Continuous bright-annealing and brazing furnaces need a reducing atmosphere. The traditional answer is a yard full of hydrogen cylinders; the modern answer is an on-site ammonia cracker. The numbers are not close.
What an Ammonia Cracker Actually Does
Liquid ammonia is vaporized and passed over a heated nickel catalyst at ~320 °C. Ammonia decomposes into 75% hydrogen and 25% nitrogen — a reducing atmosphere that prevents oxidation and can even reduce existing surface oxides during the anneal. Residual ammonia stays below 10 ppm, and below 3 ppm with a purification unit.
The Cost Comparison
| Item | Hydrogen cylinders | On-site ammonia cracker |
|---|---|---|
| Gas cost per Nm³ | High (delivery + rental + handling) | ≈ 0.4 kg NH₃ + ~0.5 kWh electricity |
| Cost stability | Volatile, supplier-dependent | Tied to ammonia & electricity price |
| Delivery dependency | Weekly truck + cylinder handling | Ammonia tank refilled monthly/quarterly |
| Safety exposure | High-pressure H₂ on site, transport risk | Low-pressure system, no H₂ storage |
| Purity control | Fixed by supplier | Adjustable, residual NH₃ < 3 ppm with purifier |
| Typical payback | — | 8–18 months at ≥ 20–30 Nm³/h continuous |
Safety: The Deciding Factor for Many Plants
Storing enough high-pressure hydrogen to feed a continuous furnace means accumulated flammable inventory — and in many jurisdictions, licensing, distances and inspection regimes that grow with cylinder count. An ammonia cracker holds only a few hundred liters of liquid ammonia (itself a regulated chemical, but far easier to license than bulk H₂), generates hydrogen on demand at low pressure, and consumes it immediately. There is no meaningful hydrogen inventory at any moment.
When Cylinders Still Make Sense
Below roughly 10 Nm³/h of intermittent use — a small batch furnace run a few hours a week — cylinder hydrogen remains reasonable. The cracker wins decisively for continuous lines, multi-shift operations and any plant where cylinder logistics are already a pain point.