Vertical Cathode Aluminum Electrolysis Cell with Gravity Collection

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Solution Overview

Problem

Traditional aluminum smelting methods using carbon anodes are inefficient, leading to greenhouse gas emissions and limited electrolysis due to anode shape and size constraints, which result in the 'anode effect' and generation of regulated gases like CF4.

Innovation Solution

The use of oxygen-evolving anodes and aluminum-wettable vertical cathodes in an electrolytic cell design, where the cell bottom is configured with sloped surfaces and channels to efficiently collect and direct liquid aluminum, reducing greenhouse gas emissions and enhancing electrolysis efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If carbon anodes are used in traditional Hall-Héroult electrolytic cells, then aluminum production can be achieved, but greenhouse gas emissions (CO2 and CF4) are generated

Engineering Contradiction:
Improvealuminum productionVSAvoidgreenhouse gas emissions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent changes the chemical composition and electrochemical properties of the anode material from carbon-based to non-consumable materials that evolve oxygen instead of CO2. This fundamental parameter change in anode material chemistry eliminates the generation of greenhouse gases while maintaining the electrolytic reduction of alumina to produce aluminum metal.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs oxygen-evolving anodes that facilitate the oxidation of oxygen ions to produce oxygen gas instead of carbon oxidation. This accelerated oxidation process at the anode surface prevents carbon consumption and eliminates CO2 and CF4 emissions, while the oxygen produced can react with carbon in the bath to form CO2 without consuming the anode material.

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

2Device complexity

If traditional carbon anodes with limited shapes and sizes are used, then structural simplicity is maintained, but electrolysis efficiency is reduced due to frequent anode effects

Engineering Contradiction:
Improveanode structureVSAvoidelectrolysis efficiency
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The patent divides the anode system into multiple independent anodes arranged in a modular configuration. Each anode can be independently designed with optimized dimensions and spacing, allowing the electrolyte and dissolved alumina to access all anode surfaces effectively. This segmentation eliminates the anode effect by ensuring complete electrolysis of alumina at the anode-cathode interface.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent transitions from traditional horizontal or limited-orientation anodes to a three-dimensional arrangement where multiple anodes are positioned at different heights and orientations. This dimensional expansion maximizes the surface area available for electrolysis and ensures that alumina can reach all anode surfaces, preventing the accumulation that causes anode effects.

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

3Ease of manufacture

If conventional cell bottom designs are used, then manufacturing simplicity is maintained, but liquid aluminum collection is inefficient

Engineering Contradiction:
Improvecell bottom structureVSAvoidaluminum collection efficiency
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent incorporates sloped surfaces in the cell bottom design that guide liquid aluminum toward collection channels. The curved or angled geometry of the cell bottom creates a natural flow path for the dense liquid aluminum to move toward the drainage channels, improving collection efficiency without requiring complex mechanical pumping systems.

Inventive Principle:
Principle #14Spheroidality (Curvature)

Solution Approach 2:

The patent utilizes the density difference between liquid aluminum and the molten electrolyte to create natural hydraulic flow. The cell bottom geometry is designed to harness this density-driven flow, allowing liquid aluminum to automatically drain into collection channels through gravity-assisted hydraulic principles, eliminating the need for additional energy-consuming collection mechanisms.

Inventive Principle:
Principle #29Pneumatics and hydraulics

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 improves aluminum production efficiency by minimizing greenhouse gas emissions and reducing the frequency of the 'anode effect', allowing for continuous and periodic collection of liquid aluminum, thereby optimizing the aluminum smelting process.

Implementation Method 1

electrolysis of alumina using oxygen evolving anodes and aluminum wettable cathodes

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 2

the first upper surface and the second upper surface are configured to direct substantially all of the liquid aluminum produced in the electrolytic cell to the channel

Methodology Applied
Scientific EffectGravity: Gravitation

Implementation Method 3

the cathodes are wettable by molten aluminum

Methodology Applied
Scientific EffectWetting: Wetting

Data Source

PatentUS11180862B2Advanced aluminum electrolysis cell
Publication Date: 2021.11.23 ELYSIS LLP
  • US11180862B2 patent drawing
  • US11180862B2 patent drawing
  • US11180862B2 patent drawing

AI summary

In some embodiments, an electrolytic cell includes: an one anode module having a plurality of anodes; a one cathode module, opposing the anode module, and comprising a plurality of vertical cathodes, wherein each of the plurality of anodes and each of the plurality of vertical cathodes are vertically oriented and spaced one from another; a cell reservoir; and a cell bottom supporting the cathode module, wherein the cell bottom comprise an first upper surface, a second upper surface, and a channel, wherein the plurality of vertical cathodes extends upward from the upper surfaces, wherein at least one cathode block is located below the plurality of vertical cathodes, wherein the first upper surface and the second upper surface are configured to direct substantially all of the liquid aluminum produced in the electrolytic cell to the channel, and wherein the channel is configured to receive liquid aluminum from the upper surfaces.