Integrated Electrochemical Cell for Continuous Lithium Brine Conversion

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Solution Overview

Problem

Existing lithium extraction and conversion methods from brine are energy-intensive, require multiple chemical reagents, and lack a fully integrated approach that avoids high temperatures and complex systems, leading to high costs and environmental impact.

Innovation Solution

An integrated electrochemical cell that combines lithium extraction and conversion in a single cell, using a catholyte chamber with a lithium intercalating electrode, a buffer chamber, and a compatible anion chamber to produce lithium products like LiOH or Li2CO3 at ambient temperatures without moving parts or electrolysis, employing reversible voltage to maintain efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If traditional lithium extraction from brine uses multiple chemical reagents and unit operations, then lithium conversion to products is achieved, but energy consumption increases and process complexity increases

Engineering Contradiction:
Improvelithium conversion processVSAvoidenergy consumption
Core Design Contradiction:
Ease of manufactureVSUse of energy by stationary object

Solution Approach 1:

The patent combines lithium extraction and conversion operations into a single electrochemical cell, eliminating the need for separate unit operations and chemical reagents. The electrochemical cell simultaneously performs lithium extraction from brine and conversion to lithium hydroxide or lithium carbonate products, reducing both process complexity and energy consumption.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The electrochemical cell is designed to perform multiple functions: it extracts lithium from brine, converts it to desired lithium products, and can adjust product composition based on operating conditions. This multi-functional approach replaces traditional sequential processes that required separate equipment and reagents for each step.

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

2Ease of manufacture

If traditional lithium extraction uses multiple unit operations and chemical reagents, then lithium product is produced, but the number of process steps increases

Engineering Contradiction:
Improvelithium extraction processVSAvoidprocess complexity
Core Design Contradiction:
Ease of manufactureVSDevice complexity

Solution Approach 1:

The patent merges lithium extraction and conversion unit operations into a single integrated electrochemical cell. This eliminates the need for multiple separate process steps, chemical reagent additions, and intermediate handling operations, thereby reducing overall process complexity while maintaining product production efficiency.

Inventive Principle:
Principle #5Merging (Combining)

3Productivity

If traditional lithium extraction from brine uses evaporation methods, then solid lithium product is obtained, but energy consumption increases

Engineering Contradiction:
Improvelithium product productionVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by stationary object

Solution Approach 1:

The patent replaces energy-intensive thermal evaporation methods with electrochemical processes. The electrochemical cell uses electrical energy to drive lithium extraction and conversion reactions, producing lithium products in aqueous or solid form without requiring high-temperature evaporation, thereby significantly reducing energy consumption while maintaining productivity.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

4Productivity

If traditional lithium extraction uses high temperatures, then lithium conversion is accelerated, but energy consumption and environmental impact increase

Engineering Contradiction:
Improvelithium conversion rateVSAvoidenvironmental impact
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent replaces thermal processing with electrochemical processing to achieve lithium conversion. The electrochemical cell uses controlled electrical potentials to drive extraction and conversion reactions at ambient or moderate temperatures, eliminating the need for high-temperature processing and associated environmental impacts while maintaining efficient productivity.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

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

Reduces energy requirements, lowers costs, and minimizes environmental footprint by producing high-purity lithium products efficiently and continuously, while avoiding high temperatures and complex systems.

Implementation Method 1

a catholyte chamber with a lithium intercalating electrode, a buffer chamber, and a compatible anion chamber to produce lithium products

Methodology Applied
Scientific EffectIntercalation:

Implementation Method 2

using a catholyte chamber with a lithium intercalating electrode

Methodology Applied
Scientific EffectElectrochemical reduction:

Implementation Method 3

a first anion exchange membrane

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Data Source

PatentUS20250352952A1Integrated electrochemical cell and method for lithium extraction from brine and conversion to lithium product
Publication Date: 2025.11.20 ELECTROFLOW TECHNOLOGIES INC
  • US20250352952A1 patent drawing
  • US20250352952A1 patent drawing
  • US20250352952A1 patent drawing

AI summary

An integrated electrochemical cell and method for processing lithium brine to obtain recovered lithium and produce a lithium product in a single continuous process. The integrated cell has a catholyte chamber with an intercalating electrode for lithium recovery from a lithium brine streaming through the catholyte chamber. A first anion exchange membrane separates the catholyte chamber from a buffer chamber. The buffer chamber streams a salt of a brine-predominant anion (e.g., a chloride salt for lithium brine containing predominantly chloride salt, or a carbonate salt for lithium brine containing predominantly carbonate salt) for removing the brine-predominant anion and thus preventing precipitation of salt species on first anion exchange membrane. An intermediate membrane separates the buffer chamber from a compatible anion chamber that streams a compatible salt that contains compatible or product anions desired for formation of the lithium product. A second anion exchange membrane separates compatible anion chamber from an anolyte chamber. The anolyte chamber has a lithium de-intercalating electrode for releasing lithium ions and it streams a lithium-bearing solution to obtain the lithium product through pairing of lithium ions with the product anions received from the compatible anion chamber via the second anion exchange membrane. A voltage source is provided for applying a potential difference between the electrodes to drive the process.