KimWonGun
Mechanical
- Oct 11, 2010
- 78
I am trying to replicate the result of an on-line orifice plate calculator but am apparently overlooking a key point. Can anyone spot my error?
I am using the equation: flow rate = flow coefficient*orifice area*sqrt(2(deltaP)/density)for a fluid.
where flow coefficient = discharge coefficient / sqrt(1-(d2/d1)^4)
inner pipe diameter (d1) = 0.837 in
orifice diameter (d2) = 0.579 in
kinematic viscosity @200F = 1.32 cSt
deltaP = 1 psi
specific gravity@ 200F = 0.9556
discharge coefficient = 0.63
flow coefficient = 0.63/(sqrt(1-0.579/0.837)^4) = 0.718
flow rate = (0.718)*(pi*(0.579)^2/4)*sqrt(2*1/(0.036111/386))
The calculator shows a flow rate of 28.5 cu in/s while my manual calculation shows 47.6 cu in/s. Where is my error? Even though the dimensional analysis works out, I wonder why the viscosity does not play a part in this equation?
I am using the equation: flow rate = flow coefficient*orifice area*sqrt(2(deltaP)/density)for a fluid.
where flow coefficient = discharge coefficient / sqrt(1-(d2/d1)^4)
inner pipe diameter (d1) = 0.837 in
orifice diameter (d2) = 0.579 in
kinematic viscosity @200F = 1.32 cSt
deltaP = 1 psi
specific gravity@ 200F = 0.9556
discharge coefficient = 0.63
flow coefficient = 0.63/(sqrt(1-0.579/0.837)^4) = 0.718
flow rate = (0.718)*(pi*(0.579)^2/4)*sqrt(2*1/(0.036111/386))
The calculator shows a flow rate of 28.5 cu in/s while my manual calculation shows 47.6 cu in/s. Where is my error? Even though the dimensional analysis works out, I wonder why the viscosity does not play a part in this equation?