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Quenching distances and maximum wall heat fluxed computed in laminar cases are compared to DNS results.
Quenching distances and maximum wall heat fluxes are derived from the quantitatively measured gas phase temperatures.
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Circumferential maximum wall temperature and minimum heat transfer coefficient were selected as the benchmark data to get a conservative conclusion in support of the fuel design and safety analysis.
The effects of nanoparticles volume concentration (0.25%, 0.5%, 1% and 1.5%) and different flow rates on wall temperature profile, maximum wall temperature, local and averaged heat transfer coefficient and local and averaged Nusselt number is studied by this experiment.
Moreover, the wall heat flux has the maximum value for the situation in which thermoporetic force is absent.
It is found that there is an optimal strip-fin size to minimize the pressure drop or pumping power on the constraint condition of maximum wall temperature, and this optimal size depends on the input heat flux and the maximum wall temperature.
It was found that even the wall heat flux was up to 1500 W/m2, the maximum wall temperature was lower than 350 °C.
In the range of parameters investigated, increases in differences between inlet and maximum wall temperatures up to 200 K are shown to have small influences on the flow field and negligible effects on heat transfer performances.
The comparison among the maximum wall temperatures shows that the simple channel is the most critical configuration at steady state condition, but it is the best configuration during the transient heating at the first overshoot.
The maximum wall temperature of wall re-heater is about 35 K lower than that of the spiral wall heater.
Wall heat flux.
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