Cryogenic Storage & LNG Equipment worked example
LNG Transfer Loss with lng transfer loss rate of 30 gal / hr: a worked example
What does the result look like when lng transfer loss rate reaches 30 gal / hr? The full calculation is worked below with real intermediate numbers. Use it when lng transfer loss in cryogenic storage and lng equipment is being quoted and consumables are a real chunk of the cost stack.
The inputs for this scenario
- LNG transfer loss rate: 30 gal / hr (raised for this scenario; the documented default is 12)
- LNG transfer duration: 8 hr (unchanged)
- LNG cost basis: 3.5 $ / gal (unchanged)
Working through the calculation
- Applying the documented formula (Liquid-equivalent LNG lost = LNG transfer loss rate × transfer duration) to the inputs above produces each figure below.
- At this operating point the engine returns 840 $ for lng transfer loss cost, the number this scenario is built around.
- At this operating point the engine returns 240 units for liquid-equivalent lng lost.
- At this operating point the engine returns 8 hr for transfer duration.
- At this operating point the engine returns 3.5 $ / unit for lng cost basis.
How this compares with the baseline
- Against the tool's baseline example, where lng transfer loss rate sits at 12 gal / hr and the headline result is 336 $, this scenario comes in 150% above the baseline at 840 $.
- A figure at this level is achievable when lng transfer loss rate is genuinely sustained, not just peaked for a shift. It assumes a constant hourly loss rate; real boil-off varies with starting temperature, ambient conditions, flow rate, and whether vapor is recovered or vented, so it is an estimate, not a metered measurement.
Results at a glance
- LNG transfer loss cost: 840 $ (headline result)
- Liquid-equivalent LNG lost: 240 units
- Transfer duration: 8 hr
- LNG cost basis: 3.5 $ / unit
Run it with your numbers
- Every input above is editable in the live LNG Transfer Loss calculator, which recalculates instantly and can be shared with the inputs intact.
Last reviewed 2026-05-12.