Open Source Electrolyzer: Difference between revisions
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= Rough Stack Materials Budget = | = Rough Stack Materials Budget = | ||
= Corrected Stack Materials and Fabrication Budget (100 kW Alkaline Electrolyzer) = | |||
{| class="wikitable" | {| class="wikitable" | ||
|+ | |+ Detailed Stack Cost Breakdown (Prototype-Realistic) | ||
! Category | ! Category | ||
! Estimated Cost | ! Description | ||
! Estimated Cost Range | |||
|- | |- | ||
| Nickel | | Nickel Foam Electrodes | ||
| Cathode + anode substrate (~24 m² total) | |||
| $600–$3,000 | | $600–$3,000 | ||
|- | |- | ||
| Separator | | Separator (Zirfon) | ||
| ~12 m² diaphragm material | |||
| ~$1,800 | | ~$1,800 | ||
|- | |- | ||
| | | Electrolyte + Chemicals | ||
| KOH + NiSO₄ + FeSO₄ + boric acid | |||
| $200–$600 | |||
|- | |||
| Gaskets | |||
| ~100 cell gasket sets (EPDM/PTFE) | |||
| $150–$500 | |||
|- | |||
| Plastic Frame Stock | |||
| HDPE/PP sheets for ~100 frames | |||
| $400–$1,200 | |||
|- | |||
| Current Collectors + Busbars | |||
| Nickel sheets/mesh + copper busbars + terminals | |||
| $500–$2,000 | |||
|- | |||
| End Plates + Compression Hardware | |||
| Steel plates, tie rods, bolts, springs | |||
| $500–$2,000 | |||
|- | |||
| Fabrication + Machining | |||
| CNC cutting, drilling, finishing of frames and plates | |||
| $1,000–$3,000 | | $1,000–$3,000 | ||
|- | |- | ||
| | | Scrap, Yield Loss, Shipping, Contingency | ||
| $ | | Material losses, damaged parts, supplier overhead | ||
| $1,500–$4,000 | |||
|- | |||
! Total Estimated Stack Cost (Corrected) | |||
! Prototype-scale, materials + fabrication | |||
! $6,650 – $19,100 | |||
|} | |||
= Interpretation = | |||
{| class="wikitable" | |||
! Layer | |||
! Meaning | |||
! Cost Range | |||
|- | |||
| Raw materials only | |||
| Just purchased materials without fabrication overhead | |||
| ~$3,600 – $8,400 | |||
|- | |||
| Practical prototype build | |||
| Includes machining, scrap, and assembly realities | |||
| ~$6,500 – $15,000 (typical target) | |||
|- | |- | ||
| High-friction prototype case | |||
| Inefficient sourcing, mistakes, iteration cycles | |||
| Up to ~$19,000 | |||
|} | |} | ||
= Key Insight = | |||
The earlier mismatch came from mixing two different accounting layers: | |||
* The visible table showed mostly **raw materials** | |||
* The total implicitly included **fabrication, waste, and prototype inefficiencies** | |||
A correct engineering budget must explicitly include: | |||
* manufacturing steps (cutting, machining, assembly) | |||
* process losses (scrap, rework) | |||
* procurement overhead (shipping, minimum orders) | |||
* structural components (compression system, busbars) | |||
Without these, the estimate will systematically understate real build cost. | |||
For planning purposes: | |||
* **Use ~$7k–$15k as a realistic first prototype stack target** | |||
* Expect cost reduction only after: | |||
* volume purchasing | |||
* simplified geometry | |||
* process standardization | |||
Revision as of 04:56, 17 March 2026
https://chatgpt.com/share/69b78df5-6188-8010-8d76-08b5073da11a
No Exotic Materials Required
No exotic manufacturing is required - no exotic membranes outside of off-the-shelf Zirfon separator which appears to contribute 10% to the cost.
$10-20k for a 100kW stack. Payback of one year with 6 hour solar, quicker with wind.
Materials Breakdown and Sourcing
| Component | Specification | Quantity | Typical Cost Range | Example Supplier / Source | Link |
|---|---|---|---|---|---|
| Nickel Foam (Cathode) | 1–2 mm thick, 20–60 PPI, >99% Ni | ~12 m² | $300–$1,500 | MTI Corporation | https://mtixtl.com/products/0-5-mm-thick-nickel-foam-for-battery-cathode-substrate-or-solid-state-electrolyte-support-l-1000-x-w-200-mm-eq-bcnf-05m |
| Nickel Foam (Anode substrate) | same spec as cathode | ~12 m² | $300–$1,500 | Goodfellow | https://www.goodfellow.com/usa/nickel-sizes-foam-group |
| Separator (Zirfon-type diaphragm) | ~0.3–0.5 mm polysulfone + zirconia composite | ~12 m² | ~$1,800 | Agfa Zirfon PERL | https://www.agfa.com/zirfon/ |
| Cell Frames / Spacers | HDPE / polypropylene plates | ~100 pieces | $500–$1,500 | McMaster-Carr plastic sheet | https://www.mcmaster.com/polypropylene-sheets/ |
| End Plates | Carbon steel or stainless plate | 2 pieces | $200–$600 | Online Metals steel plate | https://www.onlinemetals.com/ |
| Gaskets | EPDM or PTFE sheet 1–2 mm | ~100 sets | $100–$400 | McMaster-Carr gasket sheet | https://www.mcmaster.com/epdm-rubber/ |
| Current Collectors | Nickel sheet or nickel mesh | ~2–4 m² | $200–$800 | Alfa Aesar nickel sheet | https://www.fishersci.com/shop/products/nickel-foil/AA43098 |
| Busbars | Copper bar stock | ~3–5 kg | $100–$300 | McMaster copper bar | https://www.mcmaster.com/copper-bars/ |
| Electrolyte | Potassium hydroxide (KOH), 25–30 wt% | ~100–150 L solution | $200–$500 | Lab Alley KOH | https://www.laballey.com/products/potassium-hydroxide-koh |
| Anode Catalyst Bath Chemical | Nickel sulfate (NiSO₄) | ~1–2 kg | $50–$200 | Sigma-Aldrich | https://www.sigmaaldrich.com/US/en/product/aldrich/656895 |
| Anode Catalyst Bath Chemical | Ferrous sulfate (FeSO₄) | ~1 kg | $20–$80 | Fisher Scientific | https://www.fishersci.com/shop/products/ferrous-sulfate-heptahydrate |
| Anode Catalyst Bath Chemical | Boric acid (H₃BO₃) | ~1 kg | $10–$40 | Sigma-Aldrich | https://www.sigmaaldrich.com/US/en/product/sial/695092 |
Summary of Major Materials
| Material | Amount |
|---|---|
| Nickel foam | ~24 m² total |
| Zirfon separator | ~12 m² |
| Plastic frames | ~100 |
| Steel end plates | 2 |
| Gaskets | ~100 sets |
| KOH electrolyte | ~100–150 L |
Rough Stack Materials Budget
Corrected Stack Materials and Fabrication Budget (100 kW Alkaline Electrolyzer)
| Category | Description | Estimated Cost Range |
|---|---|---|
| Nickel Foam Electrodes | Cathode + anode substrate (~24 m² total) | $600–$3,000 |
| Separator (Zirfon) | ~12 m² diaphragm material | ~$1,800 |
| Electrolyte + Chemicals | KOH + NiSO₄ + FeSO₄ + boric acid | $200–$600 |
| Gaskets | ~100 cell gasket sets (EPDM/PTFE) | $150–$500 |
| Plastic Frame Stock | HDPE/PP sheets for ~100 frames | $400–$1,200 |
| Current Collectors + Busbars | Nickel sheets/mesh + copper busbars + terminals | $500–$2,000 |
| End Plates + Compression Hardware | Steel plates, tie rods, bolts, springs | $500–$2,000 |
| Fabrication + Machining | CNC cutting, drilling, finishing of frames and plates | $1,000–$3,000 |
| Scrap, Yield Loss, Shipping, Contingency | Material losses, damaged parts, supplier overhead | $1,500–$4,000 |
| Total Estimated Stack Cost (Corrected) | Prototype-scale, materials + fabrication | $6,650 – $19,100 |
Interpretation
| Layer | Meaning | Cost Range |
|---|---|---|
| Raw materials only | Just purchased materials without fabrication overhead | ~$3,600 – $8,400 |
| Practical prototype build | Includes machining, scrap, and assembly realities | ~$6,500 – $15,000 (typical target) |
| High-friction prototype case | Inefficient sourcing, mistakes, iteration cycles | Up to ~$19,000 |
Key Insight
The earlier mismatch came from mixing two different accounting layers:
- The visible table showed mostly **raw materials**
- The total implicitly included **fabrication, waste, and prototype inefficiencies**
A correct engineering budget must explicitly include:
- manufacturing steps (cutting, machining, assembly)
- process losses (scrap, rework)
- procurement overhead (shipping, minimum orders)
- structural components (compression system, busbars)
Without these, the estimate will systematically understate real build cost.
For planning purposes:
- **Use ~$7k–$15k as a realistic first prototype stack target**
- Expect cost reduction only after:
* volume purchasing * simplified geometry * process standardization