Physics for Geologists, Second edition
Physics for Geologists, Second edition
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.