Heat transfer model for evaporation in microchannels. Part I: presentation of the model

https://engineering.purdue.edu/BTPFL/BTPFL%20Publications/92.pdf

Flow boiling heat transfer in two-phase micro-channel heat sinks––I. Experimental investigation and assessment of correlation methods

Reference LTCM-ARTICLE-2005-021View record in Web of Science Record created on 2005-07-06, modified on 2017-05-10

Heat Transfer Model for Evaporation in Microchannels, Part I: Presentation of the Model

Two-phase flow in high-heat-flux micro-channel heat sink for refrigeration cooling applications: Part II—heat transfer characteristics

The forces due to surface tension and momentum change during evaporation, in conjunction with the forces due to viscous shear and inertia, govern the two-phase flow patterns and the heat transfer characteristics during flow boiling in microchannels. These forces are analyzed in this paper, and two new nondimensional groups, K1 and K2 , relevant to flow boiling phenomenon are derived. These groups are able to represent some of the key flow boiling characteristics, including the CHF. In addition, a mechanistic description of the flow boiling phenomenon is presented. The small hydraulic dimensions of microchannel flow passages present a large frictional pressure drop in single-phase and two-phase flows. The small hydraulic diameter also leads to low Reynolds numbers, in the range 100‐1000, or even lower for smaller diameter channels. Such low Reynolds numbers are rarely employed during flow boiling in conventional channels. In these low Reynolds number flows, nucleate boiling systematically emerges as the dominant mode of heat transfer. The high degree of wall superheat required to initiate nucleation in microchannels leads to rapid evaporation and flow instabilities, often resulting in flow reversal in multiple parallel channel configuration. Aided by strong evaporation rates, the bubbles nucleating on the wall grow rapidly and fill the entire channel. The contact line between the bubble base and the channel wall surface now becomes the entire perimeter at both ends of the vapor slug. Evaporation occurs at the moving contact line of the expanding vapor slug as well as over the channel wall covered with a thin evaporating film surrounding the vapor core. The usual nucleate boiling heat transfer mechanisms, including liquid film evaporation and transient heat conduction in the liquid adjacent to the contact line region, play an important role. The liquid film under the large vapor slug evaporates completely at downstream locations thus presenting a dryout condition periodically with the passage of each large vapor slug. The experimental data and high speed visual observations confirm some of the key features presented in this paper. @DOI: 10.1115/1.1643090#

Heat Transfer Mechanisms During Flow Boiling in Microchannels

https://ir.nctu.edu.tw:443/bitstream/11536/31710/1/000077189000011.pdf

Evaporation heat transfer and pressure drop of refrigerant R-134a in a small pipe

https://ir.nctu.edu.tw:443/bitstream/11536/31469/1/000078287400003.pdf

Condensation heat transfer and pressure drop of refrigerant R-134a in a plate heat exchanger

https://ir.nctu.edu.tw:443/bitstream/11536/28075/1/000180770600017.pdf

Yi-Yie Yan

Papers

Evaporation heat transfer and pressure drop of refrigerant R-134a in a small pipe

Condensation heat transfer and pressure drop of refrigerant R-134a in a plate heat exchanger

Reply to Prof. R.L. Webb’s and Dr. J.W. Paek’s comments