UV Flow Degradation of Superabsorbent Polymer to Polyacrylic Acid

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Solution Overview

Problem

Current methods for recycling superabsorbent polymers (SAP) to poly(acrylic acid) (PAA) are inefficient, requiring long timescales and high energy inputs, and often result in decarboxylation, which is undesirable.

Innovation Solution

A method involving the use of a UV irradiation zone in a flow system with a residence time of less than 120 seconds and total energy of less than 50 MJ/kg SAP, where the SAP feed stream is converted to PAA while maintaining the carboxylic groups, allowing for the incorporation of PAA into virgin SAP or other applications.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional methods are used to degrade SAP to PAA, then complete degradation can be achieved, but the process requires long timescales and high energy inputs

Engineering Contradiction:
Improvedegradation rateVSAvoidenergy input
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The invention changes the energy parameter from conventional thermal or chemical degradation to UV irradiation at 254 nm, operating at room temperature and atmospheric pressure. This parameter change achieves rapid degradation (complete degradation in minutes) with low energy input (less than 50 MJ/kg SAP), resolving the contradiction between high productivity and low energy consumption.

Inventive Principle:
Principle #35Parameter changes

2Ease of manufacture

If conventional degradation methods are used, then SAP can be converted to PAA, but decarboxylation occurs which is undesirable

Engineering Contradiction:
Improveconversion efficiencyVSAvoiddecarboxylation
Core Design Contradiction:
Ease of manufactureVSObject-generated harmful factors

Solution Approach 1:

The invention replaces thermal or chemical degradation mechanisms with photochemical degradation using UV irradiation at 254 nm. This substitution activates photofunctional groups on the SAP polymer chains, enabling degradation at room temperature without the high temperatures that cause decarboxylation, thus achieving easy manufacture without harmful byproducts.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Productivity

If UV irradiation is used with hydrogen peroxide, then degradation can occur, but the process becomes more complex and requires additional chemicals

Engineering Contradiction:
Improvedegradation speedVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The invention extracts and eliminates the need for hydrogen peroxide and other chemical additives from the degradation process. By using direct UV irradiation at 254 nm, the process achieves rapid degradation through photofunctional group activation alone, simplifying the system while maintaining high productivity.

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

This approach enables efficient degradation of SAP to PAA with reduced energy consumption and prevents decarboxylation, facilitating the recycling and reuse of SAP while maintaining its functional properties.

Implementation Method 1

irradiating the feed stream with UV in the UV irradiation zone

Methodology Applied
Scientific EffectUV irradiation: Photodissociation

Data Source

PatentEP3783054B1Recycling of superabsorbent polymer via UV irradiation in flow system
Publication Date: 2022.06.08 PROCTER & GAMBLE CO
  • EP3783054B1 patent drawingFigure 1~2
  • EP3783054B1 patent drawingFigure 3~4
  • EP3783054B1 patent drawingFigure 5~6

AI summary

Poly(acrylic acid)-based superabsorbent polymer (SAP) in a feed stream is converted with UV irradiation into poly(acrylic acid) (PAA) in a flow system. The UV total energy used to convert SAP into PAA is less than about 50 MJ/kg SAP.