Lithium Battery Recycling Wastewater Treatment: Black Mass, Electrolyte and Metal Removal
Recycling lithium-ion batteries produces water from several distinct places: the wash water from mechanical processing, the leach and precipitation circuits of a hydrometallurgical plant, and the gas scrubbing that catches electrolyte breakdown products. The stream carries nickel, cobalt, manganese and lithium in solution, fluoride from the electrolyte salt, and an organic solvent fraction. It is a metals and fluoride job with a small organic load, and the design question is whether the plant targets discharge or zero liquid discharge, because that choice changes almost every unit.
Where the Water Comes From
Mechanical processing, where cells are shredded and separated, uses water or a brine to wash the black mass off the current collector foils, and that water carries fine electrode material.
Hydrometallurgical recovery leaches the black mass in acid and then precipitates the metals step by step, and each precipitation step produces a filtrate that carries the remaining metals forward.
Thermal processing routes send electrolyte and solvent breakdown products to a scrubber, and the scrubber liquor is where the fluoride ends up.
Floor wash and equipment cleaning add a dilute but variable stream that a plant should keep separate from the process liquors.

The result is several streams of very different strength, and treating them as one combined flow is the most common design mistake in this industry.
Fluoride
The electrolyte salt in a lithium cell is a fluorinated compound, and on contact with water or heat it breaks down to release fluoride. The process logic sits close to what is described in Potato Processing effluent, particularly on the pretreatment side.
Fluoride is removed by precipitation as calcium fluoride, and the precipitation is run with an excess of calcium because fluoride has a solubility floor that a stoichiometric dose will not reach.
The sludge is calcium fluoride with co-precipitated metals, and it is classified before disposal rather than treated as an inert salt.
Fluoride is also a materials issue. It attacks glass and some stainless grades, so the treatment circuit is specified for it rather than adapted later. Where several streams need joint treatment, Fish and Seafood Processing Wastewater Treatment is the more detailed reference.

Metals and Recovery
Nickel, cobalt and manganese are recovered by precipitation or solvent extraction at controlled pH, and the sequence matters because the precipitation windows overlap.
Lithium is usually the last metal recovered and the hardest, because it stays soluble across the range where the others precipitate.
Copper and aluminium from the current collectors enter the leach and are removed early, and aluminium in solution is a particular nuisance because it precipitates across a wide range.
Where recovery is complete, the final filtrate is a sulfate or chloride salt stream rather than a metal stream, and it is treated as a salinity problem.

Organics and Solvents
The organic solvent fraction from the electrolyte is small in volume and high in chemical oxygen demand, and it is usually separated at source rather than diluted into the main flow. Much of this mirrors the situation set out in Silver Refining and Electroforming Wastewater Treatment.
Where a plant uses a thermal route, most of the organic fraction is destroyed in the furnace and the scrubber liquor carries only the breakdown products.
Measured Results from Plants We Built
We commissioned a 20 m³/day plant for this duty in Nantong, Jiangsu back in 2022. Feed COD came in around 43,040 mg/L and left at 500 mg/L — 98.8% removal. The train was Fenton + primary sedimentation + DAF + hydrolysis acidification + contact oxidation.
| Location | Year | Flow | Feed COD | Treated COD | Removal |
|---|---|---|---|---|---|
| Nantong, Jiangsu | 2022 | 20 m³/d | 43,040 mg/L | 500 mg/L | 98.8% |
Figures are site-measured values from commissioned plants, not modelled estimates.
The scrubbing liquor is therefore a fluoride and acidity problem with little organic content, which is easier than a mixed stream.
Zero Liquid Discharge
Many battery recycling plants are designed for zero liquid discharge, because the salt load is high enough that a discharge consent is difficult and because the recovered water has process value.
A zero liquid discharge circuit concentrates the salt stream by membrane and then by evaporation, producing a solid salt for disposal and a distillate for reuse.

The economics depend on the salt load, which is why the upstream decision to keep streams separate matters. A dilute combined flow costs far more to evaporate than a small concentrated one.
Keep the streams separate at source. A combined flow is larger, saltier and harder to recover from.
Treat fluoride as a design constraint, not a polishing step. It dictates materials and it dictates the sludge classification.
Finally, decide discharge versus zero liquid discharge early. The two targets produce different plants and the decision cannot be reversed cheaply.
Where This Fits in the Wider Plant
The same selection criteria reappear in Ion Exchange and Softener Regeneration effluent, which is worth opening alongside this one. Most facilities do not run a single clean stream, and a shared equalisation and biological stage is usually the economical answer once the streams are chemically compatible.
Why Choose Baihuipu as Your Manufacturer
Picking a supplier for this kind of plant is mostly about who carries the risk when something goes wrong. We have built this equipment for more than twenty years, and we are the ones who fabricated it, programmed the controls and will still answer the phone three years from now.
In-House Fabrication
Our Guangdong works produces everything from standard modular units to fully bespoke lines. Building in-house keeps cost, schedule and quality under our own control rather than a subcontractor's goodwill.
Two Decades of Field Data
Food and beverage, chemicals, electroplating, textile dyeing, mining, municipal work — we have commissioned across all of them. The useful part is not the project count, it is having seen how plants fail in year seven and designing those failures out.
Documentation You Can Actually Audit
Each system ships with as-built drawings, material certificates, welding records and a functional specification. If a client's own consultant wants to review the process calculation basis, we hand it over rather than treating it as proprietary.
We Engineer the Whole Train
Screening, equalisation, biological or chemical treatment, membranes, evaporation, brine handling — the complete line comes from one organisation. Process design, mechanical, electrical and PLC programming sit under the same roof, so there is no gap for finger-pointing at handover.
Spares, Service and Commissioning
Membranes, dosing pumps, diffusers, instrumentation and blowers are stocked for the systems we sell. Our control systems support remote diagnostics, and we can put an engineer on site for commissioning, training or an unplanned shutdown.
Talk to Our Engineers
Send through your raw water data and we will advise on the viable process route and realistic operating cost before you commit to anything. We can be reached on WhatsApp: +86 13631765076 or through hkbhp.com.
WhatsApp: +86 13631765076
Frequently Asked Questions
Which discharge standard will the treated water meet?
We design against whatever consent applies at your boundary — GB 8978, local sewer limits, or a ZLD target with no liquid discharge at all. The design basis is agreed in writing before fabrication, so there is no argument later about what "compliant" meant.
Can you work with our existing equipment?
Often yes. We regularly integrate into existing civil structures where the concrete is sound, replacing internals and controls rather than starting over. We will tell you honestly when legacy kit is beyond economic repair.
How much operator attention does the system need day to day?
Automatic control handles dosing, backwash and level control. Realistically your team spends time on chemical top-up, sample testing and sludge handling — maybe one to two hours per shift on lithium battery recycling duty, less if you opt for remote monitoring.
What spare parts should we hold on site?
Critical spares are pumps, dosing valves, instrumentation sensors and any specialty media. We ship a recommended spares kit with the plant and hold stock for everything we supply, so lead times on replacements stay short.
