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Mechanics of Fluids

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the junction, the curvature <strong>of</strong> the streamlines and the acceleration <strong>of</strong> the fluid<br />

cause the pressure at the annular face to vary in an unknown way. However,<br />

immediately downstream <strong>of</strong> the junction a vena contracta is formed, after<br />

which the stream widens again to fill the pipe. A region <strong>of</strong> separated flow is<br />

formed between the vena contracta and the wall <strong>of</strong> the pipe, and this causes<br />

practically all the dissipation <strong>of</strong> energy. Between the vena contracta plane<br />

and the downstream section 2 – where the velocity has again become sensibly<br />

uniform – the flow pattern is similar to that after an abrupt enlargement, and<br />

so the loss <strong>of</strong> head is assumed to be given by eqn 7.15:<br />

h l = u2 2<br />

2g<br />

� A2<br />

Ac<br />

− 1<br />

� 2<br />

= u2 2<br />

2g<br />

� 1<br />

Cc<br />

− 1<br />

� 2<br />

(7.16)<br />

where Ac represents the cross-sectional area <strong>of</strong> the vena contracta, and the<br />

coefficient <strong>of</strong> contraction Cc = Ac/A2.<br />

Although the area A1 is not explicitly involved in eqn 7.16, the value <strong>of</strong><br />

Cc depends on the ratio A2/A1. For coaxial circular pipes and fairly high<br />

Reynolds numbers Table 7.1 gives representative values <strong>of</strong> the coefficient k<br />

in the formula<br />

h l = ku2 2<br />

2g<br />

(7.17)<br />

Other losses in pipes 263<br />

Fig. 7.10<br />

As A1 → ∞ the value <strong>of</strong> k in eqn 7.17 tends to 0.5, and this limiting Entry loss<br />

case corresponds to the flow from a large reservoir into a sharp-edged pipe,<br />

provided that the end <strong>of</strong> the pipe does not protrude in to the reservoir (see<br />

Fig. 7.11a). A protruding pipe, as in Fig. 7.11b, causes a greater loss <strong>of</strong> head.<br />

For a non-protruding, sharp-edged pipe the loss 0.5u2 2 /2g is known as the<br />

entry loss. If the inlet to the pipe is well rounded, as in Fig. 7.11c, the fluid<br />

can follow the boundary without separating from it, and the entry loss is<br />

Table 7.1 Loss coefficient k for abrupt<br />

contraction<br />

d 2/d 1 0 0.2 0.4 0.6 0.8 1.0<br />

k 0.5 0.45 0.38 0.28 0.14 0

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