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7.58. A venturi meter is a device to measure fluid flow rates, which in its operation resembles the orifice meter (Section 3.2b). It consists of a tapered constriction in a line, with pressure taps leading to a differential manometer at points upstream of the constriction and at the point of maximum constriction (the throat). The manometer reading is directly related to the flow rate in the line. Adapted from a problem centributed by Justin Wood of North Carolina State University. Problems 399 Suppose the flow rate of an incompressible fluid is to be measured in a venturi meter in which the cross-sectional area at point 1 is four times that at point 2. (a) Derive the relationship between the velocities u and u2 at points 1 and 2. (b) Write the Bernoulli equation for the system between points 1 and 2, and use it to prove that to the extenſ friction is negligible 15 pv 24 where P and P2 are the pressures at point 1 and 2, p and V are the density and volumetric flow rate P - P2 = of the flowing fluid, and A, is the cross-sectional area of the pipe at point 1. (c) Suppose this meter is used to measure the flow rate of a stream of acetone, using mercury as the manometer fluid, and a manometer reading h = 38 cm is recorded. What is the volumetric flow rate of the acetone if the pipe diameter at point 1 is 15 cm? (Recall the differential manometer equation, %3D Equation 3,4-6.)

7.58. A venturi meter is a device to measure fluid flow rates, which in its operation resembles the orifice meter (Section 3.2b). It consists of a tapered constriction in a line, with pressure taps leading to a differential manometer at points upstream of the constriction and at the point of maximum constriction (the throat). The manometer reading is directly related to the flow rate in the line. Adapted from a problem centributed by Justin Wood of North Carolina State University. Problems 399 Suppose the flow rate of an incompressible fluid is to be measured in a venturi meter in which the cross-sectional area at point 1 is four times that at point 2. (a) Derive the relationship between the velocities u and u2 at points 1 and 2. (b) Write the Bernoulli equation for the system between points 1 and 2, and use it to prove that to the extenſ friction is negligible 15 pv 24 where P and P2 are the pressures at point 1 and 2, p and V are the density and volumetric flow rate P - P2 = of the flowing fluid, and A, is the cross-sectional area of the pipe at point 1. (c) Suppose this meter is used to measure the flow rate of a stream of acetone, using mercury as the manometer fluid, and a manometer reading h = 38 cm is recorded. What is the volumetric flow rate of the acetone if the pipe diameter at point 1 is 15 cm? (Recall the differential manometer equation, %3D Equation 3,4-6.)

Elements Of Electromagnetics
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
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7.58. A venturi meter is a device to measure fluid flow rates, which in its operation resembles the orifice meter (Section 3.2b). It consists of a tapered constriction in a line, with pressure taps leading to a differential manometer at points upstream of the constriction and at the point of maximum constriction (the throat). The manometer reading is directly related to the flow rate in the line. oment Encyclopedla tial pressure flowmeters/ venturi tube lley.com/college/felder * Adapted from a problem centributed by Justin Wood of North Carolina State University. Problems 399 Suppose the flow rate of an incompressible fluid is to be measured in a venturi meter in which the cross-sectional area at point 1 is four times that at point 2. (a) Derive the relationship between the velocities u¡ and u2 at points 1 and 2. (b) Write the Bernoulli equation for the system between points 1 and 2, and use it to prove that to the extenT friction is negligible 15 pv P - P2 = 247 where Pi and P2 are the pressures at point 1 and 2, p and V are the density and volumetric flow rate of the flowing fluid, and A is the cross-sectional area of the pipe at point 1. (c) Suppose this meter is used to measure the flow rate of a stream of acetone, using mercury as the manometer fluid, and a manometer reading h = 38 cm is recorded. What is the volumetric flow rate of the acetone if the pipe diameter at point 1 is 15 cm? (Recall the differential manometer equation, Equation 3,4-6.)
Transcribed Image Text:7.58. A venturi meter is a device to measure fluid flow rates, which in its operation resembles the orifice meter (Section 3.2b). It consists of a tapered constriction in a line, with pressure taps leading to a differential manometer at points upstream of the constriction and at the point of maximum constriction (the throat). The manometer reading is directly related to the flow rate in the line. oment Encyclopedla tial pressure flowmeters/ venturi tube lley.com/college/felder * Adapted from a problem centributed by Justin Wood of North Carolina State University. Problems 399 Suppose the flow rate of an incompressible fluid is to be measured in a venturi meter in which the cross-sectional area at point 1 is four times that at point 2. (a) Derive the relationship between the velocities u¡ and u2 at points 1 and 2. (b) Write the Bernoulli equation for the system between points 1 and 2, and use it to prove that to the extenT friction is negligible 15 pv P - P2 = 247 where Pi and P2 are the pressures at point 1 and 2, p and V are the density and volumetric flow rate of the flowing fluid, and A is the cross-sectional area of the pipe at point 1. (c) Suppose this meter is used to measure the flow rate of a stream of acetone, using mercury as the manometer fluid, and a manometer reading h = 38 cm is recorded. What is the volumetric flow rate of the acetone if the pipe diameter at point 1 is 15 cm? (Recall the differential manometer equation, Equation 3,4-6.)
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