Supercritical Water Oxidation for PFAS Destruction

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Solution Overview

Problem

Current technologies for treating PFAS-contaminated water are expensive and inefficient, with many methods producing byproducts or only partially degrading PFAS compounds, and there is a need for a system that can achieve complete destruction of PFAS under field-scale conditions.

Innovation Solution

The development of a supercritical water oxidation (SCWO) method, known as the PFAS Annihilator™, which operates at high temperatures and pressures to break down PFAS into environmentally benign end products, with specific conditions optimized for the destruction of perfluorosulfonic acids (PFSAs) and other PFAS compounds.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional remediation techniques such as oxidation using peroxide or persulfate are applied, then PFAS removal is achieved, but the effectiveness is limited and byproducts are produced

Engineering Contradiction:
ImprovePFAS removal effectivenessVSAvoidbyproduct formation
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent applies parameter changes by transitioning from conventional oxidation conditions to supercritical water oxidation conditions (temperature above 374°C and pressure above 3206 psi). This fundamental parameter change enables complete destruction of PFAS compounds including PFSAs, converting them to benign products (CO2, HF, H2O) rather than producing harmful byproducts.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs strong oxidation under supercritical water conditions to achieve complete destruction of PFAS. The supercritical water environment enables accelerated oxidation reactions that completely mineralize recalcitrant compounds like PFSAs, eliminating the formation of intermediate byproducts that occur with conventional oxidation methods.

Inventive Principle:
Principle #38Strong oxidants (Accelerated oxidation)

2Use of energy by moving object

If reductive methods are used for PFAS destruction, then energy consumption is reduced, but degradation of perfluorinated sulfonates is slow and incomplete

Engineering Contradiction:
Improveenergy consumptionVSAvoiddegradation completeness
Core Design Contradiction:
Use of energy by moving objectVSReliability

Solution Approach 1:

The patent transitions from reductive conditions to supercritical water oxidation conditions, fundamentally changing the chemical environment. This parameter change enables complete destruction of perfluorinated sulfonates through oxidation, achieving both high reliability (complete degradation) and reasonable energy efficiency compared to conventional thermal methods.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent utilizes the phase transition of water to supercritical state to enable complete PFAS destruction. The supercritical phase provides unique properties (enhanced solubility, diffusivity, and reaction rates) that allow complete oxidation of recalcitrant PFSAs, overcoming the limitations of both reductive and conventional oxidative methods.

Inventive Principle:
Principle #36Phase transitions

3Reliability

If SCWO is applied to destroy PFSAs, then near-complete destruction is achieved, but high temperature and pressure conditions are required

Engineering Contradiction:
ImprovePFAS destruction completenessVSAvoidoperating temperature
Core Design Contradiction:
ReliabilityVSTemperature

Solution Approach 1:

The patent exploits the phase transition of water to supercritical state as the enabling mechanism for PFAS destruction. The supercritical phase provides enhanced reaction conditions that achieve near-complete destruction of PFSAs. The system is designed to efficiently achieve and maintain supercritical conditions through controlled heating and pressurization.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The patent applies parameter changes by operating in the supercritical region of water (T > 374°C, P > 3206 psi). This parameter regime enables complete oxidation of recalcitrant PFSAs. The system design optimizes these parameters to achieve complete destruction while managing the energy requirements of maintaining supercritical conditions.

Inventive Principle:
Principle #35Parameter changes

4Reliability

If conventional granular activated carbon adsorption is used, then PFAS removal is achieved, but shorter chain PFAS break through faster requiring frequent change out or regeneration

Engineering Contradiction:
ImprovePFAS removal effectivenessVSAvoidsorbent replacement frequency
Core Design Contradiction:
ReliabilityVSLoss of time

Solution Approach 1:

The patent fundamentally changes the treatment approach from adsorption to complete destruction through supercritical water oxidation. This parameter change eliminates the issue of sorbent saturation and breakthrough, as the process completely mineralizes all PFAS compounds regardless of chain length, converting them to CO2, HF, and H2O.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent extracts the PFAS compounds from the water matrix through supercritical water oxidation, completely destroying them rather than transferring them to a sorbent medium. This eliminates the need for sorbent replacement or regeneration, as the contaminants are converted to benign products that remain in the aqueous phase.

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

The PFAS Annihilator™ achieves near-complete destruction of PFAS, reducing concentrations to non-detectable levels in under 30 seconds, effectively treating PFAS-contaminated materials and liquids, including AFFF and landfill leachate, with minimal byproduct formation and efficient energy use.

Implementation Method 1

SCWO involves oxidation of aqueous organic compounds at temperatures and pressures above the critical point of water in the presence of oxygen

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 2

SCWO involves oxidation of aqueous organic compounds at temperatures and pressures above the critical point of water

Methodology Applied
Scientific EffectSupercritical fluid: Supercritical Fluid

Data Source

PatentUS20230373824A1Destruction of Perfluorosulfonic Acids (PFSAs) via Supercritical Water Oxidation
Publication Date: 2023.11.23 REVIVE ENVIRONMENTAL TECHNOLOGY LLC COLUMBUS
  • US20230373824A1 patent drawing
  • US20230373824A1 patent drawing
  • US20230373824A1 patent drawing

AI summary

Supercritical water oxidation (SCWO) is a destruction technology to quickly treat per- and polyfluoroalkyl substance (PFAS)-impacted groundwater, investigation derived waste, and other aqueous matrices such as landfill leachate and aqueous film forming foam. Laboratory-prepared and field-collected samples with inlet PFAS concentrations up to 50 parts per million were consistently destroyed to less than 70 parts per trillion for all PFAS, when running at the determined optimal operating conditions (≥600° C. and 3,500 pounds per square inch). We investigated the correlation between temperature and flowrate of the system, finding that reactor temperatures ≥450° C. destroys perfluorinated carbonic acids, but higher temperatures and specified conditions are necessary to destroy perfluorosulfonic acids. Using a higher density oxygen source also increases the throughput of a SCWO reactor, here up to 140 mL/min, without affecting PFAS destruction. Continuous 5-log reduction in the concentration of PFAS (99.999% destruction) is demonstrated for 3 hours at steady-state operation. The destruction efficiency is not impacted by the addition of co-contaminants such as petroleum and other organic hydrocarbons, and the SCWO process is successfully applied to waste streams without pretreatment. The treated effluent is largely comprised of complete combustion products including carbon dioxide, water, and the corresponding anion acids; hence, the treated liquid can be released back into the environment after neutralization.