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Page Title: Application of Bernoulli’s Equation to a Venturi
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Application of Bernoulli’s Equation to a Venturi
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Thermodynamics Heat Transfer and Fluid Flow Volume 3 of 3
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Bernoulli’s Equation Summary

Fluid Flow BERNOULLI’S EQUATION Therefore the flow velocity at the throat of the venturi and the volumetric flow rate are directly proportional to the square root of the differential pressure. The  pressures  at  the  upstream  section  and  throat  are  actual  pressures,  and  velocities  from Bernoulli’s equation without a loss term are theoretical velocities.   When losses are considered in the energy equation, the velocities are actual velocities.  First, with the Bernoulli equation (that is,  without  a  head-loss  term),  the  theoretical  velocity  at  the  throat  is  obtained.     Then  by multiplying this by the venturi factor (Cv), which accounts for friction losses and equals 0.98 for most venturis, the actual velocity is obtained.   The actual velocity times the actual area of the throat determines the actual discharge volumetric flow rate. The pressure drop, P1-P2, across the venturi can be used to measure the flow rate using a U-tube manometer  as  shown  in  Figure  6.    The  reading,  R’,  of  the  manometer  is  proportional  to  the pressure drop and thus the velocity of the fluid. Rev. 0 Page 29 HT-03

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