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Bernardin, J. D. & Mudawar, I. Film boiling heat transfer of droplet streams and sprays.
Mass flux increases the saturated convective boiling heat transfer coefficient.
The boiling heat transfer can not be ignored.
Increase in system pressure increases the subcooled boiling and saturated nucleate boiling heat transfer coefficient but decreases the saturated convective boiling heat transfer coefficient.
This results in a self-cleaning fluidised bed boiling heat exchanger.
The effect of channel shape and geometrical parameter on the boiling heat transfer is studied.
Effects of boiling heat transfer and manufacturability are also discussed in this paper.
These studies may provide a more reasonable mechanistic description or engineering instruction on boiling heat transfer.
Two models are presented for the prediction of flow boiling heat transfer coefficients.
The evaluation analysis sets a channel transition criterion for flow boiling heat transfer of CO2.
However, heat flux has no influence on saturated convective boiling heat transfer coefficient.
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