In a certain industrial process, oil of density p flows through the inclined pipe in the figure manometer with fluid density Pm- measures the pressure difference between points 1 and 2 as shown. The flow is steady, so that fluids in the U-tube are stationary. Find an analytic expression for p1-p2 in terms of system parameters. Discuss the conditions for there to be no flow in the pipe, for flow to move up from 1 to 2 and for the flow to go down from 2 to 1. O a. h-0 for all cases O b. h-0, h>0, and h-0 respectively O c. h<0, h>0, and h/0 respectively O d.h-Q, h>0, and h<0 respectively O e. h/0, h>0, and h<0 respectively

Refrigeration and Air Conditioning Technology (MindTap Course List)
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Author:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
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Chapter2: Matter And Energy
Section: Chapter Questions
Problem 18RQ: Describe Dalton's law as it relates to a confined mixture of non-reactive gases.
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Transcribed Image Text:0 h S (2) p Pm
In a certain industrial process, oil of density p flows through the inclined pipe in the figure (refer to figure document). A U-tube
manometer with fluid density Pm, measures the pressure difference between points 1 and 2 as shown. The flow is steady, so that fluids
in the U-tube are stationary. Find an analytic expression for p1-p2 in terms of system parameters. Discuss the conditions for there to
be no flow in the pipe, for flow to move up from 1 to 2 and for the flow to go down from 2 to 1.
O a. h-0 for all cases
O b. h-0, h>0, and h>0 respectively
O c. h<0, h>0, and h#0 respectively
O d.h-0, h>0, and h<0 respectively
O e. h/0, h>0, and h<0 respectively
Transcribed Image Text:In a certain industrial process, oil of density p flows through the inclined pipe in the figure (refer to figure document). A U-tube manometer with fluid density Pm, measures the pressure difference between points 1 and 2 as shown. The flow is steady, so that fluids in the U-tube are stationary. Find an analytic expression for p1-p2 in terms of system parameters. Discuss the conditions for there to be no flow in the pipe, for flow to move up from 1 to 2 and for the flow to go down from 2 to 1. O a. h-0 for all cases O b. h-0, h>0, and h>0 respectively O c. h<0, h>0, and h#0 respectively O d.h-0, h>0, and h<0 respectively O e. h/0, h>0, and h<0 respectively
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