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(i) The velocities before and after the pump. (ii) The head supplied by the pump. (iii) The power supplied by the pump.

(i) The velocities before and after the pump. (ii) The head supplied by the pump. (iii) The power supplied by the pump.

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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● Oil with a specific gravity (SG) of 0.88 flows in an inclined pipe at a rate of 0.14 m³ s-1 as shown in the figure below. The diameter of the pipe at the inlet of the pump is 30 mm and at the exit 150 mm. If the differential reading in the mercury (Hg) manometer is 1 m and losses due to friction are negligible, calculate the following: ● 300mm Additional information: (ii) The head supplied by the pump. h (i) The velocities before and after the pump. (iii) The power supplied by the pump. Specific gravity of mercury Density of water Gravitational acceleration Pump H 1m S.G. = 13.6 p = 1000 kg m-³ g= 9.81 m s-² 150mm
Transcribed Image Text:● Oil with a specific gravity (SG) of 0.88 flows in an inclined pipe at a rate of 0.14 m³ s-1 as shown in the figure below. The diameter of the pipe at the inlet of the pump is 30 mm and at the exit 150 mm. If the differential reading in the mercury (Hg) manometer is 1 m and losses due to friction are negligible, calculate the following: ● 300mm Additional information: (ii) The head supplied by the pump. h (i) The velocities before and after the pump. (iii) The power supplied by the pump. Specific gravity of mercury Density of water Gravitational acceleration Pump H 1m S.G. = 13.6 p = 1000 kg m-³ g= 9.81 m s-² 150mm
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When I use Bernoulli's in the from p1+pgh1+1/2pv1^2+hp=p2+pgh2+1/2pv2^2, I cant seem to get the solution to work.

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