Recycled Textile Pulp Ozone Bleaching With Two-Step pH Control

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Solution Overview

Problem

Existing methods for ozone bleaching pulp from recycled textile material face challenges in achieving sufficient brightness and maintaining pulp viscosity due to the oxidative properties of ozone, which degrades cellulose fibers.

Innovation Solution

A method involving two ozone bleaching steps with a charge of at least 12 kg/odt, combined with pretreatment using acids and additives like chelating agents and radical scavengers, followed by additional bleaching steps such as peroxide and chlorine dioxide, to enhance brightness and maintain pulp viscosity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Illumination intensity

If ozone bleaching is applied to pulp from recycled textile material, then brightness is improved, but cellulose degradation occurs and viscosity is reduced

Engineering Contradiction:
ImprovebrightnessVSAvoidcellulose fiber strength
Core Design Contradiction:
Illumination intensityVSStrength

Solution Approach 1:

The ozone bleaching process is divided into two distinct steps with different pH conditions. The first step at high pH (10-12) performs initial brightness enhancement with reduced cellulose attack. The second step at low pH (2-3) completes the bleaching while the protective additives prevent excessive cellulose degradation. This segmentation allows each step to optimize for its specific function.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Protective additives (radical scavengers and chelating agents) are introduced before ozone bleaching begins. These additives pre-establish protection against oxidative damage by scavenging free radicals and chelating metal ions that would catalyze cellulose degradation, thereby preventing viscosity loss before it occurs.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 3:

The process utilizes significant pH parameter changes between the two bleaching steps. The transition from high pH (10-12) in the first step to low pH (2-3) in the second step creates different chemical environments that optimize both brightness achievement and cellulose protection. This parameter change is central to resolving the contradiction between bleaching effectiveness and fiber preservation.

Inventive Principle:
Principle #35Parameter changes

2Illumination intensity

If higher ozone charges are used to improve brightness, then brightness is enhanced, but cellulose degradation increases and viscosity decreases

Engineering Contradiction:
ImprovebrightnessVSAvoidcellulose content
Core Design Contradiction:
Illumination intensityVSQuantity of substance

Solution Approach 1:

The total ozone charge is segmented into two steps with different effectiveness profiles. The first step at high pH uses a portion of the total ozone charge for initial brightness improvement with minimal cellulose attack. The second step at low pH uses the remaining ozone charge to achieve final brightness while protective additives prevent excessive cellulose degradation. This segmentation allows higher total ozone charge without proportional increase in cellulose loss.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Protective additives are added before ozone bleaching to pre-establish a protective shield against oxidative damage. Radical scavengers consume harmful free radicals before they can attack cellulose, and chelating agents bind metal ions that would catalyze degradation. This preliminary protection enables the use of higher ozone charges without proportional increase in cellulose degradation.

Inventive Principle:
Principle #10Preliminary action

3Device complexity

If conventional ozone bleaching methods are used, then the process is simple, but sufficient brightness cannot be achieved

Engineering Contradiction:
Improveprocess complexityVSAvoidbrightness
Core Design Contradiction:
Device complexityVSIllumination intensity

Solution Approach 1:

The bleaching process is segmented into two distinct steps with different pH conditions and additive formulations. This segmentation enables the process to achieve superior brightness (up to 90% ISO brightness) compared to conventional single-step methods, while the added complexity is managed through systematic protocol development.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The method employs composite chemical systems combining ozone with specific additive packages in each step. The first step uses ozone with high-pH buffers and initial protective additives. The second step uses ozone with low-pH conditions and enhanced protective additives. This composite approach synergistically combines multiple chemical functions to achieve both high brightness and cellulose preservation.

Inventive Principle:
Principle #40Composite materials

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

The method achieves a brightness of about 80% in two ozone bleaching steps and up to 90% with supplementary bleaching, while minimizing cellulose degradation and maintaining pulp viscosity.

Implementation Method 1

ozone reacts with and de-composes lignin originating from the wood material

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 2

ozone bleaching of cellulose pulp from wood material is well known in the art, where ozone reacts with and de-composes lignin

Methodology Applied
Scientific EffectOzone: Ozone

Implementation Method 3

Chelating agents provide the effect that selectivity in the ozone bleaching step is improved by reducing the content of metal ions in the pulp

Methodology Applied
Scientific EffectChelation:

Implementation Method 4

Radical scavengers have a similar effect by scavenging the metal ions

Methodology Applied
Scientific EffectFree radical scavenging:

Data Source

PatentEP4217534B1Method for bleaching pulp from recycled textile material
Publication Date: 2026.02.25 VALMET AB
  • EP4217534B1 patent drawingFigure 1
  • EP4217534B1 patent drawingFigure 2

AI summary

The invention relates to a method for bleaching pulp formed from recycled textile material comprising cellulose, said method comprising ozone bleaching (3; 13a, 13b) of said pulp by means of adding ozone at a charge of at least 12 kg/odt, wherein said ozone bleaching (13a, 13b) is performed as two subsequent steps, each comprising adding ozone at a charge such that the overall charge is at least 12 kg/odt.