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CalibratePhysics

2.9

Bernoulli's Equation

Mechanical Properties of Fluids · Maharashtra HSC

Theory

Bernoulli's principle

On observing a river, the speed of the water decreases in a wide region and increases where the river is narrow. One might think that the pressure in the narrower region would be greater, but in fact the pressure within the fluid in the narrower part is less and that in the wider part is more. Daniel Bernoulli found that the speed of a fluid in a narrow region increases while its internal pressure in that region decreases. This is Bernoulli's principle.

Bernoulli's equation relates the speed of a fluid at a point, the pressure at that point, and the height of that point above a reference level. It is an application of the work–energy theorem to a fluid in flow, and is consistent with the principle of conservation of energy.

Diagram to draw

An ideal fluid flowing through a tube of varying cross section and varying height. Mark the lower end P and the upper end R. At P: area A1A_{1}, speed v1v_{1}, pressure P1P_{1}, height h1h_{1}, displacement d1d_{1} in time dtdt. At R: area A2A_{2}, speed v2v_{2}, pressure P2P_{2}, height h2h_{2}, displacement d2d_{2} in the same time. Show the forces P1A1P_{1}A_{1} pushing the element forward at P and P2A2P_{2}A_{2} opposing it at R. Q and S mark the intermediate cross sections after the displacements.

Derivation

The volume dVdV of fluid passing through any cross section during the time interval dtdt is the same:

dV=A1d1=A2d2dV = A_{1}d_{1} = A_{2}d_{2}

The fluid is ideal, so there is no internal friction, and the only non-gravitational force doing work on the fluid element is the pressure of the surrounding fluid. The net work done on the element from P to R is

W=P1A1d1−P2A2d2W = P_{1}A_{1}d_{1} - P_{2}A_{2}d_{2}

The second term is negative because the force at R opposes the displacement of the fluid. Using dV=A1d1=A2d2dV = A_{1}d_{1} = A_{2}d_{2},

W=(P1−P2) dVW = (P_{1} - P_{2})\,dV

Since WW is due to forces other than the conservative force of gravity, it equals the change in the total mechanical energy of the fluid element:

W=ΔK.E.+ΔP.E.W = \Delta \text{K.E.} + \Delta \text{P.E.}

The mechanical energy of the fluid between the sections Q and R does not change, so only the end portions matter.

Kinetic energy. At the beginning of dtdt the mass between P and Q is ρA1d1\rho A_{1}d_{1} and its kinetic energy is 12ρA1d1v12\dfrac{1}{2}\rho A_{1}d_{1}v_{1}^{2}. At the end of dtdt the kinetic energy of the fluid between R and S is 12ρA2d2v22\dfrac{1}{2}\rho A_{2}d_{2}v_{2}^{2}. Hence

ΔK.E.=12ρ dV v22−12ρ dV v12=12ρ dV(v22−v12)\Delta \text{K.E.} = \dfrac{1}{2}\rho\,dV\,v_{2}^{2} - \dfrac{1}{2}\rho\,dV\,v_{1}^{2} = \dfrac{1}{2}\rho\,dV\left(v_{2}^{2} - v_{1}^{2}\right)

Potential energy. At the beginning of dtdt the gravitational potential energy of the mass between P and Q is ρ dVgh1\rho\,dV g h_{1}, and at the end that of the mass between R and S is ρ dVgh2\rho\,dV g h_{2}. Hence

ΔP.E.=ρ dVg (h2−h1)\Delta \text{P.E.} = \rho\,dV g\,(h_{2} - h_{1})

Substituting the three results,

(P1−P2) dV=12ρ dV(v22−v12)+ρ dVg (h2−h1)(P_{1} - P_{2})\,dV = \dfrac{1}{2}\rho\,dV\left(v_{2}^{2} - v_{1}^{2}\right) + \rho\,dV g\,(h_{2} - h_{1})

P1−P2=12ρ(v22−v12)+ρg (h2−h1)P_{1} - P_{2} = \dfrac{1}{2}\rho\left(v_{2}^{2} - v_{1}^{2}\right) + \rho g\,(h_{2} - h_{1})

This is Bernoulli's equation. It states that the work done per unit volume of a fluid by the surrounding fluid is equal to the sum of the changes in kinetic and potential energies per unit volume that occur during the flow. Rearranged,

P1+12ρv12+ρgh1=P2+12ρv22+ρgh2P_{1} + \dfrac{1}{2}\rho v_{1}^{2} + \rho g h_{1} = P_{2} + \dfrac{1}{2}\rho v_{2}^{2} + \rho g h_{2}

P+12ρv2+ρgh=constantP + \dfrac{1}{2}\rho v^{2} + \rho g h = \text{constant}

Reading the equation

Dimensionally, pressure is energy per unit volume, and each of the three terms has that dimension. The term PP is called the pressure head, 12ρv2\dfrac{1}{2}\rho v^{2} the velocity head, and ρgh\rho g h the potential head. Bernoulli's principle is thus consistent with the principle of conservation of energy. For a fluid at rest, v1=v2=0v_{1} = v_{2} = 0 and the equation reduces to P1−P2=ρg(h2−h1)P_{1} - P_{2} = \rho g (h_{2} - h_{1}), the hydrostatic result.

Applications

a) Speed of efflux — Torricelli's law

Consider a liquid of density ρ\rho in a tank of large cross section A1A_{1} with an orifice of cross section A2A_{2} at the bottom, A2≪A1A_{2} \ll A_{1}, the free surface standing at a height hh above the orifice. Both the free surface and the orifice are exposed to the atmosphere, so the pressure at both is p0p_{0}. Bernoulli's equation gives

p0+12ρv12+ρgh=p0+12ρv22p_{0} + \dfrac{1}{2}\rho v_{1}^{2} + \rho g h = p_{0} + \dfrac{1}{2}\rho v_{2}^{2}

From the equation of continuity, v1=A2A1v2v_{1} = \dfrac{A_{2}}{A_{1}}v_{2}, so

v22[1−(A2A1)2]=2gh⟹v2=2gh1−(A2/A1)2v_{2}^{2}\left[1 - \left(\dfrac{A_{2}}{A_{1}}\right)^{2}\right] = 2gh \qquad\Longrightarrow\qquad v_{2} = \sqrt{\dfrac{2gh}{1 - \left(A_{2}/A_{1}\right)^{2}}}

If A2≪A1A_{2} \ll A_{1} this reduces to

v2=2ghv_{2} = \sqrt{2gh}

The speed of efflux is the same as that of a particle falling freely through the height hh under gravity. When the liquid is instead driven out by a gauge pressure pp inside a closed tank, the same argument gives v=2p/ρv = \sqrt{2p/\rho}.

b) Venturi tube

A venturi tube measures the speed of flow of a fluid in a tube. It has a constriction: as the fluid passes through it, the speed increases by the equation of continuity, and the pressure therefore decreases as required by Bernoulli's equation. Two vertical tubes are connected at the wide part (area A1A_{1}, speed v1v_{1}, pressure p1p_{1}) and at the constriction (area A2A_{2}, speed v2v_{2}, pressure p2p_{2}). For a horizontal tube,

p1+12ρv12=p2+12ρv22⟹p1−p2=12ρ(v22−v12)p_{1} + \dfrac{1}{2}\rho v_{1}^{2} = p_{2} + \dfrac{1}{2}\rho v_{2}^{2} \qquad\Longrightarrow\qquad p_{1} - p_{2} = \dfrac{1}{2}\rho\left(v_{2}^{2} - v_{1}^{2}\right)

If the difference in the liquid levels in the two vertical tubes is hh, then p1−p2=hρgp_{1} - p_{2} = h\rho g, and combining this with A1v1=A2v2A_{1}v_{1} = A_{2}v_{2} lets the rate of flow be calculated from the areas A1A_{1} and A2A_{2}. With a mercury manometer measuring the pressure difference in a water pipe, 12ρw(v22−v12)=hρHgg\dfrac{1}{2}\rho_{w}\left(v_{2}^{2} - v_{1}^{2}\right) = h\rho_{\text{Hg}}g.

c) Lifting up of an aeroplane

Because of the aerodynamic shape of the cross section of the wings, when the aeroplane runs on the runway the streamlines of air are crowded above the wings compared with those below. The air above the wings therefore moves faster than that below. By Bernoulli's principle the pressure above the wings decreases while that below does not change. This pressure difference produces an upward force on the bottom of the wings, called the dynamic lift; when it exceeds the weight of the aeroplane, the aeroplane takes off.

d) Working of an atomizer

The carburettor of an automobile engine, a paint gun, a scent spray and an insect sprayer all work on Bernoulli's principle. A tube T is dipped in the liquid, and air is blown at high speed over the tip of this tube by a piston P in a cylinder C. The high speed air creates a low pressure over the tube, so the liquid rises in it and is then blown off as very small droplets with the expelled air.

e) Blowing off of roofs by stormy wind

When a high speed stormy wind blows over a roof top it causes a low pressure pp above the roof, in accordance with Bernoulli's principle. The air below the roof, inside the room, is still at the atmospheric pressure p0p_{0}. Because of this pressure difference the roof is lifted up and is then blown off by the wind.

Standard results

  • P+12ρv2+ρgh=P + \dfrac{1}{2}\rho v^{2} + \rho g h = constant, for an ideal fluid in steady flow.
  • Horizontal pipe: p1−p2=12ρ(v22−v12)p_{1} - p_{2} = \dfrac{1}{2}\rho\left(v_{2}^{2} - v_{1}^{2}\right).
  • Torricelli: v=2ghv = \sqrt{2gh}; under a gauge pressure pp, v=2p/ρv = \sqrt{2p/\rho}.
  • Basis of Bernoulli's principle: conservation of energy (work–energy theorem applied to a fluid element).