Finding
Cell cost and yield are decided in the electrode line and in formation, which is why process changes there - dry electrode coating, faster formation - matter more than cell format
Cylindrical, prismatic and pouch cells share one flow: coat cathode slurry on aluminum foil and anode slurry on copper foil, dry and compress the electrodes, assemble them with a separator in a dry room, fill with electrolyte, then charge the cell for the first time (formation) and hold it for days to weeks (aging) to screen out defects. Electrode drying with NMP solvent recovery, dry-room air handling and formation cycling are the largest energy loads in a cell plant.
Chinese makers set the benchmark for speed and scrap rate: CATL, BYD, CALB, EVE and Gotion run lines at a scale and yield that new Western plants have struggled to match - Northvolt's failure to ramp its Skellefteå plant ended in bankruptcy in 2025. Korean and Japanese makers (LG Energy Solution, Samsung SDI, SK On, Panasonic) run most US cell plants. Most coating, calendering, winding and formation equipment comes from Chinese suppliers such as Wuxi Lead, Yinghe and Hymson, alongside Korean and Japanese toolmakers.
Dry electrode coating removes the slurry solvent and the drying oven. Tesla has scaled a dry cathode process for 4680 cells at Giga Texas; LG Energy Solution and others are piloting it. Module and pack assembly is less automated, less energy-intensive and is usually done near the vehicle plant.
Process
Process steps
The 14 steps from slurry to pack. Formation and aging are the longest; electrode coating is the most capital-intensive.
| Step | Stage | Key inputs | Output |
|---|---|---|---|
| Slurry mixing | Electrode | Cathode (NMC, LFP) or graphite anode powder, binder, conductive carbon, solvent | Uniform slurry |
| Coating | Electrode | Aluminum foil (cathode), copper foil (anode) | Active material on current collector |
| Drying | Electrode | Convection ovens; NMP solvent recovery on the cathode line | Solvent removed |
| Calendering | Electrode | Heated rollers | Target thickness, density and porosity |
| Slitting | Electrode | Electrode rolls | Electrode strips at cell width |
| Stacking or winding | Cell | Anode, cathode, separator | Electrode stack or jelly roll in a can or pouch |
| Tab welding | Cell | Laser or ultrasonic welders | Tabs joined to terminals or collector plates |
| Dry room hold | Cell | Air below 1% relative humidity | Moisture-free cell before fill |
| Electrolyte filling | Cell | LiPF6 in carbonate solvents (EC, DMC) | Wetted electrodes |
| Formation | Finish | Controlled first charge and discharge | Solid-electrolyte interphase (SEI) on the anode |
| Aging | Finish | Days to weeks at controlled temperature | Self-discharge screening |
| Cell testing | Finish | Capacity, voltage, internal resistance | Graded, matched cells |
| Module assembly | Pack | Cells, busbars, thermal interface | Series-parallel blocks; skipped in cell-to-pack designs |
| Pack assembly | Pack | Modules or cells, BMS, cooling, enclosure | Finished EV or BESS pack |
Energy
Where the energy goes, and the electrified fix
| Step | Conventional | Electrified or eliminated | Status |
|---|---|---|---|
| Electrode drying | Gas-fired or resistive convection ovens; NMP recovery | Dry electrode coating; infrared or laser drying | Dry cathode in Tesla 4680 production; others piloting |
| Dry rooms | Large air-handling and desiccant systems | Mini-environments around critical steps | Common in new Chinese lines |
| Formation | Resistive cyclers that burn energy as heat | Regenerative bidirectional cyclers; shorter protocols | Standard on new lines |
| Calendering | Hydraulic presses | Servo-driven rolls with inline thickness control | Standard |
| Pack assembly | Pneumatic tools | Electric servo robots and torque tools | Standard in gigafactories |
EV vs BESS
EV and BESS cells
| Category | EV cells | BESS cells |
|---|---|---|
| Chemistry | LFP for most volume; NMC and NCA for long range | LFP almost entirely; sodium-ion entering |
| Format | Cylindrical, prismatic, pouch | Large prismatic (280 to 500+ Ah) |
| Priority | Energy density, fast charging | Cycle life, cost per kWh, safety |
| Thermal management | Liquid cooling | Liquid cooling in most new containers |
Sources
Sources and scope
- Scope
- Battery Manufacturing Process
- Sources
- Manufacturer disclosures; equipment supplier literature; Northvolt bankruptcy filings (2025)
- Updated
- October 2026