Rotatable Electrode Reactor for Boundary Layer Diffusion

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Solution Overview

Problem

Static electrochemical reactors are inefficient in treating contaminated liquids due to stagnant flow in the laminar sub-layer near the electrodes, limiting the interaction of hydroxyl radicals with the liquid, which reduces the effectiveness of the oxidation process.

Innovation Solution

The introduction of rotatable electrodes within a reactor vessel, where the electrodes are mounted on support plates that can rotate independently, creating a gap for the liquid to flow through, thereby increasing the interaction with the laminar sub-layer and enhancing the mass-transfer efficiency by adjusting the boundary layer thickness.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If static electrodes are used in the reactor vessel, then the structure is simple and easy to manufacture, but the liquid flow becomes stagnant in the laminar sub-layer, reducing mass-transfer efficiency

Engineering Contradiction:
Improveease of manufactureVSAvoidmass-transfer efficiency
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent applies the dynamics principle by transforming the static electrodes into rotatable electrodes that can rotate about the longitudinal axis. This rotation creates continuous movement of the liquid through the gap between electrodes, preventing stagnant flow in the laminar sub-layer and significantly enhancing mass-transfer efficiency. The rotational motion dynamically renews the liquid-electrode contact, allowing hydroxyl radicals to continuously interact with contaminated liquid throughout the treatment process.

Inventive Principle:
Principle #15Dynamics

2Productivity

If the liquid velocity at the electrode interface is increased, then mass-transfer improves, but the residence time of liquid in the reactor decreases, reducing treatment effectiveness

Engineering Contradiction:
Improvemass-transfer efficiencyVSAvoidresidence time
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

The patent applies the dimensionality change principle by introducing rotational motion around the longitudinal axis, adding a third dimension of movement to the liquid flow. Instead of simply increasing linear flow velocity through the reactor, the rotation creates circumferential movement that continuously brings fresh liquid into contact with the electrode surfaces while maintaining adequate residence time. This multi-dimensional approach decouples mass-transfer enhancement from residence time reduction.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

3Productivity

If rotatable electrodes are introduced to improve liquid circulation, then mass-transfer efficiency increases, but the device complexity increases

Engineering Contradiction:
Improvemass-transfer efficiencyVSAvoiddevice complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent applies the universality principle by designing the rotatable electrode assembly to perform multiple functions simultaneously. The rotating electrodes not only enhance mass-transfer through improved liquid circulation but also provide uniform distribution of hydroxyl radicals, create turbulent flow patterns for better mixing, and maintain consistent treatment conditions throughout the reactor volume. This multi-functionality justifies the added complexity by delivering superior overall treatment performance.

Inventive Principle:
Principle #6Universality (Multi-functionality)

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 design significantly increases the use of hydroxyl radicals for oxidation, leading to a drastic improvement in mass-transfer and overall reactor efficiency, allowing for the effective treatment of high volumes of contaminated liquids.

Implementation Method 1

The reactor uses electric energy, which is applied to the electrodes, to generate an electrolytic process when a liquid is present

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 2

An electric current is then applied to the electrodes which starts the electrochemical reaction in the liquid

Methodology Applied
Scientific EffectElectrochemical reaction:

Implementation Method 3

a layer on top of the electrodes called the boundary layer

Methodology Applied
Scientific EffectBoundary layer: Boundary Layer

Implementation Method 4

the velocity in what is called the 'laminar (viscous) sub layer,' (the portion of the boundary layer which resides closest to the electrode interface) is extremely low

Methodology Applied
Scientific EffectLaminar flow: Laminar Flow

Data Source

PatentUS12103870B2Rotational electro-oxidation reactor with improved boundary-layer diffusion
Publication Date: 2024.10.01 E OX CORP INC
  • US12103870B2 patent drawing
  • US12103870B2 patent drawing
  • US12103870B2 patent drawing

AI summary

An electrochemical oxidation reactor includes rotatable electrodes inside a reactor vessel. The electrodes treat liquid within the reactor and are mounted to support plates, which in turn are mounted on each of two independently-driven shafts. The plates are attached to each other in a spaced relationship so that a gap is formed therebetween. The gap is sized to receive liquid to be treated so that liquid located within the gap will react with the electrodes. The shafts are rotatable at equal or different relative rotational speeds and directions. Additionally, each shaft may be independently linearly displaced in an oscillatory movement at equal or different frequencies. The relative shaft rotation, direction and axial vibration translate similar movements to the electrodes and such movement generates turbulence to the liquid located within the gap. The turbulence increases the interaction between liquid and the electrodes.