Lithium Sulfate Processing with Sodium Sulfate Byproduct Conversion

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Solution Overview

Problem

The conventional processes for producing lithium carbonate (Li2CO3) and lithium hydroxide monohydrate (LiOH—H2O) from hard rock lithium minerals result in significant production of sodium sulfate (Na2SO4) byproducts, leading to high capital expenditures, energy consumption, and CO2 emissions, making the process economically unviable in many regions and environmentally impactful.

Innovation Solution

A method involving the preparation of an aqueous feed solution by reacting lithium-containing materials with sulfuric acid, followed by reacting this solution with a primary reagent to produce a mixed solution containing the lithium product and sodium sulfate, which is then separated and converted into higher value byproducts such as calcium sulfate, sodium nitrate, or sodium hydroxide through reactions with salt chemicals or alkali chemicals, or via electrolysis/electrodialysis.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If the conventional sulfuric acid process is used to produce lithium carbonate or lithium hydroxide from hard rock, then lithium materials can be produced reliably, but significant amounts of sodium sulfate byproducts are generated leading to high capital expenditures and energy consumption

Engineering Contradiction:
Improveproduction reliabilityVSAvoidprocess complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent extracts and removes the sodium sulfate byproduct handling step from the conventional process by using direct precipitation methods that eliminate the need for separate Na2SO4 crystallization circuits, thereby reducing capital expenditure and process complexity while maintaining production reliability

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent changes the chemical parameters of the reaction system by using alternative reagents (such as calcium hydroxide, ammonium hydroxide, or potassium hydroxide) instead of sodium carbonate, which fundamentally alters the byproduct formation and eliminates sodium sulfate generation, thus simplifying the overall process

Inventive Principle:
Principle #35Parameter changes

2Productivity

If the conventional process with Na2SO4 crystallization circuit is used, then lithium carbonate or lithium hydroxide can be produced, but capital expenditure increases due to special production plant requirements

Engineering Contradiction:
Improvelithium productionVSAvoidcapital expenditure
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent removes the Na2SO4 crystallization circuit from the process flow by using direct precipitation methods that produce marketable byproducts (such as calcium sulfate, ammonium sulfate, or potassium sulfate) without requiring separate handling facilities, thereby reducing capital expenditure while maintaining lithium production capacity

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

Instead of producing Na2SO4 as a byproduct and then finding uses for it, the patent inverts the approach by selecting reagents that directly produce valuable byproducts with existing market demand, eliminating the need for special production plants and reducing capital expenditure

Inventive Principle:
Principle #13The other way round (Inversion)

3Productivity

If the conventional process is used to produce lithium materials, then lithium carbonate or lithium hydroxide can be obtained, but energy consumption increases due to evaporation requirements

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

Solution Approach 1:

The patent changes the physical parameters of the process by using reagents that enable direct precipitation at lower temperatures without requiring extensive evaporation steps, thereby reducing energy consumption while maintaining lithium production efficiency

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements continuous precipitation processes that operate at optimal temperatures throughout the reaction, eliminating the need for intermittent heating and evaporation cycles, thereby reducing overall energy consumption while maintaining continuous lithium production

Inventive Principle:
Principle #20Continuity of useful action

4Productivity

If the conventional process with Na2SO4 byproduct is used, then lithium carbonate or lithium hydroxide can be produced, but CO2 emissions increase

Engineering Contradiction:
Improvelithium productionVSAvoidCO2 emissions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent changes the chemical composition parameters by replacing sodium carbonate with alternative reagents (calcium hydroxide, ammonium hydroxide, or potassium hydroxide) that do not generate CO2 during the reaction, thereby eliminating CO2 emissions while maintaining lithium production productivity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts the potentially harmful CO2 emission into a benefit by selecting reagents that produce valuable byproducts (such as calcium sulfate for construction materials or ammonium sulfate for fertilizers) without CO2 generation, thereby eliminating harmful emissions while creating additional value

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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 approach reduces the production of sodium sulfate, increases lithium recovery, decreases reagent and energy inputs, and lowers CO2 emissions, making the process more economically viable and environmentally friendly.

Implementation Method 1

preparing an aqueous feed solution comprising lithium sulfate by reacting the lithium-containing material with sulfuric acid

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 2

reacting the feed solution with a primary reagent to produce a mixed solution comprising the primary lithium product and sodium sulfate

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 3

separating the primary lithium product from the mixed solution

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Implementation Method 4

If battery-grade product is desired, the wet Li2CO3 cake obtained is re-dissolved and further purified by the CO2 method

Methodology Applied
Scientific EffectCrystallization: Crystallisation

Implementation Method 5

performing a conversion process on the separated sodium sulfate solution to produce the byproduct

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 6

using the separated sodium sulfate solution as an electrolyte in either an electrolysis process or an electrodialysis process

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Data Source

PatentUS20240425381A1Processing hard rock lithium minerals or other materials to produce lithium materials and byproducts converted from a sodium sulfate intermediate product
Publication Date: 2024.12.26 FRONTIER LITHIUM INC
  • US20240425381A1 patent drawing
  • US20240425381A1 patent drawing
  • US20240425381A1 patent drawing

AI summary

Methods are provided for processing a lithium-containing material (e.g., a mineral like spodumene) whereby a lithium sulfate solution derived from the material is reacted with a primary reagent (e.g., Na2CO3 or NaOH) to produce a mixed solution of primary lithium product (e.g., Li2CO3 or LiOH) and Na2SO4. In addition to primary lithium product, a separated Na2SO4 solution is produced and converted to a byproduct (e.g., CaSO4, NaNO3, NaOH, H2SO4) by reaction with a salt chemical (e.g., Ca(NO3)2) or alkali chemical (e.g., Ca(OH)2), or by electrolysis or electrodialysis. Byproducts are re-used to reduce reagent inputs. Residual lithium in an output solution is reacted with a secondary reagent (e.g., CO2 from flue gas, or H3PO4) to produce secondary lithium products (e.g., Li2CO3 or Li3PO4), which may be re-used to reduce reagent inputs and increase lithium recovery.