fluid_mechanics
110 Chapter 3 ■ Elementary Fluid Dynamics—The Bernoulli Equation 3.6 Examples of Use of the Bernoulli Equation In this section we illustrate various additional applications of the Bernoulli equation. Between any two points, 112 and 122, on a streamline in steady, inviscid, incompressible flow the Bernoulli equation can be applied in the form p 1 1 2rV 2 1 gz 1 p 2 1 2rV 2 2 gz 2 (3.17) Obviously if five of the six variables are known, the remaining one can be determined. In many instances it is necessary to introduce other equations, such as the conservation of mass. Such considerations will be discussed briefly in this section and in more detail in Chapter 5. V The exit pressure for an incompressible fluid jet is equal to the surrounding pressure. 3.6.1 Free Jets One of the oldest equations in fluid mechanics deals with the flow of a liquid from a large reservoir. A modern version of this type of flow involves the flow of coffee from a coffee urn as indicated by the figure in the margin. The basic principles of this type of flow are shown in Fig. 3.11 where a jet of liquid of diameter d flows from the nozzle with velocity V. 1A nozzle is a device shaped to accelerate a fluid.2 Application of Eq. 3.17 between points 112 and 122 on the streamline shown gives gh 1 2rV 2 We have used the facts that z 1 h, z 2 0, the reservoir is large 1V 1 02 and open to the atmosphere 1 p 1 0 gage2, and the fluid leaves as a “free jet” 1 p 2 02. Thus, we obtain V B 2 gh r 12gh (3.18) which is the modern version of a result obtained in 1643 by Torricelli 11608–16472, an Italian physicist. The fact that the exit pressure equals the surrounding pressure 1 p 2 02 can be seen by applying F ma, as given by Eq. 3.14, across the streamlines between 122 and 142. If the streamlines at the tip of the nozzle are straight 1r 2, it follows that p 2 p 4 . Since 142 is on the surface of the jet, in contact with the atmosphere, we have p 4 0. Thus, p 2 0 also. Since 122 is an arbitrary point in the exit plane of the nozzle, it follows that the pressure is atmospheric across this plane. Physically, since there is no component of the weight force or acceleration in the normal 1horizontal2 direction, the pressure is constant in that direction. Once outside the nozzle, the stream continues to fall as a free jet with zero pressure throughout 1 p 5 02 and as seen by applying Eq. 3.17 between points 112 and 152, the speed increases according to V 12g 1h H2 where H is the distance the fluid has fallen outside the nozzle. Equation 3.18 could also be obtained by writing the Bernoulli equation between points 132 and 142 using the fact that z 4 0, z 3 /. Also, V 3 0 since it is far from the nozzle, and from hydrostatics, p 3 g1h /2. (1) V3.9 Flow from a tank h d (2) (3) z (2) (4) H (5) V F I G U R E 3.11 Vertical flow from a tank.
3.6 Examples of Use of the Bernoulli Equation 111 h (1) d h (2) (3) d h (2) (1) a d j d (3) a (a) (b) F I G U R E 3.12 Horizontal flow from a tank. F I G U R E 3.13 Vena contracta effect for a sharp-edged orifice. h V = 0 V = 2gh (1) V = √2gh The diameter of a fluid jet is often smaller than that of the hole from which it flows. h (2) As learned in physics or dynamics and illustrated in the figure in the margin, any object dropped from rest that falls through a distance h in a vacuum will obtain the speed V 12gh, the same as the water leaving the spout of the watering can shown in the figure in the margin. This is consistent with the fact that all of the particle’s potential energy is converted to kinetic energy, provided viscous 1friction2 effects are negligible. In terms of heads, the elevation head at point 112 is converted into the velocity head at point 122. Recall that for the case shown in Fig. 3.11 the pressure is the same 1atmospheric2 at points 112 and 122. For the horizontal nozzle of Fig. 3.12a, the velocity of the fluid at the centerline, V 2 , will be slightly greater than that at the top, V 1 , and slightly less than that at the bottom, V 3 , due to the differences in elevation. In general, d h as shown in Fig. 3.12b and we can safely use the centerline velocity as a reasonable “average velocity.” If the exit is not a smooth, well-contoured nozzle, but rather a flat plate as shown in Fig. 3.13, the diameter of the jet, d j , will be less than the diameter of the hole, d h . This phenomenon, called a vena contracta effect, is a result of the inability of the fluid to turn the sharp 90° corner indicated by the dotted lines in the figure. Since the streamlines in the exit plane are curved 1r 6 2, the pressure across them is not constant. It would take an infinite pressure gradient across the streamlines to cause the fluid to turn a “sharp” corner 1r 02. The highest pressure occurs along the centerline at 122 and the lowest pressure, p 1 p 3 0, is at the edge of the jet. Thus, the assumption of uniform velocity with straight streamlines and constant pressure is not valid at the exit plane. It is valid, however, in the plane of the vena contracta, section a–a. The uniform velocity assumption is valid at this section provided d j h, as is discussed for the flow from the nozzle shown in Fig. 3.12. The vena contracta effect is a function of the geometry of the outlet. Some typical configurations are shown in Fig. 3.14 along with typical values of the experimentally obtained contraction coefficient, C c A jA h , where A j and A h are the areas of the jet at the vena contracta and the area of the hole, respectively. F l u i d s i n t h e N e w s Cotton candy, glass wool, and steel wool Although cotton candy and glass wool insulation are made of entirely different materials and have entirely different uses, they are made by similar processes. Cotton candy, invented in 1897, consists of sugar fibers. Glass wool, invented in 1938, consists of glass fibers. In a cotton candy machine, sugar is melted and then forced by centrifugal action to flow through numerous tiny orifices in a spinning “bowl.” Upon emerging, the thin streams of liquid sugar cool very quickly and become solid threads that are collected on a stick or cone. Making glass wool insulation is somewhat more complex, but the basic process is similar. Liquid glass is forced through tiny orifices and emerges as very fine glass streams that quickly solidify. The resulting intertwined flexible fibers, glass wool, form an effective insulation material because the tiny air “cavities” between the fibers inhibit air motion. Although steel wool looks similar to cotton candy or glass wool, it is made by an entirely different process. Solid steel wires are drawn over special cutting blades which have grooves cut into them so that long, thin threads of steel are peeled off to form the matted steel wool.
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3.6 Examples of Use of the Bernoulli Equation 111<br />
h<br />
(1)<br />
d<br />
h<br />
(2)<br />
(3)<br />
d h<br />
(2)<br />
(1)<br />
a<br />
d j<br />
d<br />
(3)<br />
a<br />
(a)<br />
(b)<br />
F I G U R E 3.12 Horizontal flow from a tank. F I G U R E 3.13 Vena<br />
contracta effect for a sharp-edged orifice.<br />
h<br />
V = 0<br />
V = 2gh<br />
(1)<br />
V = √2gh<br />
The diameter of a<br />
<strong>fluid</strong> jet is often<br />
smaller than that of<br />
the hole from<br />
which it flows.<br />
h<br />
(2)<br />
As learned in physics or dynamics and illustrated in the figure in the margin, any object<br />
dropped from rest that falls through a distance h in a vacuum will obtain the speed V 12gh,<br />
the same as the water leaving the spout of the watering can shown in the figure in the margin. This<br />
is consistent with the fact that all of the particle’s potential energy is converted to kinetic energy,<br />
provided viscous 1friction2 effects are negligible. In terms of heads, the elevation head at point 112<br />
is converted into the velocity head at point 122. Recall that for the case shown in Fig. 3.11 the pressure<br />
is the same 1atmospheric2 at points 112 and 122.<br />
For the horizontal nozzle of Fig. 3.12a, the velocity of the <strong>fluid</strong> at the centerline, V 2 , will be<br />
slightly greater than that at the top, V 1 , and slightly less than that at the bottom, V 3 , due to the differences<br />
in elevation. In general, d h as shown in Fig. 3.12b and we can safely use the centerline<br />
velocity as a reasonable “average velocity.”<br />
If the exit is not a smooth, well-contoured nozzle, but rather a flat plate as shown in Fig. 3.13,<br />
the diameter of the jet, d j , will be less than the diameter of the hole, d h . This phenomenon, called<br />
a vena contracta effect, is a result of the inability of the <strong>fluid</strong> to turn the sharp 90° corner indicated<br />
by the dotted lines in the figure.<br />
Since the streamlines in the exit plane are curved 1r 6 2, the pressure across them is<br />
not constant. It would take an infinite pressure gradient across the streamlines to cause the<br />
<strong>fluid</strong> to turn a “sharp” corner 1r 02. The highest pressure occurs along the centerline at 122<br />
and the lowest pressure, p 1 p 3 0, is at the edge of the jet. Thus, the assumption of uniform<br />
velocity with straight streamlines and constant pressure is not valid at the exit plane. It<br />
is valid, however, in the plane of the vena contracta, section a–a. The uniform velocity assumption<br />
is valid at this section provided d j h, as is discussed for the flow from the nozzle<br />
shown in Fig. 3.12.<br />
The vena contracta effect is a function of the geometry of the outlet. Some typical configurations<br />
are shown in Fig. 3.14 along with typical values of the experimentally obtained contraction<br />
coefficient, C c A jA h , where A j and A h are the areas of the jet at the vena contracta and the<br />
area of the hole, respectively.<br />
F l u i d s i n t h e N e w s<br />
Cotton candy, glass wool, and steel wool Although cotton candy<br />
and glass wool insulation are made of entirely different materials<br />
and have entirely different uses, they are made by similar processes.<br />
Cotton candy, invented in 1897, consists of sugar fibers. Glass wool,<br />
invented in 1938, consists of glass fibers. In a cotton candy machine,<br />
sugar is melted and then forced by centrifugal action to flow through<br />
numerous tiny orifices in a spinning “bowl.” Upon emerging, the<br />
thin streams of liquid sugar cool very quickly and become solid<br />
threads that are collected on a stick or cone. Making glass wool insulation<br />
is somewhat more complex, but the basic process is similar.<br />
Liquid glass is forced through tiny orifices and emerges as very fine<br />
glass streams that quickly solidify. The resulting intertwined flexible<br />
fibers, glass wool, form an effective insulation material because the<br />
tiny air “cavities” between the fibers inhibit air motion. Although<br />
steel wool looks similar to cotton candy or glass wool, it is made by<br />
an entirely different process. Solid steel wires are drawn over special<br />
cutting blades which have grooves cut into them so that long, thin<br />
threads of steel are peeled off to form the matted steel wool.