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Mechanics of Fluids

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362 The flow <strong>of</strong> an inviscid fluid<br />

Fig. 9.1<br />

which the fluid flows. The average velocities across each face <strong>of</strong> the element<br />

are as shown. For an incompressible fluid, volume flow rate into the element<br />

equals volume flow rate out; thus for unit thickness perpendicular to the<br />

diagram<br />

uδy + vδx =<br />

�<br />

u + ∂u<br />

∂x δx<br />

� �<br />

δy + v + ∂v<br />

∂y δy<br />

�<br />

δx<br />

whence, as the size <strong>of</strong> the element becomes vanishingly small, we have in the<br />

limit the partial differential equation<br />

∂u ∂v<br />

+ = 0 (9.1)<br />

∂x ∂y<br />

9.2 THE STREAM FUNCTION<br />

Figure 9.2 illustrates two-dimensional plane flow. It is useful to imagine a<br />

transparent plane, parallel to the paper and unit distance away from it; the<br />

lines in the diagram should then be regarded as surfaces seen edge on, and<br />

the points as lines seen end on. A is a fixed point but P is any point in the<br />

plane. The points A and P are joined by the arbitrary lines AQP, ARP. For<br />

an incompressible fluid flowing across the region shown, the volume rate <strong>of</strong><br />

flow across AQP into the space AQPRA must equal that out across ARP.<br />

Whatever the shape <strong>of</strong> the curve ARP, the rate <strong>of</strong> flow across it is the same<br />

as that across AQP; in other words, the rate <strong>of</strong> flow across the curve ARP<br />

depends only on the end points A and P. Since A is fixed, the rate <strong>of</strong> flow<br />

across ARP is a function only <strong>of</strong> the position <strong>of</strong> P. This function is known as<br />

the stream function, ψ. The value <strong>of</strong> ψ at P therefore represents the volume<br />

flow rate across any line joining P to A at which point ψ is arbitrarily zero.<br />

(A may be at the origin <strong>of</strong> coordinates, but this is not necessary.)<br />

If a curve joining A to P ′ is considered (Fig. 9.3), PP ′ being along a streamline,<br />

then the rate <strong>of</strong> flow across AP ′ must be the same as across AP since,<br />

by the definition <strong>of</strong> a streamline, there is no flow across PP ′ . The value <strong>of</strong><br />

ψ is thus the same at P ′ as at P and, since P ′ was taken as any point on the<br />

streamline through P, it follows that ψ is constant along a streamline. Thus<br />

the flow may be represented by a series <strong>of</strong> streamlines at equal increments<br />

<strong>of</strong> ψ, like the contour lines on a map.

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