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Q2) Tank A distributes water with a kinematic viscosity of 1.13 x 10-6 m²/s to gauge B as shown in Figure below at a rate of 0.1 m³/s. If the pipe is 150 mm wrought iron, compute (1) the energy loss due to friction in pipe and (2) minor energy losses and (3) total energy losses. 25 m air P2140kPa gauge K-0.9 295m K- B 300 m K-0.9 150 m

Q2) Tank A distributes water with a kinematic viscosity of 1.13 x 10-6 m²/s to gauge B as shown in Figure below at a rate of 0.1 m³/s. If the pipe is 150 mm wrought iron, compute (1) the energy loss due to friction in pipe and (2) minor energy losses and (3) total energy losses. 25 m air P2140kPa gauge K-0.9 295m K- B 300 m K-0.9 150 m

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Q2) Tank A distributes water with a kinematic viscosity of 1.13 x 10-6 m²/s to gauge B as shown in Figure below at a rate of 0.1 m³/s. If the pipe is 150 mm wrought iron, compute (1) the energy loss due to friction in pipe and (2) minor energy losses and (3) total energy losses. 25 m air P2140kPa gauge K-0.9 295m K- B 300 m K-0.9 150 m
Transcribed Image Text:Q2) Tank A distributes water with a kinematic viscosity of 1.13 x 10-6 m²/s to gauge B as shown in Figure below at a rate of 0.1 m³/s. If the pipe is 150 mm wrought iron, compute (1) the energy loss due to friction in pipe and (2) minor energy losses and (3) total energy losses. 25 m air P2140kPa gauge K-0.9 295m K- B 300 m K-0.9 150 m
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