction:
Object-affected harmful factorsVSIllumination intensity

Solution Approach 1:

The patent optimizes critical process parameters including catalyst addition temperature (below BHET melting point or 150-200°C), degree of polymerisation conditions, and moisture control. These parameter changes suppress the formation of colored by-products and impurities that reduce brightness, enabling rPET to achieve L* color values comparable to virgin PET while maintaining environmental benefits

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs an inert atmosphere (nitrogen or carbon dioxide) throughout the polymerisation process to prevent oxidation and other unwanted reactions that generate colored impurities. This inert environment protection maintains the brightness and color quality of rPET, making it comparable to virgin PET while preserving the environmental advantages of recycling

Inventive Principle:
Principle #39Inert atmosphere (Inert environment)

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 enhances the L* color value of rPET by 3 to 5 units, increasing its brightness and making it more comparable to vPET, thus improving the utility of recycled materials in PET production.

Implementation Method 1

A method involving the use of an antimony-containing catalyst, added at a temperature between the melting point of BHET and 220°C

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

exposing BHET in a molten state to glycol removal below 10% free glycol prior to catalyst addition

Methodology Applied
Scientific EffectEvaporation: Evaporation

Data Source

PatentUS20230203244A1A method for improving l* color in a pet polymer
Publication Date: 2023.06.29 KOCH TECHNOLOGY SOLUTIONS LLC
  • US20230203244A1 patent drawing
  • US20230203244A1 patent drawing
  • US20230203244A1 patent drawing

AI summary

A method for improving L* color of polyethylene terephthalate polymer, the method including bis-hydroxylethyl-eneterephthalate being polycondensed to produce said polyethylene terephthalate polymer in a polyethylene terephthalate manufacturing process, and wherein said process requires an antimony-containing catalyst, the method comprising the steps of: i) adding said antimony-containing catalyst at a temperature in a range of a melting point of said BHET to an upper temperature of 220° C.; and ii) exposing said BHET in a molten state to glycol removal before addition of said antimony-containing catalyst.