A pipeline conveys benzene from one point to the other. A gauge attached to line reads 150 kPa. It is desired to check the gauge reading with benzene –over-mercury U-tube manometer. Determine the expected height difference of the mercury in the manometer; if on one end the manometer is open to the atmosphere and on the other end where the gauge pressure is connected there is a 3 cm height of benzene above the mercury meniscus. (benzene density is 876 kg/m3 and mercury 13600 kg/m3
A pipeline conveys benzene from one point to the other. A gauge attached to line reads 150 kPa. It is desired to check the gauge reading with benzene –over-mercury U-tube manometer. Determine the expected height difference of the mercury in the manometer; if on one end the manometer is open to the atmosphere and on the other end where the gauge pressure is connected there is a 3 cm height of benzene above the mercury meniscus. (benzene density is 876 kg/m3 and mercury 13600 kg/m3
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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Question
A pipeline conveys benzene from one point to the other. A gauge attached to line reads 150
kPa. It is desired to check the gauge reading with benzene –over-mercury U-tube manometer.
Determine the expected height difference of the mercury in the manometer; if on one end
the manometer is open to the atmosphere and on the other end where the gauge pressure is
connected there is a 3 cm height of benzene above the mercury meniscus. (benzene density
is 876 kg/m3 and mercury 13600 kg/m3
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