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The model accounts for the rotation of the kiln walls and mixing blades, multiphase flow modelling of the solid (fuel) and gaseous (mixture of gases) phases, heat transfer between phases and the heated kiln walls and mass transfer due to chemical reaction between species of different (heterogeneous) phases.
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Similar effects can be seen during the substorm expansion and recovery phases (not shown) but this is expected if one considers that the substorm expansion phases heats a preheated plasma sheet.
Additionally, solid phase heat recovery increases the efficiency gains made possible by gas phase heat recovery.
CPL is a high efficiency two-phase heat transfer device.
Hence, the degradation of two-phase heat transfer due to mass diffusion resistance is not captured.
For the absorber, this is caused by the degradation of the two-phase heat transfer coefficient.
Most of the studies are focused on pool boiling and single-phase heat transfer in microchannels.
Various properties relevant to two-phase heat transfer were also measured.
Martensite (bright phase), heat affected zone below martensite and pearlite matrix.
Heat pipes are two-phase heat transfer devices with extremely high effective thermal conductivity.
Lee et al. [26] investigated on the use of nanofluids for single-phase and two-phase heat transfer in microchannels.
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