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Thermally Developing Flow and Heat Transfer in Rectangular Microchannels of Different Aspect Ratios

Poh Seng Lee, +1 more
- 01 Aug 2006 - 
- Vol. 49, Iss: 17, pp 3060-3067
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TLDR
In this paper, three-dimensional numerical simulations were performed for laminar thermally developing flow in microchannels of different aspect ratios, based on the temperature and heat flux distributions obtained, both the local and average Nusselt numbers were presented graphically as a function of the dimensionless axial distance and channel aspect ratio.
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This article is published in International Journal of Heat and Mass Transfer.The article was published on 2006-08-01 and is currently open access. It has received 399 citations till now. The article focuses on the topics: Nusselt number & Micro heat exchanger.

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Citations
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Journal ArticleDOI

Fluid flow and heat transfer in wavy microchannels

TL;DR: In this paper, Wang et al. used the Poincare section to analyze the fluid mixing in three-dimensional wavy microchannels with rectangular cross-sections and found that the quantity and the location of the vortices may change along the flow direction, leading to chaotic advection.
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History, Advances, and Challenges in Liquid Flow and Flow Boiling Heat Transfer in Microchannels: A Critical Review

TL;DR: In this paper, the authors provide a historical perspective of the progress made in understanding the underlying mechanisms in single-phase liquid flow and two-phase flow boiling processes and their use in high heat flux removal applications.
Journal ArticleDOI

An experimental study of flow friction and heat transfer in wavy microchannels with rectangular cross section

TL;DR: In this article, an experimental investigation has been conducted on the flow friction and heat transfer in sinusoidal microchannels with rectangular cross sections, and the experimental results, mainly the overall Nusselt number and friction factor, for wavy micro-channels are compared with those of straight baseline channels with the same cross section and footprint length.
Journal ArticleDOI

Review of micro- and mini-channel heat sinks and heat exchangers for single phase fluids

TL;DR: In this paper, a review of micro-and minichannel heat exchangers as heat sinks and heat exchanger has been presented, and the persisting lacunae of this technology drawn from the review have been pointed out.
Journal ArticleDOI

Saturated flow boiling heat transfer and pressure drop in silicon microchannel arrays

TL;DR: In this article, the authors investigated flow boiling in arrays of parallel microchannels using a silicon test piece with imbedded discrete heat sources and integrated local temperature sensors, and the experimental results allow a critical assessment of the applicability of existing models and correlations in predicting the heat transfer rates and pressure drops in microchannel arrays.
References
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Book

Convective Heat and Mass Transfer

TL;DR: In this article, the echangeurs de : chaleur, couche de : limite, modeles de : turbulence, transfert de masse reference record created on 2005-11-18, modified on 2016-08-08
Journal Article

Laminar Flow Forced convection in ducts

Book

Handbook of single-phase convective heat transfer

TL;DR: In this paper, the effect of temperature-dependent Fluid properties on convective heat transfer has been investigated in the context of closed-loop convection in Ducts and cross-flow convection over Rod Bundles.
Journal ArticleDOI

Experimental and numerical study of pressure drop and heat transfer in a single-phase micro-channel heat sink

TL;DR: In this paper, the authors investigated the pressure drop and heat transfer characteristics of a single-phase micro-channel heat sink, which consisted of an array of rectangular micro-channels 231 lm wide and 713 lm deep.
Frequently Asked Questions (12)
Q1. What have the authors contributed in "Thermally developing flow and heat transfer in rectangular microchannels of different aspect ratios" ?

In this paper, a three-dimensional numerical simulation was performed for laminar thermally developing flow in microchannels of different aspect ratios. 

Microchannel heat sinks are of particular interest due to the very high rates of heat transfer they enable in conjunction with greatly reduced heat sink length scales and coolant mass. 

Numerical simulations based on the finite volume method were conducted to predict steady, laminar heat transfer coefficients in hydrodynamically developed but thermally developing flow. 

The dimensionless thermal entrance length, * thz , defined as the distance required over which the localNusselt number, Nuz, drops to 1.05 times the fully developed value, Nu [11], can be determined from the results. 

They concluded that the H1 thermal boundary condition is the most appropriate for simplified analyses, when full conjugate analyses are not affordable. 

Svino and Siegel [13] investigated the effect of unequal heat addition on adjacent sides of rectangular channels and found that poor convection due to low velocities in the corners and along the narrow wall causes peak temperatures to occur at the corners. 

To simplify the full three-dimensional conjugate analysis, the computational domain has typically been restricted to include only the fluid region, with one of the following alternative thermal boundary conditions applied to the channel walls: H1 (circumferentially constant wall temperature and axially constant wall heat flux), H2 (uniform wall heat flux, both axially and circumferentially), and T (uniform wall temperature, both axially and circumferentially) [8]. 

As the flow is assumed to be hydrodynamically fully developed, the following exact analytical solution by Marco and Han [10] for the fully developed velocity profile in a rectangular duct is used as the inlet condition: 216 2 ( , , 0)21 / 2 1 cosh /1 cos 3 cosh / 21, 3, ...b dpu x y dzn n y b n xn a b bn n (2)in which the pressure gradient dp/dz is given in terms of the mean fluid velocity, um, by 25 51,3 ,...1 192 1 1 tanh 3 2 2 mndp b n a udz a n bb (3)Figure 2 shows such a fully developed velocity profile. 

This is reflected in the increase in local Nusselt number in the microchannel at a larger aspect ratio, since the relative importance of the narrow walls and corners diminishes with increasing aspect ratio. 

both these sets of results were limited to a smallrange of channel aspect ratios ( = 1 to 4), and were also restricted by the available computationalresources of the time. 

the results of such analyses can be generalized to microchannels of different dimensions, de-coupled from details of the substrate. 

The proposed correlations are easy to use, provide detailed heat transfer coefficient predictions in the entrance region of microchannels, and cover a wide parameter range.