Flow Measurement Worked Examples

Each problem states the calibration coefficient and measurement geometry it uses. Empirical constants are treated as model inputs rather than universal physical constants.

Problem 1: Discharge Through a Tank Orifice

A circular sharp-edged orifice has diameter 50.0 mm50.0\text{ mm}, calibrated discharge coefficient Cd=0.600C_d=0.600, and center 4.00 m4.00\text{ m} below a large reservoir free surface. Both free surface and jet are at atmospheric pressure. Determine discharge.

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Problem 2: Orifice Coefficients from Measured Jet Data

An orifice test gives theoretical jet velocity 10.0 m/s10.0\text{ m/s} and measured vena-contracta velocity 9.50 m/s9.50\text{ m/s}. The vena-contracta area is 60.0%60.0\% of the geometric orifice area. Determine CvC_v, CcC_c, and CdC_d using the definitions in this topic.

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Problem 3: Venturi Meter from Piezometric-Head Difference

A water Venturi has D1=200 mmD_1=200\text{ mm}, D2=100 mmD_2=100\text{ mm}, measured piezometric-head difference Δh=0.500 m\Delta h=0.500\text{ m} of water, and calibrated Cd=0.980C_d=0.980. Determine discharge.

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Problem 4: Venturi Meter with a Mercury Manometer

A horizontal Venturi carries water. D1=300 mmD_1=300\text{ mm}, D2=150 mmD_2=150\text{ mm}, Cd=0.980C_d=0.980, and a differential mercury manometer connecting equal-elevation taps reads y=0.120 my=0.120\text{ m}. Use SGHg=13.6SG_{\text{Hg}}=13.6. Determine discharge.

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Problem 5: Orifice Meter in a Pipe

A d=100 mmd=100\text{ mm} orifice plate is installed in a D=200 mmD=200\text{ mm} water pipe. The compatible pressure-tap measurement gives Δp=20.0 kPa\Delta p=20.0\text{ kPa} and the calibrated coefficient is Cd=0.620C_d=0.620. Determine discharge with the incompressible orifice-meter relation.

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Problem 6: Pitot-Static Local Velocity

A calibrated Pitot-static tube in water measures stagnation-minus-static pressure Δp=5.00 kPa\Delta p=5.00\text{ kPa}. Use probe coefficient C=0.980C=0.980 and ρ=1000 kg/m3\rho=1000\text{ kg/m}^3. Determine the local velocity.

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Problem 7: Suppressed Rectangular Sharp-Crested Weir

A free, ventilated suppressed rectangular weir is L=1.50 mL=1.50\text{ m} wide with measured head H=0.300 mH=0.300\text{ m}. Use Cd=0.620C_d=0.620 in the general rectangular-weir equation. Determine discharge.

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Problem 8: Contracted Francis Weir

A free sharp-crested rectangular weir has physical crest length L=1.50 mL=1.50\text{ m}, two effective end contractions, and measured head H=0.200 mH=0.200\text{ m}. Use the stated SI Francis form Q=1.84(L−0.2H)H3/2Q=1.84(L-0.2H)H^{3/2}. Determine effective length and discharge.

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Problem 9: 90-Degree V-Notch Weir

A free, ventilated 90∘90^\circ V-notch has head H=0.250 mH=0.250\text{ m} and an applicable coefficient Cd=0.600C_d=0.600. Determine discharge from the general triangular-weir relation.

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Problem 10: Cipolletti Head for a Target Discharge

A free-flow Cipolletti weir has bottom crest length L=2.50 mL=2.50\text{ m}. Using the stated SI empirical relation Q=1.86LH3/2Q=1.86LH^{3/2}, determine the head required for Q=1.00 m3/sQ=1.00\text{ m}^3/\text{s}.

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Problem 11: Velocity-Area Measurement in a Channel

A 6.00 m6.00\text{ m} wide channel is divided into five equal 1.20 m1.20\text{ m} subsections. Representative depths are 0.8000.800, 1.201.20, 1.501.50, 1.101.10, and 0.700 m0.700\text{ m}; corresponding representative mean velocities are 0.6000.600, 0.8000.800, 1.001.00, 0.7500.750, and 0.500 m/s0.500\text{ m/s}. Estimate discharge with the midsection-style area summation.

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