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Transport Phenomena.pdf

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Chapter 1<br />

Viscosity and the Mechanisms<br />

of Momentum <strong>Transport</strong><br />

§1.1 Newton's law of viscosity (molecular momentum transport)<br />

§1.2 Generalization of Newton's law of viscosity<br />

§1.3 Pressure and temperature dependence of viscosity<br />

§1.4° Molecular theory of the viscosity of gases at low density<br />

§1.5° Molecular theory of the viscosity of liquids<br />

§1.6° Viscosity of suspensions and emulsions<br />

§1.7 Convective momentum transport<br />

The first part of this book deals with the flow of viscous fluids. For fluids of low molecular<br />

weight, the physical property that characterizes the resistance to flow is the viscosity.<br />

Anyone who has bought motor oil is aware of the fact that some oils are more "viscous"<br />

than others and that viscosity is a function of the temperature.<br />

We begin in §1.1 with the simple shear flow between parallel plates and discuss how<br />

momentum is transferred through the fluid by viscous action. This is an elementary example<br />

of molecular momentum transport and it serves to introduce "Newton's law of viscosity"<br />

along with the definition of viscosity /л. Next in §1.2 we show how Newton's law<br />

can be generalized for arbitrary flow patterns. The effects of temperature and pressure<br />

on the viscosities of gases and liquids are summarized in §1.3 by means of a dimensionless<br />

plot. Then §1.4 tells how the viscosities of gases can be calculated from the kinetic<br />

theory of gases, and in §1.5 a similar discussion is given for liquids. In §1.6 we make a<br />

few comments about the viscosity of suspensions and emulsions.<br />

Finally, we show in §1.7 that momentum can also be transferred by the bulk fluid<br />

motion and that such convective momentum transport is proportional to the fluid density p.<br />

§1.1 NEWTON'S LAW OF VISCOSITY (MOLECULAR<br />

TRANSPORT OF MOMENTUM)<br />

In Fig. 1.1-1 we show a pair of large parallel plates, each one with area A, separated by a<br />

distance У. In the space between them is a fluid—either a gas or a liquid. This system is<br />

initially at rest, but at time t = 0 the lower plate is set in motion in the positive x direction<br />

at a constant velocity V. As time proceeds, the fluid gains momentum, and ultimately<br />

the linear steady-state velocity profile shown in the figure is established. We<br />

require that the flow be laminar ("laminar" flow is the orderly type of flow that one usually<br />

observes when syrup is poured, in contrast to "turbulent" flow, which is the irregular,<br />

chaotic flow one sees in a high-speed mixer). When the final state of steady motion<br />

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