R-290 GWP and CO₂e
Propane. Current and expanding, because it sits outside the F-Gas phase-down entirely. The trade-off is flammability, not compliance paperwork.
Great Britain
3
Retained Regulation (EU) No 517/2014, Annex IV (non-fluorinated substances used in mixture GWP calculation)
EU / Northern Ireland
0.02
Regulation (EU) 2024/573, Annex VI (non-fluorinated substances, AR6 basis)
These two figures genuinely differ. Use the one for the regime the equipment is in — Great Britain, or Northern Ireland under the Windsor Framework.
Charge in kg → tonnes CO₂e
t CO₂e = charge (kg) × GWP ÷ 1,000. This figure, not the charge in kilograms, is what sets the statutory leak-check frequency.
| Charge | t CO₂e (GB) | t CO₂e (EU/NI) |
|---|---|---|
| 1 kg | 0.00 | 0.00 |
| 2 kg | 0.01 | 0.00 |
| 5 kg | 0.01 | 0.00 |
| 10 kg | 0.03 | 0.00 |
| 20 kg | 0.06 | 0.00 |
| 50 kg | 0.15 | 0.00 |
| 100 kg | 0.30 | 0.00 |
Leak-check thresholds in kg
Propane is not a fluorinated greenhouse gas, so the F-Gas leak-check thresholds do not apply to it in either regime — there is no charge size at which a statutory F-Gas leak check is triggered. The values above exist in the annexes only so that the GWP of a *mixture* containing propane can be calculated. What does govern a propane system is its flammability: it is an A3, and the charge limits, ventilation and electrical requirements come from the relevant safety standard and the site risk assessment, not from F-Gas.
Where you meet R-290
- •Monobloc air-to-water heat pumps
- •Small integral refrigeration and process cooling units
- •Small chillers where an outdoor or plant-room safety case supports it