Electrocoagulation Reactor with Rotatable Cathode for Wastewater Treatment

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Solution Overview

Problem

Existing electrocoagulation-based wastewater treatment systems are not capable of sufficient remediation of contaminated waters for large-scale commercialization due to high costs and limited treatment volumes.

Innovation Solution

An electrocoagulation reactor design featuring a rotatable cathode with surface features defining water flow paths and two treatment zones with different voltages applied across gaps between sacrificial and non-sacrificial anodes, combined with a clarifier for solid separation, enhances contaminant removal and treatment efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional electrocoagulation systems are used, then treatment capability is provided, but treatment volume is limited and cost is high

Engineering Contradiction:
Improvetreatment volumeVSAvoidsystem complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The electrocoagulation system is divided into multiple treatment zones (first treatment zone with sacrificial anode, second treatment zone with non-sacrificial anode) arranged in series, allowing parallel processing of wastewater streams and increasing overall treatment volume while maintaining manageable complexity in each individual zone

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system transitions from a single treatment zone to multiple treatment zones arranged spatially in series, adding a dimensional aspect to the treatment process that increases throughput capacity without proportionally increasing the complexity of individual treatment units

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

2Reliability

If single treatment zone is used, then device simplicity is maintained, but remediation efficacy is insufficient

Engineering Contradiction:
Improveremediation efficacyVSAvoidnumber of treatment zones
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The treatment process is segmented into distinct zones with different anode configurations (sacrificial vs. non-sacrificial), where each zone performs a specific remediation function, thereby improving overall efficacy while keeping each zone's design relatively simple and modular

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different treatment zones are designed with different anode types tailored to specific local requirements: the first zone uses sacrificial anodes for certain contaminant removal, while the second zone uses non-sacrificial anodes for other contaminants, optimizing remediation efficacy for different pollutant types in different locations

Inventive Principle:
Principle #3Local quality

3Productivity

If uniform voltage is applied across all zones, then system operation is simplified, but treatment optimization is limited

Engineering Contradiction:
Improvetreatment efficiencyVSAvoidvoltage control system
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

Each treatment zone is equipped with independent voltage control, allowing the first zone and second zone to operate at different voltages optimized for their specific contaminant removal requirements, thereby improving overall treatment efficiency while maintaining relatively simple independent control systems for each zone

Inventive Principle:
Principle #3Local quality

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 treats contaminated water by applying distinct voltages across multiple treatment zones and utilizing a clarifier for solid separation, achieving significant contaminant removal and meeting commercial-scale treatment requirements at a lower cost.

Implementation Method 1

Electrocoagulation is an electrochemical method of treating water contaminated with various species in an electrocoagulation reactor having a cathode and a sacrificial anode. Supplying current to the electrodes causes the release of metal cations (usually iron or aluminum) from the sacrificial anode

Methodology Applied
Scientific EffectElectrocoagulation: Electrolysis

Implementation Method 2

Supplying current to the electrodes causes the release of metal cations (usually iron or aluminum) from the sacrificial anode, and the formation of hydrogen gas at the cathode

Methodology Applied
Scientific EffectElectrochemical reduction: Electrolysis

Implementation Method 3

Rotating the cathode helps to ensure even consumption of the sacrificial anode and inhibit fouling of the active surface of the cathode

Methodology Applied
Scientific EffectTurbulence: Turbulence

Implementation Method 4

The clarifier has a cylindrical side wall, an upper wall, a conical bottom wall, a first outlet port in the upper wall connected to a first outlet conduit and a second outlet port in the bottom wall connected to a second outlet conduit

Methodology Applied
Scientific EffectSedimentation: Sedimentation

Data Source

PatentEP2414292B1Wastewater treatment apparatus and method
Publication Date: 2017.09.06 BOYDEL WASTEWATER TECH
  • EP2414292B1 patent drawingFigure 1
  • EP2414292B1 patent drawingFigure 2A
  • EP2414292B1 patent drawingFigure 2B

AI summary

An apparatus (20) for treating contaminated water has an electrocoagulation reactor (26) and a clarifier (30) to receive the effluent of the reactor. The reactor has a reaction vessel (48) having an inlet (58) and an outlet (62), a sacrificial anode (64), a rotatable cathode (68) and a non-sacrificial anode (66). A first gap (70) between the sacrificial anode and the cathode comprises a first water treatment zone. A second gap (74) between the cathode and the non-sacrificial anode comprises the second water treatment zone. The water flow path is from the inlet to the first treatment zone, then to the second treatment zone and then to the outlet. In the clarifier, the reactor effluent is separated into cleaned water and the contaminated sludge.