Micro Hydrofloc PFAS Removal via Electroactive Gel and Oxidation

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Solution Overview

Problem

Conventional water treatment processes are ineffective and costly for removing per-and polyfluoroalkyl substances (PFAS) due to their chemical stability and resistance to degradation, leading to environmental contamination and health risks, with existing methods failing to achieve complete mineralization and incurring high energy consumption and treatment costs.

Innovation Solution

A four-stage process involving gelling aids to render PFAS molecules electroactive, followed by electrochemical oxidation to reduce carbon chain length, electrochemical coagulation to form micro-hydroflocs, and aeration to separate flocs, utilizing hydrophobic associative polymers and advanced oxidation processes to enhance PFAS removal efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional water treatment processes are used to remove PFAS, then treatment can be implemented, but removal efficiency is insufficient and energy consumption is high

Engineering Contradiction:
ImprovePFAS removal efficiencyVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The treatment process is divided into four distinct stages: (1) gelling aid addition to render PFAS electroactive, (2) electrochemical oxidation to reduce carbon chain length, (3) electrochemical coagulation to form micro-hydroflocs, and (4) aeration to separate flocs. This segmentation allows each stage to target specific PFAS characteristics, improving overall removal efficiency while optimizing energy use at each step.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The process changes the electrochemical parameters of PFAS molecules by adding gelling aids that render them electroactive. This parameter change enables subsequent electrochemical oxidation and coagulation processes to effectively target and remove PFAS, achieving superior removal efficiency compared to conventional methods while controlling energy consumption through optimized electrochemical parameters.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If conventional treatment methods are used, then some PFAS removal can be achieved, but complete mineralization is not accomplished

Engineering Contradiction:
Improvecomplete mineralizationVSAvoidtreatment process complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The process performs preliminary action by adding gelling aids to render PFAS molecules electroactive before applying electrochemical oxidation. This preliminary modification prepares the PFAS for more effective degradation, enabling complete mineralization that would not be achieved with conventional direct oxidation methods, while the systematic approach manages complexity through staged processing.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The treatment employs composite mechanisms combining gelling aids, electrochemical oxidation, electrochemical coagulation, and aeration in a integrated system. This composite approach achieves complete mineralization by combining multiple complementary processes, with each component contributing specific functions that collectively accomplish thorough PFAS degradation.

Inventive Principle:
Principle #40Composite materials

3Productivity

If existing treatment processes are applied to PFAS-contaminated water, then treatment can be implemented, but treatment costs are high

Engineering Contradiction:
ImprovePFAS removal efficiencyVSAvoidtreatment cost
Core Design Contradiction:
ProductivityVSQuantity of substance

Solution Approach 1:

The electrochemical process utilizes electrical energy to drive the transformation and removal of PFAS, with the system's own energy input enabling the chemical reactions that achieve complete mineralization. This self-service approach eliminates the need for expensive external chemical additives or complex multi-step processes, reducing overall treatment costs while maintaining high removal efficiency.

Inventive Principle:
Principle #25Self-service

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 process effectively reduces PFAS to below EPA thresholds in drinking water, achieving rapid and efficient removal of both long and short chain PFAS molecules with reduced energy consumption and cost, suitable for large-scale treatment.

Implementation Method 1

gelling aids to render the PFAS molecules electroactive

Methodology Applied
Scientific EffectElectroactive complex formation:

Implementation Method 2

oxidation process to reduce the carbon chain length of the PFAS molecules

Methodology Applied
Scientific EffectElectrochemical oxidation: Oxidation

Implementation Method 3

coagulation process to form micro-hydroflocs

Methodology Applied
Scientific EffectElectrochemical coagulation: Coagulation

Implementation Method 4

The PFAS molecules are adsorbed into the hydroflocs, which are aerated to separate the flocs from the treated water

Methodology Applied
Scientific EffectAeration: Aeration

Implementation Method 5

aeration to separate flocs

Methodology Applied
Scientific EffectFlotation: Froth Floatation

Implementation Method 6

utilizing hydrophobic associative polymers and advanced oxidation processes to enhance PFAS removal efficiency

Methodology Applied
Scientific EffectHydrophobic interaction: Hydrophobe

Data Source

PatentUS20260008706A1Utilization of Micro Hydroflocs for the Effective and Complete Removal of Long and Short Chain PFAS Molecules from Contaminated Water
Publication Date: 2026.01.08 STREAMGO WATER USA LLC
  • US20260008706A1 patent drawing
  • US20260008706A1 patent drawing
  • US20260008706A1 patent drawing

AI summary

Various embodiments provide methods for removing concentrations of PFAS from a contaminated stream of water or leachate. In a primary pretreatment stage, the incoming contaminated water is mixed with a hydrophobically associative gelling aid to generate an electroactive microgel with PFAS. In a secondary electrochemical oxidation stage, the electro-active microgel is reacted to reduce the PFAS carbon chain length. In a tertiary electrochemical coagulation stage, microhydrogels are generated which adsorb the degraded PFAS molecules and form microflocs. Lastly nanoparticles are added to the micro hydroflocs to aggregate the micro hydroflocs into macroflocs for easy flotation and removal.