Modeling study on two-phase adiabatic expansion in a reciprocating expander
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文摘
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Heat transfer coefficient from the liquid bulk to the gas–liquid interface is correlated as a Nusselt number which is expressed as a function of Prandtl, Reynolds and Bond numbers.

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Using the correlated Nusselt number, the energy balance equations are solved to predict the pressure change and the indicated adiabatic efficiency during two phase adiabatic expansion.

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The model predicts the indicated adiabatic efficiency within about 5% accuracy.

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The model indicates that the degradation of the indicated adiabatic efficiency is mainly due to the insufficient heat transfer from the liquid bulk to the interface.

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