Lithium Sulfate Monohydrate Concentration from High-Sulfate Brines
Find Innovative SolutionsGenerate Solutions
Solution Overview
Problem
Existing processes are unable to economically process high sulfate brines to produce lithium sulfate monohydrate due to high impurity levels of chlorine and magnesium, making them financially unattractive for lithium production.
Innovation Solution
A three-stage process involving grinding, flotation, and leaching is employed to concentrate lithium sulfate monohydrate with low impurity contents, utilizing a selective concentration stage to enhance purity and recovery, followed by a leaching stage to achieve over 95% purity.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Quantity of substance
If high sulfate brines are processed using conventional methods, then lithium production can be achieved, but the impurity levels of chlorine and magnesium become too high, making the process financially unattractive
Solution Approach 1:
The flotation process is divided into multiple stages: rougher flotation to remove coarse impurities, cleaner flotation to further purify the concentrate, and scavenger flotation to recover additional lithium. This segmented approach progressively reduces chlorine and magnesium impurity levels while concentrating lithium sulfate monohydrate, making the brine economically viable for lithium production
Solution Approach 2:
The process selectively extracts lithium sulfate monohydrate from the complex brine mixture containing high levels of chlorine and magnesium impurities. Through controlled flotation conditions and selective reagents, lithium is separated and concentrated while leaving harmful impurities in the tailings, achieving over 95% purity in the final product
2Manufacturing precision
If selective concentration stages are added to enhance purity, then lithium sulfate monohydrate purity increases to over 95%, but the process complexity increases
Solution Approach 1:
Multiple flotation operations (rougher, cleaner, and scavenger stages) are combined into an integrated flow sheet that processes the brine systematically. The merging of these stages achieves high purity (over 95%) through progressive concentration while managing complexity through unified process control and coordinated reagent application across all stages
3Productivity
If conventional flotation methods are used on high sulfate brines, then processing can proceed, but the recovery rate of lithium is insufficient and impurities remain high
Solution Approach 1:
The rougher flotation stage performs preliminary separation by removing coarse impurities and concentrating lithium sulfate monohydrate before the cleaner stages. This preliminary action prepares the material for subsequent high-purity concentration steps, ensuring both high recovery rates and low impurity content in the final product
Solution Approach 2:
Different flotation stages use locally optimized conditions and reagents tailored to specific purification needs. The rougher stage uses conditions optimized for high recovery, while cleaner stages use conditions optimized for high purity. This local quality approach allows each stage to perform its specific function effectively, achieving both high productivity and low impurity content
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 effectively concentrates lithium sulfate monohydrate to over 95% purity, addressing the financial unattractiveness of high sulfate brines by enhancing recovery and reducing impurities.
Implementation Method 1
flotation, and leaching is employed to concentrate lithium sulfate monohydrate with low impurity contents
Implementation Method 2
followed by a leaching stage to achieve over 95% purity
Data Source
AI summary
This patent application refers to a global process to obtain lithium sulfate monohydrate ore with low contents of impurities associated to chlorine and magnesium; in particular, the process consists of the concentration, through grinding, flotation, leaching and filtration stages, of the lithium sulfate present in potassium Carnallite (KCl*MgCl2*6H2O) stockpiles with high contents of lithium sulfate (Li2SO4*H2O) and sodium chloride (NaCl). The greatest advantage of the invention's process is that it uses salts and brines which are not currently being processed today and which have already been extracted far potassium production.

