Nickel Iron Battery Manufacturing: Difference between revisions
(Created page with "= NiFe Factory Material and Plate Model for 20 MWh/year = Assumptions: * Plant output: 20,000 kWh/year * Planning mass intensity: 20 kg/kWh finished wet battery * Total finished battery mass: 400 t/year * 20-foot container payload basis: 28.3 t/container * Plate area model: 40 mg/cm² coated-face loading, 75% utilization, 1.2 V nominal * Resulting areal energy density used for sizing: 104 Wh/m² of coated face {| class="wikitable sortable" ! Material / Metric ! Unit ba...") |
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* Finished-battery outbound logistics are about 14 standard 20-foot containers per year by weight. | * Finished-battery outbound logistics are about 14 standard 20-foot containers per year by weight. | ||
* The electrode line must process about 384,615 m²/year of coated electrode faces under the plate-loading assumption used here. | * The electrode line must process about 384,615 m²/year of coated electrode faces under the plate-loading assumption used here. | ||
= Nickel-Iron Battery Manufacturing Process Chain = | |||
{| class="wikitable sortable" | |||
! Material / Component | |||
! Raw Inputs | |||
! Processing Steps | |||
! Equipment | |||
! Output Product | |||
|- | |||
| Nickel hydroxide active material | |||
| Nickel scrap or nickel salts, NaOH or KOH, water | |||
| 1. Dissolve nickel in acid to form nickel salt solution<br> | |||
2. Precipitate Ni(OH)₂ using NaOH or KOH<br> | |||
3. Filter slurry<br> | |||
4. Wash precipitate<br> | |||
5. Dry powder<br> | |||
6. Mill to particle size | |||
| Dissolution reactor<br>Stirred tank precipitator<br>Filter press<br>Dryer oven<br>Ball mill or jet mill | |||
| Nickel hydroxide powder | |||
|- | |||
| Iron electrode powder | |||
| Iron powder feedstock, optional additives (graphite, iron sulfide) | |||
| 1. Acquire or atomize iron powder<br> | |||
2. Blend additives<br> | |||
3. Homogenize powder mixture | |||
| Powder atomizer (if internal)<br>Ribbon blender<br>Powder mixer | |||
| Iron electrode powder blend | |||
|- | |||
| Potassium hydroxide electrolyte | |||
| KOH pellets, distilled water, optional lithium hydroxide additive | |||
| 1. Purify water<br> | |||
2. Dissolve KOH slowly with agitation<br> | |||
3. Add optional LiOH stabilizer<br> | |||
4. Filter solution | |||
| Mixing tank<br>Agitator<br>Filtration unit | |||
| Battery electrolyte solution (20–30% KOH) | |||
|- | |||
| Nickel current collector | |||
| Steel coil or mesh | |||
| 1. Steel coil cleaning<br> | |||
2. Perforation or mesh forming<br> | |||
3. Optional nickel plating<br> | |||
4. Sheet cutting | |||
| Coil feed line<br>Punch press<br>Plating bath<br>Shear cutter | |||
| Nickel current-collector sheets | |||
|- | |||
| Iron current collector | |||
| Steel coil or mesh | |||
| 1. Coil cleaning<br> | |||
2. Perforation or mesh stamping<br> | |||
3. Degreasing<br> | |||
4. Sheet cutting | |||
| Coil line<br>Punch press<br>Degreasing washer<br>Sheet cutter | |||
| Iron electrode mesh sheets | |||
|- | |||
| Nickel electrode plates | |||
| Nickel hydroxide powder, binder (PTFE), conductive carbon, solvent, collector mesh | |||
| 1. Slurry mixing<br> | |||
2. Roll-to-roll coating onto collector<br> | |||
3. Drying oven<br> | |||
4. Compression/calendering<br> | |||
5. Plate cutting | |||
| Planetary mixer<br>Coating line<br>Drying oven<br>Calender rollers<br>Laser or punch cutter | |||
| Nickel electrode plates | |||
|- | |||
| Iron electrode plates | |||
| Iron powder mixture, binder, solvent, steel mesh | |||
| 1. Paste mixing<br> | |||
2. Paste coating or filling into mesh<br> | |||
3. Drying<br> | |||
4. Compression/calendering<br> | |||
5. Plate cutting | |||
| Mixer<br>Coating station<br>Drying oven<br>Roll press<br>Plate cutter | |||
| Iron electrode plates | |||
|- | |||
| Separator sheets | |||
| Polypropylene, polyethylene, nylon, or cellulose sheet rolls | |||
| 1. Receive separator rolls<br> | |||
2. Slit to width<br> | |||
3. Die-cut sheets | |||
| Slitting machine<br>Die cutter | |||
| Separator sheets | |||
|- | |||
| Plastic battery cases | |||
| HDPE or polypropylene pellets (virgin or recycled) | |||
| 1. Pellet drying<br> | |||
2. Injection molding<br> | |||
3. Cooling<br> | |||
4. Trim flashing | |||
| Plastic dryer<br>Injection molding machine<br>Trim station | |||
| Battery case halves | |||
|- | |||
| Bus bars and terminals | |||
| Copper bar stock or sheet | |||
| 1. Cut to length<br> | |||
2. Drill terminal holes<br> | |||
3. Surface cleaning | |||
| Saw or shear<br>CNC drill<br>Deburring tools | |||
| Copper bus bars and terminals | |||
|- | |||
| Electrode stack assembly | |||
| Nickel plates, iron plates, separators | |||
| 1. Pick-and-place electrode stacking<br> | |||
2. Insert separators<br> | |||
3. Align stack | |||
| Automated stacking machine<br>Robotic arm | |||
| Cell electrode stack | |||
|- | |||
| Tab welding | |||
| Electrode tabs and bus bar leads | |||
| 1. Align tabs<br> | |||
2. Weld tabs to bus bars | |||
| Ultrasonic welder<br>Resistance welder | |||
| Electrically connected electrode stack | |||
|- | |||
| Cell insertion | |||
| Electrode stack, plastic case | |||
| 1. Insert stack into molded case<br> | |||
2. Install internal insulation | |||
| Robotic assembly station | |||
| Cell assembly | |||
|- | |||
| Electrolyte filling | |||
| Electrolyte solution | |||
| 1. Metered electrolyte fill<br> | |||
2. Degas air bubbles | |||
| Metering pump<br>Fill station | |||
| Filled battery cell | |||
|- | |||
| Cell sealing | |||
| Cell lid, gasket | |||
| 1. Lid placement<br> | |||
2. Ultrasonic weld or compression seal | |||
| Ultrasonic welder<br>Press | |||
| Sealed battery cell | |||
|- | |||
| Formation cycling | |||
| Newly assembled cells | |||
| 1. Initial charge cycle<br> | |||
2. Rest period<br> | |||
3. Discharge cycle<br> | |||
4. Repeat formation cycles | |||
| Programmable formation racks<br>Battery cyclers | |||
| Activated NiFe battery cells | |||
|- | |||
| Quality testing | |||
| Finished cells | |||
| 1. Leak test<br> | |||
2. Capacity test<br> | |||
3. Internal resistance measurement<br> | |||
4. Visual inspection | |||
| Pressure tester<br>Battery analyzer<br>Inspection station | |||
| Qualified battery cells | |||
|- | |||
| Module assembly | |||
| Cells, bus bars, frame | |||
| 1. Arrange cells<br> | |||
2. Connect bus bars<br> | |||
3. Install terminals<br> | |||
4. Final inspection | |||
| Assembly bench<br>Torque tools | |||
| Battery module | |||
|- | |||
| Recycling loop | |||
| Used cells | |||
| 1. Drain electrolyte<br> | |||
2. Shred plastic cases<br> | |||
3. Separate metals<br> | |||
4. Recover nickel compounds<br> | |||
5. Recycle steel | |||
| Shredder<br>Magnetic separator<br>Chemical recovery tanks | |||
| Recovered nickel, steel, and plastics | |||
|} | |||
Latest revision as of 01:19, 16 March 2026
NiFe Factory Material and Plate Model for 20 MWh/year
Assumptions:
- Plant output: 20,000 kWh/year
- Planning mass intensity: 20 kg/kWh finished wet battery
- Total finished battery mass: 400 t/year
- 20-foot container payload basis: 28.3 t/container
- Plate area model: 40 mg/cm² coated-face loading, 75% utilization, 1.2 V nominal
- Resulting areal energy density used for sizing: 104 Wh/m² of coated face
| Material / Metric | Unit basis | Per kWh | Annual total for 20 MWh | Commodity cost | Commodity $/kWh | Annual commodity cost | Integrated $/kWh | Annual integrated cost | 20 ft containers by weight |
|---|---|---|---|---|---|---|---|---|---|
| Nickel, contained metal | kg | 1.20 | 24.0 t | $17.34/kg | $20.81 | $416,160 | $20.81 | $416,160 | 0.85 |
| Nickel hydroxide equivalent | kg | 1.90 | 37.9 t | derived from nickel content | n/a | n/a | n/a | n/a | 1.34 |
| Iron powder | kg | 5.50 | 110.0 t | $2.00/kg purchased | $11.00 | $220,000 | $4.40 | $88,000 | 3.89 |
| Steel mesh / sheet / case internals | kg | 6.00 | 120.0 t | $1.018/kg purchased | $6.11 | $122,160 | $3.60 | $72,000 | 4.24 |
| KOH, dry basis | kg | 2.00 | 40.0 t | $0.91/kg | $1.82 | $36,400 | $1.82 | $36,400 | 1.41 |
| HDPE / PP case resin | kg | 1.00 | 20.0 t | $0.87/kg | $0.87 | $17,400 | $0.87 | $17,400 | 0.71 |
| Copper bus bars / terminals | kg | 0.30 | 6.0 t | $12.758/kg | $3.83 | $76,548 | $3.83 | $76,548 | 0.21 |
| Separator + binder + additives | kg | 0.80 | 16.0 t | $3.00/kg assumed | $2.40 | $48,000 | $2.40 | $48,000 | 0.57 |
| Deionized water | kg | 3.20 | 64.0 t | $0.001/kg assumed | $0.00 | $64 | $0.00 | $64 | 2.26 |
| Total | 20.00 kg | 400.0 t | $46.84/kWh | $936,732 | $37.73/kWh | $754,572 | 14.13 |
Electrode Plate Area Model
The next table is for factory sizing of the electrode fabrication line. It uses the aggressive planning assumption of 104 Wh/m² of coated face.
| Plate metric | Formula basis | Per kWh | Annual total for 20 MWh |
|---|---|---|---|
| Positive coated-face area | 1000 Wh / 104 Wh/m² | 9.62 m² | 192,308 m² |
| Negative coated-face area | matched to positive area | 9.62 m² | 192,308 m² |
| Total coated-face area, both polarities | positive + negative | 19.23 m² | 384,615 m² |
| Positive metal-sheet plate area | double-coated plates, so coated-face area / 2 | 4.81 m² | 96,154 m² |
| Negative metal-sheet plate area | double-coated plates, so coated-face area / 2 | 4.81 m² | 96,154 m² |
| Total metal-sheet electrode area | positive sheet + negative sheet | 9.62 m² | 192,308 m² |
Shipping Container Summary
| Shipping item | Annual tonnage | 20 ft containers at 28.3 t payload |
|---|---|---|
| Finished wet batteries | 400.0 t | 14.13 |
| All nickel input, contained metal basis | 24.0 t | 0.85 |
| Iron powder | 110.0 t | 3.89 |
| Steel | 120.0 t | 4.24 |
| KOH | 40.0 t | 1.41 |
| Everything except water | 336.0 t | 11.87 |
Main Readout
- A 20 MWh/year NiFe plant at 20 kg/kWh is about 400 t/year of finished battery output.
- On purchased materials, this planning model lands near $46.84/kWh.
- With aggressive in-house iron and steel integration, the same model lands near $37.73/kWh.
- Finished-battery outbound logistics are about 14 standard 20-foot containers per year by weight.
- The electrode line must process about 384,615 m²/year of coated electrode faces under the plate-loading assumption used here.
Nickel-Iron Battery Manufacturing Process Chain
| Material / Component | Raw Inputs | Processing Steps | Equipment | Output Product |
|---|---|---|---|---|
| Nickel hydroxide active material | Nickel scrap or nickel salts, NaOH or KOH, water | 1. Dissolve nickel in acid to form nickel salt solution 2. Precipitate Ni(OH)₂ using NaOH or KOH |
Dissolution reactor Stirred tank precipitator Filter press Dryer oven Ball mill or jet mill |
Nickel hydroxide powder |
| Iron electrode powder | Iron powder feedstock, optional additives (graphite, iron sulfide) | 1. Acquire or atomize iron powder 2. Blend additives |
Powder atomizer (if internal) Ribbon blender Powder mixer |
Iron electrode powder blend |
| Potassium hydroxide electrolyte | KOH pellets, distilled water, optional lithium hydroxide additive | 1. Purify water 2. Dissolve KOH slowly with agitation |
Mixing tank Agitator Filtration unit |
Battery electrolyte solution (20–30% KOH) |
| Nickel current collector | Steel coil or mesh | 1. Steel coil cleaning 2. Perforation or mesh forming |
Coil feed line Punch press Plating bath Shear cutter |
Nickel current-collector sheets |
| Iron current collector | Steel coil or mesh | 1. Coil cleaning 2. Perforation or mesh stamping |
Coil line Punch press Degreasing washer Sheet cutter |
Iron electrode mesh sheets |
| Nickel electrode plates | Nickel hydroxide powder, binder (PTFE), conductive carbon, solvent, collector mesh | 1. Slurry mixing 2. Roll-to-roll coating onto collector |
Planetary mixer Coating line Drying oven Calender rollers Laser or punch cutter |
Nickel electrode plates |
| Iron electrode plates | Iron powder mixture, binder, solvent, steel mesh | 1. Paste mixing 2. Paste coating or filling into mesh |
Mixer Coating station Drying oven Roll press Plate cutter |
Iron electrode plates |
| Separator sheets | Polypropylene, polyethylene, nylon, or cellulose sheet rolls | 1. Receive separator rolls 2. Slit to width |
Slitting machine Die cutter |
Separator sheets |
| Plastic battery cases | HDPE or polypropylene pellets (virgin or recycled) | 1. Pellet drying 2. Injection molding |
Plastic dryer Injection molding machine Trim station |
Battery case halves |
| Bus bars and terminals | Copper bar stock or sheet | 1. Cut to length 2. Drill terminal holes |
Saw or shear CNC drill Deburring tools |
Copper bus bars and terminals |
| Electrode stack assembly | Nickel plates, iron plates, separators | 1. Pick-and-place electrode stacking 2. Insert separators |
Automated stacking machine Robotic arm |
Cell electrode stack |
| Tab welding | Electrode tabs and bus bar leads | 1. Align tabs 2. Weld tabs to bus bars |
Ultrasonic welder Resistance welder |
Electrically connected electrode stack |
| Cell insertion | Electrode stack, plastic case | 1. Insert stack into molded case 2. Install internal insulation |
Robotic assembly station | Cell assembly |
| Electrolyte filling | Electrolyte solution | 1. Metered electrolyte fill 2. Degas air bubbles |
Metering pump Fill station |
Filled battery cell |
| Cell sealing | Cell lid, gasket | 1. Lid placement 2. Ultrasonic weld or compression seal |
Ultrasonic welder Press |
Sealed battery cell |
| Formation cycling | Newly assembled cells | 1. Initial charge cycle 2. Rest period |
Programmable formation racks Battery cyclers |
Activated NiFe battery cells |
| Quality testing | Finished cells | 1. Leak test 2. Capacity test |
Pressure tester Battery analyzer Inspection station |
Qualified battery cells |
| Module assembly | Cells, bus bars, frame | 1. Arrange cells 2. Connect bus bars |
Assembly bench Torque tools |
Battery module |
| Recycling loop | Used cells | 1. Drain electrolyte 2. Shred plastic cases |
Shredder Magnetic separator Chemical recovery tanks |
Recovered nickel, steel, and plastics |