All Flow Meters for Steam & Gas MUST have "Density
Compensation" to safeguard against error in reading depending on
difference between the specific density and the actual flow density.
Error in Orifice /Differential Pressure Device :
[√ specific volume actual/specific volume -1 ] x 100
= :[√ 4.44 cu.ft/lb/3. cu.ft/lb -1 ] x 100 = 6.8%
over reading by Meter
Error in Vortex Pressure Device :
[specific volume actual/specific volume -1 ] x 100
= :[ 4.44 cu.ft/lb/3.89 cu.ft/lb ]- 1 x 100 = 14.0% over reading by Meter
Calibrated for 100 psi (specific volume 3.89 cu.ft/lb ) when
actual is 85 psi (specific volume 4.44 cu.ft/lb)
Example case, the Boiler House Boiler is at say ≤8.0 Bar
= 115 psi or 3.46 cu.ft/lb specific volume. Whereas you are getting ≤5.0 Bar at
your Header = 70 psi or 5.19 cu.ft/lb specific volume.
Now your meter was calibrated at obviously 8.0 bar or 115
psi while you are getting
≤ 5.0 bar or 70 psi.
Therefore based on above the Error in Reading
without density compensation on an Orifice flow Meter will be :
Error in Orifice /Differential Pressure Device :
[√ specific volume actual/specific volume -1 ] x 100
= :[√ 5.19 cu.ft/lb/3.46 cu.ft/lb -1 ] x 100 = 22.47 % over reading by Meter
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I not only use all the brains that I have, but all that I can borrow. Woodrow Wilson
You can always use pV=nRT and get fairly good results. Knowing that m=Mn where M=18.0538 g.mol-1 for water and steam, and R = 8314 J.kmol-1.K-1, we have:
p * V = (m / 18.0538 g.mol-1) (8314 J.kmol-1.K-1) T
V / m = (1 / 18.0538 g.mol-1) (8314 J.kmol-1.K-1) T/p
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