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Book ChapterDOI

Heat transfer to newtonian and non-newtonian fluids in rectangular ducts

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TLDR
In this paper, the authors provide an overview of the analytical and experimental hydrodynamics and heat transfer studies of Newtonian and non-Newtonian fluids in laminar and turbulent flow through rectangular tubes.
Abstract
Publisher Summary This chapter provides an overview of the analytical and experimental hydrodynamics and heat transfer studies of Newtonian and non-Newtonian fluids in laminar and turbulent flow through rectangular tubes. The chapter in particular focuses on the rectangular duct geometry, with emphasis on the friction factor and heat transfer behavior of non-Newtonian fluids. It is recognized that non-Newtonian behavior is generally more complicated than Newtonian flow. In the case of non-Newtonian fluids, the theoretical predictions yield low estimates of the heat transfer under laminar flow conditions. The fact that the available experimental heat transfer measurements lie above the predictions could reflect an inadequacy in the analytical model. For non-Newtonians in turbulent flow through rectangular channels, the situation is even more complicated. Some non-Newtonian fluids act as pseudoplastics, showing some reduction in friction and heat transfer as compared with a Newtonian fluid. Other non-Newtonian fluids experience large reductions in the friction factor and in heat transfer under turbulent flow conditions.

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Citations
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Journal ArticleDOI

Pressure drop correlations for two-phase flow within horizontal rectangular channels with small heights

TL;DR: In this article, the two-phase frictional multiplier was expressed using the Lockhart-Martinelli type correlation but with the modification on parameter C. The correlations with the modified C successfully cover wide ranges of the Martinelli parameter (X=0.303-79.4) and the all-liquid Reynolds number (ReLo=175-17700) based on the hydraulic diameter within the deviation of ±10%.
Journal ArticleDOI

Heat transfer correlation for boiling flows in small rectangular horizontal channels with low aspect ratios

TL;DR: In this paper, a correlation is proposed to represent the heat transfer coefficients of the boiling flows through horizontal rectangular channels with low aspect ratios, where the gap between the upper and lower plates of each channel ranges from 0.4 to 2 mm.
Journal ArticleDOI

Correlation for flow boiling heat transfer in mini-channels

TL;DR: In this paper, the Chen correlation has been modified to be used for four flow conditions such as liquid-laminar and gas-turbulent one often occurring in mini-channels.
Book ChapterDOI

Non-Newtonian fluid heat transfer in porous media

TL;DR: In this paper, a review of the literature on non-Newtonian-fluid heat transfer in porous media is presented, with a focus on boundary layer and confined flows.
Journal ArticleDOI

Determination of shear viscosity and shear rate from pressure drop and flow rate relationship in a rectangular channel

TL;DR: In this paper, the authors presented a unique approach to calculate the shear viscosity and shear rate with the pressure drop and flow rate data from a channel having a rectangular cross-section with a height-to-width ratio (H/W) of close to one.
References
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Book

Boundary layer theory

TL;DR: The flow laws of the actual flows at high Reynolds numbers differ considerably from those of the laminar flows treated in the preceding part, denoted as turbulence as discussed by the authors, and the actual flow is very different from that of the Poiseuille flow.
Book

Heat Transfer

J. P. Holman
Journal ArticleDOI

A calculation procedure for heat, mass and momentum transfer in three-dimensional parabolic flows

TL;DR: In this article, a general, numerical, marching procedure is presented for the calculation of the transport processes in three-dimensional flows characterised by the presence of one coordinate in which physical influences are exerted in only one direction.
Journal Article

Laminar Flow Forced convection in ducts