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6.9 Some Simple Solutions for Laminar, Viscous, Incompressible Fluids 315<br />

V6.14 Complex<br />

pipe flow<br />

and therefore<br />

Equation 6.148 for<br />

yield<br />

(6.149)<br />

can be substituted into Eq. 6.149, and the resulting equation integrated to<br />

(6.150)<br />

This relationship can be expressed in terms of the pressure drop, ¢p, which occurs over a length,<br />

/, along the tube, since<br />

and therefore<br />

v z<br />

R<br />

Q 2p v z r dr<br />

Q pR 4<br />

8m a 0p<br />

0z b<br />

0<br />

¢p<br />

/ 0p 0z<br />

Q pR 4 ¢p<br />

8m/<br />

(6.151)<br />

R<br />

Poiseuille’s law relates<br />

pressure drop<br />

and flowrate for<br />

steady, laminar flow<br />

in circular tubes.<br />

r<br />

v z<br />

v max<br />

= 1 – (<br />

r_<br />

R)<br />

2<br />

v max<br />

For a given pressure drop per unit length, the volume rate of flow is inversely proportional to the<br />

viscosity and proportional to the tube radius to the fourth power. A doubling of the tube radius<br />

produces a 16-fold increase in flow! Equation 6.151 is commonly called Poiseuille’s law.<br />

In terms of the mean velocity, V, where V QpR 2 , Eq. 6.151 becomes<br />

V R2 ¢p<br />

8m/<br />

The maximum velocity v max occurs at the center of the tube, where from Eq. 6.148<br />

so that<br />

v max R2<br />

4m a 0p<br />

0z b R2 ¢p<br />

4m/<br />

v max 2V<br />

The velocity distribution, as shown by the figure in the margin, can be written in terms of<br />

v z<br />

v max<br />

1 a r R b 2<br />

(6.152)<br />

(6.153)<br />

as<br />

(6.154)<br />

As was true for the similar case of flow between parallel plates 1sometimes referred to as<br />

plane Poiseuille flow2, a very detailed description of the pressure and velocity distribution in<br />

tube flow results from this solution to the Navier–Stokes equations. Numerous experiments<br />

performed to substantiate the theoretical results show that the theory and experiment are in<br />

agreement for the laminar flow of Newtonian <strong>fluid</strong>s in circular tubes or pipes. In general, the<br />

flow remains laminar for Reynolds numbers, Re rV12R2m, below 2100. Turbulent flow in<br />

tubes is considered in Chapter 8.<br />

v max<br />

F l u i d s i n t h e N e w s<br />

Poiseuille’s law revisited Poiseuille’s law governing laminar<br />

flow of <strong>fluid</strong>s in tubes has an unusual history. It was developed in<br />

1842 by a French physician, J. L. M. Poiseuille, who was interested<br />

in the flow of blood in capillaries. Poiseuille, through a<br />

series of carefully conducted experiments using water flowing<br />

through very small tubes, arrived at the formula, Q K¢p D 4 / .<br />

In this formula Q is the flowrate, K an empirical constant, ¢p the<br />

pressure drop over the length /, and D the tube diameter. Another<br />

formula was given for the value of K as a function of the water<br />

temperature. It was not until the concept of viscosity was introduced<br />

at a later date that Poiseuille’s law was derived mathematically<br />

and the constant K found to be equal to p8m,<br />

where<br />

m is the <strong>fluid</strong> viscosity. The experiments by Poiseuille have long<br />

been admired for their accuracy and completeness considering<br />

the laboratory instrumentation available in the mid nineteenth<br />

century.

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