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MechanicalFluid MechanicsmediumFE ExamCoursework

Pressure Drop Across a Venturi

Water (ρ=1000 kg/m3\rho = 1000\ \text{kg/m}^3) flows through a horizontal venturi meter.

The inlet diameter is D1=100 mmD_1 = 100\ \text{mm} and the throat diameter is D2=50 mmD_2 = 50\ \text{mm}. The inlet velocity is V1=2.0 m/sV_1 = 2.0\ \text{m/s}.

Neglecting losses, find the pressure drop P1P2P_1 - P_2 between the inlet and the throat.

Given
D1100 mmInlet diameter
D250 mmThroat diameter
V12 m/sInlet velocity
ρ1000 kg/m^3Water density
Hint 1

Two relations are needed: one to find the throat velocity, one to convert velocities into pressures.

Hint 2

Continuity relates velocity to area, and area goes as diameter squared.

Hint 3

Halving the diameter quarters the area, so the velocity quadruples — to 8 m/s.

Worked solution — try the problem first

Step 1 — Continuity gives the throat velocity.

A1V1=A2V2V2=V1A1A2=V1(D1D2)2A_1V_1 = A_2V_2 \quad \Longrightarrow \quad V_2 = V_1\frac{A_1}{A_2} = V_1\left(\frac{D_1}{D_2}\right)^2

The area ratio goes as the square of the diameter ratio:

V2=2.0×(10050)2=2.0×4=8.0 m/sV_2 = 2.0 \times \left(\frac{100}{50}\right)^2 = 2.0 \times 4 = 8.0\ \text{m/s}

Step 2 — Bernoulli between inlet and throat. The meter is horizontal, so the elevation terms cancel:

P1+12ρV12=P2+12ρV22P_1 + \tfrac{1}{2}\rho V_1^2 = P_2 + \tfrac{1}{2}\rho V_2^2

P1P2=12ρ(V22V12)=12(1000)(8.022.02)P_1 - P_2 = \tfrac{1}{2}\rho\left(V_2^2 - V_1^2\right) = \tfrac{1}{2}(1000)\left(8.0^2 - 2.0^2\right)

=500(644)=500×60=30,000 Pa= 500(64 - 4) = 500 \times 60 = 30{,}000\ \text{Pa}

P1P2=30 kPa\boxed{P_1 - P_2 = 30\ \text{kPa}}

The pressure falls at the throat because the fluid speeds up — that is the whole operating principle of the meter.

Concepts:Bernoulli equationContinuityVenturi meter

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