1. Stage 1: H2 and N2 obtained from natural gas and air
2. Stage 2: Gases compressed to 200 atm
3. Stage 3: Pressurised gases pumped into tank with iron catalyst at 450°C, N2 + 3H2 ⇌ 2NH3
4. Stage 4: Unreacted H2 and N2, and product NH3 pass into cooling tank, NH3 liquefied and stored
5. Stage 5: Unreacted H2 and N2 recycled back into the system