In order to describe the motion of a fluid, in principle one might apply Newton’s laws to a particle (a small volume element of fluid) and follow its progress in time. This is a difficult approach. Instead, we consider the properties of the fluid, such as velocity and pressure, at fixed points in space.
In order to simplify the discussion we make several assumptions:
There is no dissipation of energy due to internal friction between adjacent layer in the fluid.
The velocity and pressure at each point are constant in time
A tiny paddle wheel placed in the liquid will not rotate.
In rotational flow, for example, in eddies, the fluid has net angular momentum about a given point.
In general, the velocity of a particle will not be constant along a streamline. The density and the cross-sectional area of a tube of flow will also change. Consider two sections of a tube of flow, as shown in figure(12.28). The mass of fluid contained in a small cylinder of length Δl1 and area A1 is Δm1 = ρ1A1Δl1. |
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Since fluid does not leave the tube of flow, this mass will later pass through a cylinder of length Δl2 and area A2. The mass in this cylinder is Δm2 = ρ2A2Δl2. The lengths Δl1 and Δl2 are related to the speeds at the respective locations: Δl1 = v1Δt and Δl2 = v2Δt. Since no mass is lost or gained.
Δm 1 = Δm 2 , and
ρ1A 1 v 1 = ρ 2 A 2 v 2 (12.28)
This is called the equation of continuity. It is a statement of the conservation of mass.
If the fluid is incompressible, its density remains unchanged. This is a good approximation for liquid, but not for gases. If ρ1 = ρ2, the equation (12.28) becomes,
A 1 v 1 = A 1 v 2 (12.29)
The product Av is the volume rate of flow (m3/s). Figure(12.29) shows a pipe whose cross section narrows. From equation (12.29) we conclude that the speed of a fluid is greatest where the cross-sectional area is the least. Notice that the streamlines are close together where the speed is higher.