Caustic Digestion Process for Lithium Silicate Recovery

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Solution Overview

Problem

Current lithium recovery processes from lithium-bearing silicates, such as acid-roasting and lime-roasting, are energy-intensive and economically inefficient due to significant reagent consumption and high energy costs.

Innovation Solution

A caustic digestion process involving heating a mixture of lithium silicate with a concentrated sodium hydroxide solution, followed by dilution and removal of aluminates and silicates to produce a pregnant lithium solution, which is then evaporated to recover lithium carbonate or lithium hydroxide, reducing energy consumption and reagent usage.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If acid-roasting or lime-roasting processes are used to extract lithium from silicates, then lithium recovery is achieved, but energy consumption and reagent consumption increase significantly

Engineering Contradiction:
Improvelithium recoveryVSAvoidenergy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The patent changes the chemical parameters of the extraction process by using concentrated sodium hydroxide solution (40-80 wt%) instead of traditional acid or lime reagents. The process operates at moderate temperatures (200-350°C) under pressure, fundamentally altering the extraction chemistry from acid-based to alkali-based digestion, thereby reducing energy and reagent consumption while maintaining effective lithium recovery

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent replaces the thermal-mechanical roasting process (which requires high temperatures and significant energy input) with a chemical digestion process using concentrated caustic solution. This substitution eliminates the need for high-temperature roasting while achieving comparable or superior lithium extraction efficiency

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

2Productivity

If conventional roasting processes are used, then lithium extraction is effective, but operating costs become uneconomic

Engineering Contradiction:
Improvelithium extraction efficiencyVSAvoidoperating cost
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The patent modifies the extraction parameters by using concentrated sodium hydroxide (40-80 wt%) at moderate temperatures (200-350°C) under pressure, achieving high lithium extraction efficiency without the excessive energy consumption of conventional roasting, thereby reducing operating costs to economically viable levels

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The process employs cyclic operation with periodic heating, digestion, filtration, and evaporation stages. The barren solution is recycled back to the digestion step, creating a periodic but efficient operation cycle that minimizes continuous energy input while maintaining high extraction productivity

Inventive Principle:
Principle #19Periodic action

3Productivity

If high concentration caustic solution is used for digestion, then lithium extraction efficiency improves, but subsequent processing complexity increases

Engineering Contradiction:
Improvelithium extraction efficiencyVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent recycles the barren solution (containing unreacted caustic and dissolved impurities) back to the digestion step after filtration and evaporation. This recovery and reuse of the barren solution simplifies the overall process by eliminating the need for fresh caustic preparation and reducing waste treatment complexity, while maintaining high extraction efficiency through continuous operation

Inventive Principle:
Principle #34Discarding and recovering

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 process achieves high lithium extraction efficiency (>85%) with lower energy costs by using caustic digestion and subsequent evaporation steps, effectively recovering lithium values from silicates like spodumene and lepidolite.

Implementation Method 1

reacting a lithium bearing mineral with a basic material of sufficient strength to dissolve the mineral

Methodology Applied
Scientific EffectChemical reaction (caustic digestion): Chemical Bonding

Implementation Method 2

adding lime to the diluted heated mixture in an amount sufficient to produce calcium aluminate and calcium silicate solids

Methodology Applied
Scientific EffectChemical precipitation: Precipitation

Implementation Method 3

evaporating the pregnant lithium solution to increase a lithium concentration thereof

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 4

contacting the evaporated pregnant lithium solution with carbon dioxide to produce lithium carbonate solids

Methodology Applied
Scientific EffectChemical precipitation: Precipitation

Data Source

PatentEP3494240B1Caustic digestion process
Publication Date: 2021.09.29 LITHIUM AUSTRALIA LIMITED
  • EP3494240B1 patent drawingFigure 1

AI summary

The present disclosure provides a process for extracting and recovering lithium values from a lithium-bearing material, in particular from lithium-bearing silicates such as spodumene and lepidolite. The process for extracting lithium values from the lithium-bearing material includes heating a mixture of the lithium-bearing material and a caustic solution up to 350 °C. The mixture may be heated in a range of 200 °C to 300 °C in an autoclave. Alternatively, the mixture may be baked at a temperature in a range of 250 °C to 350 °C at atmospheric pressure. The heated mixture is then diluted and aluminates and silicates from the diluted heated mixture are removed to produce a pregnant lithium solution. The pregnant lithium solution may be evaporated to increase the lithium concentration thereof and lithium carbonate and/or lithium hydroxide are recovered from the evaporated pregnant lithium solution.