Grey water system
US-2024051852-A1 · Feb 15, 2024 · US
US11203542B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11203542-B2 |
| Application number | US-201716612282-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 11, 2017 |
| Priority date | May 11, 2017 |
| Publication date | Dec 21, 2021 |
| Grant date | Dec 21, 2021 |
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Lithium brine is treated with a multiple pass nanofiltration (NF) membrane system. Sulfate is added to permeate from an upstream pass before it flows through a downstream pass. Optionally the sulfate may be added to the permeate by dosing it with sulfuric acid or a slat such as sodium sulfate. The softened brine may then be processed further, for example by a combination of solvent extraction, electrolysis, crystallization and drying, to produce a lithium hydroxide product that can be used to make batteries.
Opening claim text (preview).
The invention claimed is: 1. A lithium brine treatment system comprising, a) a upstream nanofiltration membrane unit; b) a downstream nanofiltration membrane unit; c) a sulfate dosing system; and d) a solvent extraction system that includes at least a lithium extraction unit and a stripping unit, where the stripping unit includes a lithium chloride discharge outlet, wherein a permeate outlet of the upstream nanofiltration system is connected to a feed inlet of the downstream nanofiltration unit and the sulfate dosing system is connected between the upstream and downstream nanofiltration units. 2. A process for softening lithium brine comprising the steps of, a) flowing the lithium brine to a nanofiltration membrane unit to produce a first permeate; b) adding sulfate to the first permeate; and, c) flowing the first permeate to another nanofiltration membrane unit to produce a softened permeate. 3. The process of claim 2 wherein in step b) an amount of sulfate is added to the first permeate such that a molar concentration of sulfate ions in the first permeate is 70% or more of a sum of the molar concentrations of Ca2+ and Mg2+ ions in the first permeate. 4. The process of claim 2 wherein sulfate is added to the first permeate by adding an aqueous solution of sodium sulfate or sulfuric acid to the first permeate. 5. The process of claim 2 wherein the softened permeate is treated by way of solvent extraction to produce lithium chloride. 6. The process of claim 3 wherein the amount of sulfate is added to the first permeate such that a molar concentration of sulfate ions in the first permeate is less than 80% of a sum of the molar concentrations of Ca2+ and Mg2+ ions in the first permeate. 7. The process of claim 2 wherein the lithium brine has a total dissolved solids concentration between 15 and 35%.
Hydroxides (by simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine C25B1/34) · CPC title
by nanofiltration · CPC title
Halides · CPC title
Inorganic compounds · CPC title
comprising multiple nanofiltration steps · CPC title
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