Electrolyte Circulation Device for Iron Electrolysis
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Solution Overview
Problem
Current electrochemical iron production methods are energy-intensive and have high operational costs due to the use of external pumps for electrolyte recirculation, leading to difficulties in scaling up production at high rates.
Innovation Solution
An apparatus for electrochemical iron production that includes a casing with a gas-permeable anode plate and a cathode plate, an electrolyte chamber, and a degassing unit with an electrolyte recirculation part. This apparatus features an electrolyte circulation device with a pumping device and non-return devices to aspirate and recirculate the electrolyte efficiently, reducing the need for fresh electrolyte and minimizing energy consumption.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Loss of substance
If external pumps are used for electrolyte recirculation, then electrolyte can be recirculated within the cell, but energy consumption increases and heat losses occur
Solution Approach 1:
The electrolyte recirculation system uses the buoyancy force generated by gas bubbles rising through the electrolyte to drive circulation, eliminating the need for external pumps. The gas-liquid separation chamber allows electrolyte to be lifted and recirculated passively through gravity and buoyancy forces, making the system self-service and energy-efficient.
Solution Approach 2:
The mechanical pump system is replaced with a passive fluid dynamics-based recirculation system utilizing buoyancy and gravity. Gas bubbles rising through the electrolyte create upward flow, while the gas-liquid separation chamber directs electrolyte back to the cell, substituting mechanical energy input with natural physical forces.
2Loss of substance
If external pumps are used for electrolyte recirculation, then electrolyte can be recirculated within the cell, but operative cost increases
Solution Approach 1:
The system automatically recirculates electrolyte using buoyancy-driven flow and gravity, requiring no external power input or complex control systems. This self-service mechanism reduces operative costs by eliminating pump energy consumption and associated maintenance.
3Loss of substance
If external pumps are used for electrolyte recirculation, then electrolyte can be recirculated within the cell, but upscaling at high production rate becomes difficult
Solution Approach 1:
The recirculation system dynamically adapts to production rate requirements through the gas-liquid separation chamber design. As gas generation increases with higher production rates, the buoyancy-driven flow automatically increases, providing scalable recirculation capacity without requiring proportionally larger pumps or more complex systems.
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 apparatus achieves improved energy efficiency and reduced operational costs by effectively recirculating the electrolyte within the system, thereby minimizing energy consumption and heat losses, and enabling higher production rates with a lower environmental footprint.
Implementation Method 1
an electrolyte circulation device including a pumping device located at one extremity of the casing
Implementation Method 2
at least a first non-return device located in the electrolyte chamber and a second non-return device located in the gas recovery part
Implementation Method 3
a gas permeable anode plate
Implementation Method 4
production of iron metal through reduction of iron ore by an electrolysis reaction
Data Source
AI summary
An apparatus (1) for the production of iron metal through reduction of iron ore by an electrolysis reaction, the apparatus including an electrolyte circulation device (30) including a pumping device (22) located at one extremity of the casing (4) and at least a first (31A) check valve located in the electrolyte chamber (6) and a second (31B) check valve located in the gas recovery part (8), the electrolyte circulation device (30) being designed, when actuating by an actuator (28), to aspirate the electrolyte (5) from the electrolyte chamber (6) or to pull the electrolyte (5) back into the gas recovery part (8).

