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Cooling liquid flow boiling heat transfer in an annular minigap with an enhanced wall

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Figure

Fig. 2. The schematic diagram of the test section: 1- a glass pipe for viewing flow patterns, 2 - a copper pipe, 3 - an annular minigap, 4 - a cartridge heater, 5 - a test section header,  6 – a thermocouple
Fig. 4. A schematic diagram illustrating the assumptions adopted for the planar multilayer wall as horizontal cross-section, #1 - a cartridge heater, #2 - a thermal conductive filler layer, #3 - a metal pipe, #4 - a minigap, #5 - a glass pipe
Fig. 5. Heat transfer coefficient vs. the minigap length, experimental parameters: mass flow rate of 2.22‧ 10-3 kg‧ s-1  a)  qw = 7 kW m-2, b) qw = 11 kW m-2 and c) qw = 18 kW m-2
Fig. 7. Heat transfer coefficient vs. the minigap length, mass flow rate of 6.67‧ 10-3  kg∙s-1, a) qw = 11 kW/m2,  b) qw = 15 kW/m2, c) qw = 18 kW/m2 and d) qw = 24 kW/m2
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