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Heat transfer coefficient measurement of LN2 and GN2 in a microchannel at low Reynolds flow.

Published

Author(s)

Seungwhan Baek, Peter E. Bradley, Ray Radebaugh

Abstract

The heat transfer coefficients of single-phase fluids in the laminar flow regime have been studied for decades. However, inconsistent results are found in the literature. The common finding is that the Nusselt number is dependent on the Reynolds number in the laminar flow regime, which is contrary to laminar flow heat transfer theory. Recently, researchers indicated that axial conduction in the wall of the microchannel can affect the measurement. However, there have not been thorough studies that demonstrate consistency or lack thereof between experiment and theory. This study provides an experimental investigation on heat transfer performance of gaseous and liquid nitrogen flow through microchannels with hydraulic diameters of 110 μm and 180 μm. A model has been developed to investigate heat transfer in a microchannel from which analysis shows that the temperature profile of the fluid and wall change non-linearly along the length of the microchannel when the flow rate is low (e.g., Re
Citation
International Journal of Heat and Mass Transfer
Volume
127

Keywords

heat transfer coefficient, microchannel, axial conduction, single-phase, laminar flow, micro-scale
Created July 30, 2018, Updated September 25, 2018