Journal
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER
Volume 150, Issue -, Pages -Publisher
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijheatmasstransfer.2019.119271
Keywords
Flow boiling; Microchannels; Two-phase instabilities; Two-phase oscillations; Two-phase mixing; Electronic cooling
Categories
Funding
- US Department of Defense, Office of Naval Research [N000141210724, N000141612307]
- National Science Foundation [ECS-0335765]
- U.S. Department of Defense (DOD) [N000141612307] Funding Source: U.S. Department of Defense (DOD)
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Flow boiling in parallel and isolated microchannels has been extensively studied. In this study, five parallel microchannels (W = 200 mu m, H = 250 mu m, L = 10 mm) are interconnected by 28 micro-slots (20 mu m wide and 250 mu m deep) starting from the outlet. These micro-slots serve as nucleation sites to greatly enhance nucleate boiling. More importantly, the alternating and enhanced nucleate boiling in neighboring microchannels can generate additional pressure drop during the bubble growth-departure cycle and hence enable highly desirable periodic rewetting inside channels, particularly near outlet regions. This new microchannel configuration can substantially enhance nucleate boiling during flow boiling processes. Coupling with the enhanced nucleate boiling and the induced thin film evaporation, heat transfer coefficient (HTC) in present microchannel configuration can be enhanced up to similar to 107.6% at mass flux 250 kg/m(2)center dot s with a similar to 17% higher critical heat flux (CHF) compared to the plain-wall microchannels with inlet restrictors (IRs). In addition, we achieve a CHF value of 810 W/cm(2) at a moderate mass flux of 430 kg/m(2)center dot s. All these enhancements are realized without compromising two-phase pressure drop compared to plain wall microchannels with inlet restrictors (IRs). Two-phase flow instabilities in terms of temperature and pressure drop fluctuations are also significantly suppressed. (C) 2019 Elsevier Ltd. All rights reserved.
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