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calculation of calibrated diaphragm flow

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TECNOMODEL

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I can't find the correct formula:confused:
I have a calibrated orifice on a pressure duct, knowing the orifice area and fluid pressure (oil) how to calculate the flow?
 
I can't find the correct formula:confused:
I have a calibrated orifice on a pressure duct, knowing the orifice area and fluid pressure (oil) how to calculate the flow?
to calculate the flow rate, by memory, you need the fluid speed, note the area.
 
It's a fact that I don't have, by the way, impossible to measure.
the system you indicate comes from bernoulli, but I have a pressure duct from which "spillo" an oil quota.
in the duct I have no fluid speed when I have the pressure, it seemed to me that it was also calculable with area and pressure.
 
by applying bernoulli (energy conservation) you should be able to obtain the output speed from the hole.
speed output from the hole = root (2*conducted pressure/density)
volumetric flow = speed*section*coefficient of contraction
 
by applying bernoulli (energy conservation) you should be able to obtain the output speed from the hole.
speed output from the hole = root (2*conducted pressure/density)
volumetric flow = speed*section*coefficient of contraction
I was also thinking about bernoulli.
What measuring unit would you use?
What do you mean by contraction coefficient?
 
formulas related to the manometric sockets with calibrated hole follow the rule of the incomprehensible fluid if we are talking about oil. therefore follow the following formula:wp_ss_20171214_0001.webpAs you can see, you always have a pressure variation between the two points...and then a sort of fluid speed indication.

for a compressible real gas, the question becomes more complex.
 
formulas related to the manometric sockets with calibrated hole follow the rule of the incomprehensible fluid if we are talking about oil. therefore follow the following formula:View attachment 48843As you can see, you always have a pressure variation between the two points...and then a sort of fluid speed indication.

for a compressible real gas, the question becomes more complex.
Good, I went close.
I lose a little on that flow coefficient:frown: the efflux coefficient to calculate it from where you take it?
What else is that pressure?

Thank you very much
 
Good, I went close.
I lose a little on that flow coefficient:frown: the efflux coefficient to calculate it from where you take it?
What else is that pressure?

Thank you very much
excellent [MENTION=21735]Mechanical[/MENTION], I should take the fluid mechanics notes to get that formula. [MENTION=48249]technomodel[/MENTION] However in the first approximation you can consider alpha =1 (alpha takes into account the reality of the fluid).
delpa p is the pressure change between the two environments you are considering. (e.g. p reservoir= 7 bar p environment = 1 bar in absolute terms delta is simply 6 bar)

greetings
 
I don't get the accounts back from experimental checks.
My orifice is not really circular but it is a circular sector. I calculated the equivalent to the sector area.
the value that I echo however is different from the measured test counter.
my orifice corresponds to a ø 0.7, we use oil with density 873 kg/m3, delta p is 79 bar.
the value of p in which unit of measure should be expressed?
 
the delta p in pa. there is written all in my formulas, including unit of measurement in brackets square.
 
You're right, I'm sorry.
I had seen all the others and I had escaped that. I know that if they don't come a little vacation:frown:
 
It's normal... too... too... too... too... .

here in briance: there, sü, neem....fá balá i man
translated: come on, let's go... let's dance the hands

But come on and give you... some castronata la ai fa.
 
mistakes that sqrt( density * pressure) will never make a speed.... if anything is sqrt(pressure/density):

(kg*m/s^2)/m^2; rho = kg/m^3 .

make the simplifications and then the root and you will return m/s.
 
of course if you multiply for the area of your hole you get your volumetric flow rate: m^3/s or lt/s
 

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