Catalytic Reduction and Biofilm Oxidation for TCA, TCE, and 1,4-Dioxane Removal

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Solution Overview

Problem

Current methods for removing trichloroethane (TCA), trichloroethene (TCE), and 1,4-dioxane from contaminated water face challenges such as inhibition among co-contaminants, long start-up periods, and secondary contamination, with existing technologies struggling to achieve efficient and continuous removal.

Innovation Solution

A system comprising a catalyst film and an ethane-oxidizing biofilm, utilizing precious metal nanoparticles and controlled H2 and O2 delivery through nonporous membranes, enables simultaneous reduction of TCA and TCE and oxidation of 1,4-D, minimizing inhibition and secondary contamination.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If biological processes are used for TCA/TCE removal, then cost is reduced, but the process requires long hydraulic retention time (at least 24 hours) and strict anaerobic conditions

Engineering Contradiction:
ImprovecostVSAvoidhydraulic retention time
Core Design Contradiction:
Ease of manufactureVSDuration of action of moving object

Solution Approach 1:

The system divides the contaminant removal process into two sequential stages: a catalytic reduction stage using Pd nanoparticles to convert TCA/TCE to less toxic compounds, followed by a biological oxidation stage to degrade these compounds. This segmentation allows each stage to operate under optimized conditions, with the catalytic stage achieving rapid reduction without requiring long retention times, while the biological stage efficiently degrades the transformed compounds.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent introduces Pd nanoparticles as an intermediary catalyst that mediates the transformation of TCA/TCE into intermediate products (ethane, ethene) that are more amenable to biological degradation. This intermediary catalytic step accelerates the overall process, reducing the required hydraulic retention time while maintaining cost-effectiveness through the use of nanoparticle catalysts.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If simultaneous bioreduction of TCE and TCA is applied, then treatment efficiency is improved, but mutual inhibition between co-contaminants occurs

Engineering Contradiction:
Improvetreatment efficiencyVSAvoidmutual inhibition
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The system segments the treatment process into two distinct functional stages: first, catalytic reduction of TCA and TCE to ethane and ethene using Pd nanoparticles; second, biological oxidation of these reduced products. This segmentation eliminates mutual inhibition between TCA and TCE during the same process stage, as each contaminant is transformed independently in the catalytic stage before being processed biologically in the second stage.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent changes the fundamental mechanism from simultaneous biological reduction to sequential catalytic then biological treatment. By altering the process parameters and mechanism, the system avoids the mutual inhibition problem that plagues simultaneous bioreduction, achieving reliable and efficient treatment of both TCA and TCE without interference between the contaminants.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If catalytic reductive dechlorination is used, then removal efficiency is improved, but high energy input and catalyst deactivation occur

Engineering Contradiction:
Improveremoval efficiencyVSAvoidenergy input
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent employs Pd nanoparticles as a catalyst that can be easily replenished or replaced. These nanoparticles provide high catalytic activity for the reduction of TCA/TCE but are small enough to be cost-effective and can be regenerated or replaced without significant expense, avoiding the high energy input and deactivation issues associated with traditional bulk metal catalysts.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The system changes the catalytic approach by using nanoparticle-scale Pd catalysts instead of traditional bulk metals. This parameter change at the nanoscale increases surface area and catalytic efficiency, reducing the total metal required and lowering energy input requirements while maintaining high removal efficiency for TCA and TCE.

Inventive Principle:
Principle #35Parameter changes

4Productivity

If electron donor and carbon source are added to promote 1,4-D co-oxidation, then biodegradation efficiency is improved, but secondary contamination occurs from unused substances

Engineering Contradiction:
Improvebiodegradation efficiencyVSAvoidsecondary contamination
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The system performs preliminary catalytic reduction of TCA and TCE before the biological oxidation stage. By transforming these contaminants into ethane and ethene in advance, the biological stage only needs to oxidize these simpler compounds along with 1,4-D, reducing the need for excessive electron donors and carbon sources that would otherwise be required to handle the more resistant chlorinated solvents.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The Pd nanoparticle catalyst acts as an intermediary that prepares the contaminants for biological degradation. By converting TCA/TCE into more biodegradable forms, the catalyst enables efficient biological oxidation of 1,4-D and the reduced products without requiring large amounts of external electron donors and carbon sources, thus preventing secondary contamination from unused additives.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 system effectively reduces TCA and TCE to ethane and oxidizes 1,4-D to CO2, achieving efficient removal of contaminants while avoiding toxic intermediates and reducing operational costs, with hydraulic retention times of no more than 24 hours.

Implementation Method 1

a catalyst film that reduces TCA and TCE

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

utilizing precious metal nanoparticles and controlled H2 delivery

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 3

oxidizes 1,4-D to CO2

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 4

ethane-oxidizing biofilm capable of 1,4-D degradation

Methodology Applied
Scientific EffectBiodegradation: Decomposition (biological)

Implementation Method 5

controlled H2 delivery through bubbleless gas-transfer membranes

Methodology Applied
Scientific EffectGas transfer: Diffusion

Data Source

PatentUS12168622B2Methods and systems for removing trichloroethane, trichloroethene, and 1,4-dioxane from contaminated water and wastewater
Publication Date: 2024.12.17 FLORIDA STATE UNIV RES FOUND INC
  • US12168622B2 patent drawing
  • US12168622B2 patent drawing
  • US12168622B2 patent drawing

AI summary

Disclosed herein are systems and methods for removing trichloroethane (TCA), trichloroethene (TCE), and 1,4-dioxane (1,4-D) from contaminated liquids. The system and methods rely on catalyst reduction of TCA and TCE, where the reduced products are then degraded by microorganisms The system comprises a first reactor comprising a catalyst film of precious metal nanoparticles deposited on a first nonporous membrane and a second reactor comprising a biofilm of microorganisms that are capable of degrading ethane and 1,4-D deposited on a second nonporous membrane. The first reactor further comprises a hydrogen gas source, wherein the hydrogen gas source delivers hydrogen to the gas-phase side of the first nonporous membrane, and the catalyst film is deposited on the liquid-phase side. The second reactor further comprises an oxygen gas source, wherein the oxygen gas source delivers oxygen to the gas-phase side of the second non-porous membrane, and the biofilm is deposited on the liquid-phase side.