Case 1 — HFC-to-NH₃ conversion, food distribution centre, Western Europe
Regional grocery distributor facing F-Gas phase-down on an ageing R404A plant serving 18,000 pallet positions. Budget band USD $2M–$4M.
Before
- R404A central plant, 14 years old, with refrigerant cost rising every quota cycle
- Specific energy consumption roughly 30% above comparable modern plants
- No heat recovery; boiler plant running separately for washdown water
- Leak-repair spend growing year on year; compliance exposure under F-Gas tightening
After
- Energy consumption down roughly a third against the old R404A baseline
- Heat recovery now covers the majority of washdown hot-water demand
- F-Gas compliance exposure removed; refrigerant cost risk effectively eliminated
- Spread between lowest and highest compliant bid narrowed from about 28% to under 10% after normalisation
Procurement approach
- Feasibility study tendered separately from the EPC scope to keep advice independent
- Four conversion specialists invited on one common design basis: duty per suction level, design ambient, N+1 redundancy
- Every bidder required to state refrigerant charge in kg and the architecture chosen to minimise it
- Bids normalised to a 10-year total cost: installed cost, energy at the site tariff, maintenance, expected overhaul and refrigerant risk
Decision criteria
- Demonstrated HFC-to-NH₃ conversion references with existing evaporators retained
- Charge minimisation: low-charge NH₃ package with CO₂ secondary distribution to the sales-floor-adjacent rooms
- 10-year TCO, not headline CAPEX — including energy at part load where the plant runs most of the year
- Heat-recovery scope sized against the site's actual hot-water demand
- Live-site execution plan: the warehouse stayed operational throughout
