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Effect of Running Parameters on Flow Boiling Instabilities in Microchannels
Flow boiling instability in microchannels is problematic. This study found heat flux, heater length, and mass flux significantly impact instability, with higher heat flux triggering more severe instabilities.
Area of Science:
- Heat Transfer
- Fluid Dynamics
- Microscale Engineering
Background:
- Flow boiling instability (FBI) in microchannels can cause mechanical vibrations and disrupt heat transfer.
- Understanding these instabilities is crucial for reliable microchannel heat sink performance.
Purpose of the Study:
- To experimentally investigate the effects of heat flux, microchannel length, and mass flux on flow boiling instability.
- To analyze pressure drop and temperature variations under different operating conditions.
Main Methods:
- Utilized a synchronous optical visualization experimental system.
- Employed pure acetone as the working fluid in a parallel triangle silicon microchannel heat sink.
- Systematically varied heat flux, heater length, and mass flux to record pressure drops and surface temperatures.
Main Results:
- Identified heat flux, heater length, and mass flux as key parameters influencing boiling instability.
- Observed earlier boiling incipience (TBI) and critical heat flux (CHF) at lower mass flux or longer heater lengths.
- Found pressure drops increased sharply in the two-phase region with increasing heat flux, leading to more pronounced instabilities.
Conclusions:
- Heat flux, microchannel length, and mass flux are critical factors determining flow boiling instability.
- Optimizing these parameters is essential for mitigating undesirable vibrations and maintaining stable heat transfer in microchannels.
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