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LNG BOG Compressor - Shaft Power

Adiabatic shaft-power estimate for a boil-off gas (BOG) compressor handling methane from atmospheric tank vapour to the DF-engine supply pressure.

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Formula, assumptions, and limits

Pshaft=m˙cpT1[(p2p1)k1k1]ηadP_{shaft} = \frac{\dot m \cdot c_p \cdot T_1 \cdot \left[\left(\frac{p_2}{p_1}\right)^{\frac{k-1}{k}} - 1\right]}{\eta_{ad}}
SymbolMeaningUnit
m˙\dot mBOG mass flowkg/s
cpc_pSpecific heat at constant pressurekJ/kg·K
T1T_1Suction temperatureK
kkIsentropic exponent
ηad\eta_{ad}Adiabatic efficiency

Source: GIIGNL Handbook - BOG Management; NIST Chemistry WebBook - methane

In short

Adiabatic shaft-power estimate for a boil-off gas (BOG) compressor handling methane from atmospheric tank vapour to the DF-engine supply pressure.

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