PFAS Electrostatic Membrane Separation for Low-Waste Water Treatment

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Solution Overview

Problem

Conventional methods for removing PFAS from water are ineffective, particularly for branched and shorter chain compounds, and result in significant toxic waste due to incomplete resin regeneration and inefficient anion exchange systems.

Innovation Solution

The Aqueous Electrostatic Concentrator (AEC) system uses an aqueous electronic separator with three chambers and semipermeable membranes to electrostatically concentrate PFAS compounds, reducing voltage potential and capacitance at the membrane surface to extend membrane life and enhance PFAS removal efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional anion exchange resin is used to remove PFAS from water, then some PFAS can be removed, but the resin becomes saturated and requires regeneration that generates toxic waste

Engineering Contradiction:
ImprovePFAS removal effectivenessVSAvoidtoxic regenerant waste
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent extracts and removes PFAS from water using a membrane filtration system that separates contaminants from the water stream, eliminating the need for resin regeneration and associated toxic waste generation. The membrane system physically extracts PFAS without requiring chemical regeneration processes.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent changes the operational parameters by using a membrane filtration system instead of conventional resin exchange, operating at controlled flow rates and pressure differentials to achieve continuous PFAS removal without saturation issues that plague conventional resin systems.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If conventional activated carbon adsorption is used, then longer-chain PFAS can be removed, but branched and shorter chain compounds remain difficult to remove

Engineering Contradiction:
ImprovePFAS removal effectivenessVSAvoidcapability to remove different PFAS types
Core Design Contradiction:
ReliabilityVSAdaptability or versatility

Solution Approach 1:

The patent segments the PFAS removal process into multiple membrane stages with different pore sizes and filtration mechanisms, allowing selective removal of different PFAS types including branched and shorter chain compounds that conventional activated carbon cannot effectively remove.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent employs composite membrane materials with multiple layers having different properties, combining filtration, adsorption, and concentration functions to achieve broad-spectrum PFAS removal effectiveness across different molecular structures and chain lengths.

Inventive Principle:
Principle #40Composite materials

3Productivity

If high current is applied in electrostatic concentration, then PFAS removal efficiency increases, but membrane damage occurs

Engineering Contradiction:
ImprovePFAS removal rateVSAvoidmembrane durability
Core Design Contradiction:
ProductivityVSStrength

Solution Approach 1:

The patent dynamically adjusts the current density and operating parameters during the electrostatic concentration process, optimizing the balance between PFAS removal efficiency and membrane stress, allowing high productivity while preventing membrane damage through controlled, adaptive operation.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent incorporates protective measures and pre-conditioning of the membrane system before high-current operation, including gradual ramp-up of current density and monitoring systems that prevent excessive stress on the membrane, cushioning against potential damage while enabling high removal rates.

Inventive Principle:
Principle #11Beforehand cushioning (Prior cushioning)

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 AEC system achieves high PFAS removal rates of up to 95% in a single pass, significantly extending membrane life and reducing toxic waste generation, with treated water containing less than 10 parts per billion of PFAS.

Implementation Method 1

The Aqueous Electrostatic Concentrator (AEC) system uses an aqueous electronic separator with three chambers and semipermeable membranes to electrostatically concentrate PFAS compounds

Methodology Applied
Scientific EffectElectrostatic concentration: Electrostatics

Implementation Method 2

an aqueous electronic separator with three chambers and semipermeable membranes to electrostatically concentrate PFAS compounds

Methodology Applied
Scientific EffectSemipermeable membrane filtration: Semipermeable Membrane

Implementation Method 3

reducing voltage potential and capacitance at the membrane surface to extend membrane life and enhance PFAS removal efficiency

Methodology Applied
Scientific EffectVoltage potential reduction: Capacitance

Data Source

PatentUS12496553B2Apparatus and method for mediation of PFAS contamination in an environment
Publication Date: 2025.12.16 MOORE RANDALL
  • US12496553B2 patent drawing
  • US12496553B2 patent drawing
  • US12496553B2 patent drawing

AI summary

A method of moderating concentration of at least highly fluorinated alkyl materials (e.g., molecules) from a contaminated aqueous feed liquid containing an original composition of between 5 parts/trillion and 3000 parts/billion of the at least highly fluorinated materials per liter of water into an aqueous electronic separator having multiple chambers including a feed chamber having a liquid exit port from which a mediated aqueous contaminated feed liquid exits and a liquid input port into which the contaminated aqueous feed liquid enters the feed chamber; an anodic electrode chamber filled with an aqueous anodic liquid; and a cathodic electrode chamber filled with an aqueous cathodic liquid; wherein the feed chamber is between and adjacent to the anodic electrode chamber and the cathodic electrode chamber and the feed chamber is separated from each of the anodic electrode chamber and the cathodic electrode chamber by at least one semipermeable membrane.