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Boil-Off Gas (BOG) Calculator

LNG/NGL Tank Heat Ingress & BOG Generation

Boil-Off Gas (BOG) Calculator
Calculate the boil-off gas generation rate from LNG and NGL cryogenic storage tanks due to heat ingress. Determines heat transfer through tank walls, roof, and bottom slab, with BOG mass and volume rates, holding time without recovery, and compressor sizing for BOG recovery systems. Per API 625, EN 1473, and GPSA Ch. 11.

Tank Type & Product

Tank Dimensions

ft
ft
%

Insulation

in

Typical: Perlite 24-48", PU Foam 4-8", Vacuum varies

Environmental Conditions

°F
°F

Auto-set from product: LNG=-260, Ethane=-128, Propane=-44, Butane=31

mph
-

1.0 = outdoor, 0.0 = indoor/shaded

Additional Parameters

Btu/lb

LNG=219, Ethane=210, Propane=184, Butane=166, NGL Mix=195

%

Typical 5-10% of total for piping and nozzle penetrations

$/MMBtu

Understanding Boil-Off Gas

What is BOG?
Boil-off gas is vapor generated when heat enters a cryogenic storage tank. Since the product is stored at its boiling point, any heat ingress causes evaporation. The BOG rate depends on insulation quality, ambient conditions, and tank geometry.
Typical BOG Rates:
Full containment LNG: 0.03-0.05%/day
Double wall LNG: 0.05-0.08%/day
Single containment: 0.08-0.15%/day
Pressurized NGL: 0.01-0.03%/day
BOG Management Options:
BOG recovery compressor (most common), BOG recondenser, fuel gas system, or flare (last resort). Proper BOG management is critical for tank pressure control, safety, economics, and environmental compliance.

Formula

mBOG = Qtotal / hfg
mBOG = Boil-off gas mass rate (lb/hr)
Qtotal = Total heat ingress (Btu/hr)
hfg = Latent heat of vaporization (Btu/lb)
Qwall = Uwall × Awall × ΔT
Qroof = Uroof × Aroof × ΔT + Qsolar
Qbottom = Ubottom × Abottom × (Tground - Tproduct)

Standards & References

  • API 625
    Tank Systems for Refrigerated Liquefied Gas Storage
  • EN 1473
    Installation and Equipment for LNG — Design of Onshore Installations
  • GPSA Engineering Data Book
    Chapter 11: Hydrocarbon Recovery
  • NFPA 59A
    Standard for LNG Production, Storage, and Handling
  • BS 7777
    Flat-Bottomed, Vertical, Cylindrical Storage Tanks for Low Temperature Service

Engineering Notes

  • Design BOG: Size recovery systems for worst-case summer ambient plus solar load
  • U-values: Overall heat transfer coefficients include insulation, tank wall, and surface film resistances
  • Solar load: Can add 10-20% to total heat ingress for outdoor unshaded tanks
  • Wind effect: Higher wind increases the external film coefficient, raising U-values 5-15%
  • Aging: Insulation performance degrades 0.5-1% per year; design for end-of-life conditions
  • Hold time: Relief valve set pressure determines maximum hold time without BOG recovery

Quick Reference — Product Properties

  • LNG: -260°F, hfg=219 Btu/lb, ρ=26.4 lb/ft³
  • Ethane: -128°F, hfg=210 Btu/lb, ρ=35.5 lb/ft³
  • Propane: -44°F, hfg=184 Btu/lb, ρ=31.6 lb/ft³
  • Butane: 31°F, hfg=166 Btu/lb, ρ=36.1 lb/ft³
  • NGL Mix: -80°F, hfg=195 Btu/lb, ρ=33.0 lb/ft³

Frequently Asked Questions

What is boil-off gas (BOG) in LNG storage?

Boil-off gas (BOG) is the vapor generated from cryogenic liquids stored at or near their boiling point when heat enters the storage tank from the surroundings. For LNG stored at approximately -260°F (-162°C), any heat ingress through the tank walls, roof, bottom, or piping penetrations causes a small fraction of the liquid to evaporate. Typical BOG rates for well-insulated LNG tanks are 0.03-0.05% of inventory per day.

How is BOG rate calculated for cryogenic storage tanks?

BOG rate is calculated by first determining total heat ingress into the tank (Q_total = Q_wall + Q_roof + Q_bottom + Q_misc), then dividing by the product's latent heat of vaporization: m_BOG = Q_total / h_fg. The heat ingress through each surface depends on the overall heat transfer coefficient (U-value), surface area, and temperature difference between ambient conditions and the stored product.

What are typical BOG rates for different tank types?

Typical BOG rates vary by tank construction: Full containment LNG tanks achieve 0.03-0.05%/day; double wall LNG tanks 0.05-0.08%/day; single containment 0.08-0.15%/day. Pressurized NGL bullets typically have lower BOG rates due to the product being stored at higher pressures. Tank insulation type (perlite, polyurethane foam, or vacuum) significantly impacts the BOG rate.

Why is BOG management important in LNG terminals?

BOG management is critical because uncontrolled BOG causes tank pressure rise, potentially triggering relief valve operation and product loss. BOG must either be recovered (compressed and returned to the process or used as fuel gas), reliquefied using a BOG recondenser, or flared. Proper BOG management directly impacts terminal economics, safety, and environmental compliance.