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17. Calculate the pressure at point A in Fig. 2.50. The slope of the tube is 4 horizontal to 1 vertical. The diameters of reservoir and tube are 50 mm and 5 mm respectively. The fluid in the pipe is air and that in the manometer is kerosene (sp. gr. = 0.8). [Ans. -0.494 kN/m²] Air Oil (S=0.8) Reservoir a Tube 1 0.25 m

17. Calculate the pressure at point A in Fig. 2.50. The slope of the tube is 4 horizontal to 1 vertical. The diameters of reservoir and tube are 50 mm and 5 mm respectively. The fluid in the pipe is air and that in the manometer is kerosene (sp. gr. = 0.8). [Ans. -0.494 kN/m²] Air Oil (S=0.8) Reservoir a Tube 1 0.25 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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17. Calculate the pressure at point A in Fig. 2.50. The slope of the tube is 4 horizontal to 1 vertical. The diameters of reservoir and tube are 50 mm and 5 mm respectively. The fluid in the pipe is air and that in the manometer is kerosene (sp. gr. = 0.8). [Ans. -0.494 kN/m²] Air LIT Oil (S=0.8) Reservoir A Tube 0.25 m
Transcribed Image Text:17. Calculate the pressure at point A in Fig. 2.50. The slope of the tube is 4 horizontal to 1 vertical. The diameters of reservoir and tube are 50 mm and 5 mm respectively. The fluid in the pipe is air and that in the manometer is kerosene (sp. gr. = 0.8). [Ans. -0.494 kN/m²] Air LIT Oil (S=0.8) Reservoir A Tube 0.25 m
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