3.2-4. Metering Flow by a Venturi. A venturi meter having a throat diameter of 38.9 mm is installed in a line having an inside diameter of 102.3 mm. It meters water having a density of 999 kg/m. The measured pressure drop across the 206 Chap. 3 Problems venturi is 156.9 kPa. The venturi coefficient C, is 0.98. Calculate the gal/min and m'/s flow rate. Ans. 330 gal/min, 0.0208 m³/s

Introduction to Chemical Engineering Thermodynamics
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ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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3.2-4. Metering Flow by a Venturi. A venturi meter having a throat diameter of
38.9 mm is installed in a line having an inside diameter of 102.3 mm. It meters
water having a density of 999 kg/m³. The measured pressure drop across the
206
Chap. 3
Problems
venturi is 156.9 kPa. The venturi coefficient C, is 0.98. Calculate the gal/min and
m'/s flow rate.
Ans. 330 gal/min, 0.0208 m³/s
Transcribed Image Text:3.2-4. Metering Flow by a Venturi. A venturi meter having a throat diameter of 38.9 mm is installed in a line having an inside diameter of 102.3 mm. It meters water having a density of 999 kg/m³. The measured pressure drop across the 206 Chap. 3 Problems venturi is 156.9 kPa. The venturi coefficient C, is 0.98. Calculate the gal/min and m'/s flow rate. Ans. 330 gal/min, 0.0208 m³/s
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