Industry · Battery & new energy

Battery & new energy material processing

Cathode, anode, electrolyte and solid-state powders are judged on contamination, moisture and repeatability — not on throughput alone.

Battery material production tolerates very little contamination. Iron, chromium or nickel picked up from a worn agitator, moisture absorbed during an open transfer, or a batch that was blended three minutes too long all show up later as capacity fade or inconsistent electrochemical performance.

Our equipment for this sector is configured around three constraints: contact surfaces that will not shed metal ions, a closed material path from receiving to packing, and a documented batch record. That covers cathode active materials (LFP, NMC, LCO, NCA), anode materials (graphite, silicon, LTO), electrolyte precursors and solid-state electrolyte powders.

Battery-grade processing standards

Contamination-controlled contact surfaces

SS316L contact parts with electropolished, crevice-free interiors. Shaft seals are specified for the powder rather than taken from a catalogue.

Inerting and explosion protection

Nitrogen blanketing and oxygen monitoring for solvent-wet and reactive powders, with explosion-proof motors, conductive grounding and pressure relief where the dust classification requires it.

Temperature and vacuum capability

Heating jackets for precursor drying and cooling jackets for exothermic steps. Vacuum-rated vessels where solvent removal or moisture-sensitive material is involved.

Low-attrition blending

Gentle tumbling or low-shear plough action for materials where particle morphology decides flow behaviour — spherical powders for additive manufacturing being the clearest case.

Battery material applications

01

Cathode active materials

LFP, NMC, LCO and NCA precursor blends with lithium source. High-intensity plough mixing for solid-state synthesis, with liquid addition controlled by spray.

02

Anode materials

Natural and artificial graphite, silicon, silicon oxide and LTO. Ribbon mixing for pitch coating and carbon precursor blends.

03

Electrolyte precursors

LiPF6, LiFSI and solvent or additive blending. Corrosion-resistant 316L wetted parts and vacuum-capable vessels for fluoride-bearing chemistry.

04

Solid-state electrolytes

LLZO, LATP and sulfide systems. High-energy mixing with inert gas blanketing; sealed discharge ports for glove-box connection.

05

Conductive additives

Carbon black, CNT and graphene dispersion. Double paddle and high-shear configurations for slurry preparation.

06

Precursor co-precipitation

NMC hydroxide precursor blending with pH-controlled solution addition through injection lances in a 316L ribbon or plough mixer.

Battery-grade equipment

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Frequently asked questions

Which mixer suits LFP cathode powder?

LFP blends usually go through a double cone or plough mixer in 316L with inert gas purging, followed by vacuum drying. The choice between them comes down to how fragile the powder is and whether liquid addition is part of the step.

Can the equipment connect to a glove box?

Yes — sealed discharge ports and vacuum conveying are specified for oxygen- and moisture-sensitive material, so the transfer between the mixer and the glove box stays closed.

How is contamination controlled?

Contact parts are 316L, electropolished and passivated, with crevice-free welds and seals selected for the powder. Wear parts are replaceable and documented, so a batch record can be tied to a known component condition.

Need battery & new energy equipment?

Tell us the material, batch size and any compliance or containment requirement. We will come back with the configuration we would build and the questions we would ask before quoting.

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