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Physics for Geologists, Second edition

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Fluids and fluid flow 123<br />

ardentes, as happened on Mount PelCe in Martinique, West Indies, in May<br />

1902 with the destruction of the town of St Pierre and all but one or two of<br />

the town's 30 000 inhabitants.<br />

When solids are suspended in a fluid, that fluid acquires a greater bulk<br />

density, and so tends to move to the most stable position it can reach, min-<br />

imizing the potential energy of the system. Snow avalanches and turbidity<br />

currents are similar.<br />

Bernoulli's theorem<br />

Water can be regarded <strong>for</strong> practical purposes as incompressible over the<br />

pressure changes that may take place in relatively short distances and with<br />

slow movement. Daniel Bernoulli (1700-82, of Switzerland) used this and<br />

the principle of conservation of energy to <strong>for</strong>mulate an energy balance.<br />

Consider an ideal liquid flowing through a pipe of decreasing diameter<br />

(Figure 12.6). The work done on the liquid in the pipe is equal to the change<br />

of energy of the liquid. At station 1, the <strong>for</strong>ce applied to the liquid is equal<br />

to plA1, where p is the pressure and A is the area normal to the flow; and<br />

in moving the liquid a small distance 611 in the small interval of time St,<br />

the work done is equal to p1A1811. Likewise, the work done at station 2 is<br />

p2A2812. The weight of liquid passing station 1 during the interval of time<br />

6t is pgA1611; and the same weight of liquid leaves station 2.<br />

The potential energy Ep per unit of mass entering at station 1 is gzl, so the<br />

potential energy of unit weight is zl and the potential energy of the liquid<br />

entering at station 1 is pgA1611z1, and that leaving at station 2 is pgA2612z2.<br />

The kinetic energy Ek per unit of weight is q2/2g, where q is the volu-<br />

metric flow rate; so the kinetic energy of the liquid entering at station 1 is<br />

pg~1611q:/2g; and that leaving at station 2 is pg~2612qi/2g.<br />

Copyright 2002 by Richard E. Chapman<br />

Figure 12.6 Bernoulli's theorem relates the energy changes in flow through a<br />

converging tube. The three terms in Equation 12.8 are the three<br />

'heads' - pressure head, elevation head and velocity head (which is<br />

ignored) - illustrated in Figure 12.7.

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