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API Publication 2517, first issued in 1989 and amended by the 1994 Addendum, provides a standardized methodology for estimating evaporation losses from external floating-roof tanks storing volatile liquids. The document supersedes earlier API bulletins and remains a key reference for tank emission calculations in the petroleum industry.
The scope covers standing storage losses and withdrawal losses from external floating-roof tanks. It accounts for losses through rim seals, deck fittings (including hatches, gauging ports, and vacuum breakers), and deck seams. The publication also addresses the effect of deck-mounted equipment and seal systems on overall emission rates.
API Publ 2517 presents a comprehensive set of equations to estimate total evaporation loss from external floating-roof tanks. The loss per year (LT) is the sum of standing storage loss (LS) and withdrawal loss (LW):
| Parameter | Symbol | Typical Units | Description |
|---|---|---|---|
| Tank diameter | D | ft (m) | Nominal diameter of tank shell |
| Wind speed | U | mph (m/s) | Average wind speed at tank site |
| Vapor pressure | PVA | psia (kPa) | True vapor pressure of stored liquid at storage temperature |
| Seal factor | KS | lb-mol/ft·yr (kg-mol/m·yr) | Empirical factor depending on seal system |
| Fitting loss factor | KF | lb-mol/yr (kg-mol/yr) | Loss factor per fitting type |
The rim seal loss is calculated using the equation:
LR = KS · D · PVA · MV · KC
where MV is the molecular weight of the vapor and KC is the product factor for custom sealing systems.
Deck fitting losses depend on the number and type of fittings. The total loss from deck fittings is the sum over all fittings of the product of fitting loss factor (KF) and vapor pressure adjustment.
To properly implement the API Publ 2517 methodology, the following steps are essential: