Manometer reading doubt in the case of viscous fluid

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SUMMARY

The discussion focuses on the correct method for reading an open air manometer when dealing with viscous fluids. It establishes that while the manometer reading can be expressed as ##p_a=\rho g z_a##, the presence of viscosity complicates the application of Bernoulli's equation. The fluid's motion and height differences at points A, B, and C must be considered, as the pressure variation is not solely dependent on hydrostatic principles. The conversation also references the need for corrections to Bernoulli's equation in viscous flow scenarios, highlighting the importance of understanding pressure gradients in laminar flow conditions.

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Soren4
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I wonder if it is correct to read an open air manometer in the case of viscous fluid in the following (usual) way. Consider the situation showed in the picture where a viscous fluid is flowing, in fact ##z_C <z_A##.

4567890.png


The reading of the manometer would be ##p_a=\rho g z_a##, ##p_b=\rho g z_b##, ##p_c=\rho g z_c##,

The main problem is that, while the black points ##A##, ##B## and ##C## are at the same heights, the fluid in ##B## is in the manometer for an height ##d## more than the fluid in ##A## and ##C## (or equivalently, the corresponding green points are not at the same height).

In the manometer the fluid is not moving, so I have no problem in writing that ##\Delta p=\rho g h##, but inside the tube the fluid is moving and therefore the variation of pressure with height would be different.

That would not be a problem if the green points were at the same height or in the case of validity of Bernoulli equation because ##\Delta p=\rho g h## would still be valid along vertical lines (even if the fluid is in motion).

But here Bernoulli equation cannot be used, since the fluid is viscous, so my question is: can I read the manometer referring heights to the horizontal line in the middle of the tube, or is there some other way to read it.

Furthermore I would like to know if there is a precise relation between the pressure in the green points and the pressure at black points. As said before, in the case of non viscous fluid, the pressures would be equal there, but what about this case?
 
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Soren4 said:
But here Bernoulli equation cannot be used, since the fluid is viscous, so my question is: can I read the manometer referring heights to the horizontal line in the middle of the tube, or is there some other way to read it.

the effect of viscosity may not be accounted for by just changing the base reference of measuring 'pressure' as due to constriction the velocity of the fluid must have increased.

there are some studies done for correction to Bernoulli's equation due to viscous flow ,therefore one can relate it...
you may see
<https://www.researchgate.net/publication/1773651_Bernoulli_correction_to_viscous_losses_Radial_flow_between_two_parallel_discs>
well i do not know (as i have not worked on it in detail)
whether it can work but as some experimental data have been generated ,so it may be helpfull.
 
Last edited by a moderator:
In laminar viscous flow in a horizontal pipe, the pressure varies hydrostatically in the vertical direction, and the pressure gradient in the axial direction does not depend on the vertical coordinate.
 

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