Four-Chamber Electrochemical Cell for Cleaner Lithium Extraction

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Solution Overview

Problem

Conventional electrochemical lithium extraction systems suffer from contamination of saltwater into the lithium recovery solution, high freshwater usage, and low lithium extraction efficiency due to passive lithium extraction mechanisms and mixing of saltwater and lithium recovery solution through electrode pores.

Innovation Solution

The system employs an electrochemical lithium recovery apparatus with a configuration of multiple electrochemical cells, each comprising four chambers bounded by lithium-intercalated or lithium-deintercalated electrodes and anion exchange membranes, which prevents saltwater and lithium recovery solution mixing and enhances lithium selectivity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional electrochemical lithium extraction systems use passive lithium extraction mechanisms with electrode pores, then lithium extraction can occur, but saltwater contaminates the lithium recovery solution and extraction efficiency is low

Engineering Contradiction:
Improvelithium extraction efficiencyVSAvoidpurity of lithium recovery solution
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The system divides the electrochemical cell into multiple chambers (first chamber, second chamber, third chamber, fourth chamber) separated by anion exchange membranes. This segmentation prevents direct mixing between saltwater and lithium recovery solution while maintaining separate extraction pathways, thereby improving both extraction efficiency and solution purity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Anion exchange membranes are introduced as intermediary elements between chambers containing saltwater and chambers containing lithium recovery solution. These membranes selectively transport ions while preventing direct contact and mixing between the two solutions, resolving the contamination issue while enabling continuous lithium extraction.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Device complexity

If conventional systems allow saltwater and lithium recovery solution to mix through electrode pores, then extraction process is simpler, but contamination increases and extraction efficiency decreases

Engineering Contradiction:
Improveconfiguration complexityVSAvoidlithium extraction efficiency
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The system segments the extraction process into distinct chambers separated by anion exchange membranes, creating multiple pathways for ion transport while preventing solution mixing. This segmentation improves extraction efficiency by maintaining concentration gradients and preventing contamination, with the added complexity being offset by the removal of contamination handling requirements.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system transitions from a single-chamber or two-chamber design to a four-chamber configuration, adding spatial dimensions to the extraction process. This multi-dimensional arrangement allows simultaneous extraction in multiple zones while maintaining separation between saltwater and recovery solution, improving overall productivity.

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

3Device complexity

If conventional systems use simple chamber configurations, then device complexity is low, but saltwater contaminates recovery solution through passive extraction mechanisms

Engineering Contradiction:
Improvechamber configurationVSAvoidprevention of solution mixing
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

Anion exchange membranes serve as intermediary barriers between chambers, selectively allowing ion transport while preventing bulk solution mixing. This intermediary structure provides reliable separation between saltwater and lithium recovery solution, ensuring high purity of the recovered lithium solution while maintaining a manageable device configuration.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The anion exchange membranes function as thin film barriers that provide effective separation between chambers. These membranes are permeable to ions but impermeable to bulk solution flow, preventing contamination while allowing lithium extraction to proceed efficiently through ionic transport.

Inventive Principle:
Principle #30Flexible shells and thin films

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 configuration significantly reduces contamination, minimizes freshwater usage, and improves lithium extraction efficiency by maintaining the separation of saltwater and lithium recovery solution, thereby enhancing the overall effectiveness of lithium extraction.

Implementation Method 1

a first chamber and an adjacent second chamber, wherein the first and second chambers are bounded by and share either an intermediate lithium-intercalated electrode or an intermediate lithium-deintercalated electrode

Methodology Applied
Scientific EffectIntercalation:

Implementation Method 2

a third chamber adjacent the first chamber, wherein the first and third chambers are bounded by and share an anion exchange membrane

Methodology Applied
Scientific EffectIon Exchange: Ion Exchange

Data Source

PatentUS20250188634A1System and process for extracting lithium from a saltwater
Publication Date: 2025.06.12 SALTWORKS TECHNOLOGIES INC
  • US20250188634A1 patent drawing
  • US20250188634A1 patent drawing
  • US20250188634A1 patent drawing

AI summary

Methods, systems, and techniques for extracting lithium from a saltwater using an electrochemical apparatus that performs the lithium extraction. The electrochemical apparatus includes a four-chamber electrochemical cell with adjacent two saltwater chambers or two adjacent lithium recovery solution chambers. Each chamber is bounded by an anion exchange membrane and either a lithium-deintercalated electrode or a lithium-intercalated electrode. The lithium deintercalated electrode and the lithium intercalated electrode may include a saltwater-impermeable and electrically conductive substrate, and respectively a porous lithium-deintercalated media and a porous lithium-intercalated media in contact with one or more surfaces of the saltwater-impermeable and conductive substrate. The lithium-deintercalated electrode absorbs lithium from the saltwater and the lithium-intercalated electrode releases lithium into the lithium recovery solution when an electrical potential is applied to the lithium-deintercalated electrode and the lithium-intercalated electrode.