Luuk21
Chemical
- Oct 21, 2023
- 24
Hi,
I'm having some trouble converting a Cv (imperial) formula to a formula that can be used for Kv (metric).
It concerns a Cv calculation for a gas flow trough a control valve. The formula is:
Cv = [Qg * (SpGrg * T)^0.5] / [1360 * ([P1 - P2]*P2)]
This is for sub critical flow.
Cv = capacity coefficient for fully open control valve
SpGrg = specific gravity gas compared to Mw air
Qg = gas florate ft^3/h at 14.7 psia and 60 deg F
T = flowing temperature, deg R
P1/P2 = in/out pressure in psia
I used the following conversions;
Kv = 0.862 Cv
Qg = 0.0283168466 m3/h
T = 5/9 K
P = 0.0689475729 bar
I would expect a clean outcome, however, the Pressure factors do not cancel out. Substituting R for P-X does not help.
I used WolframAlpha for conversion - what am I missing here? See attachment for overview
I'm having some trouble converting a Cv (imperial) formula to a formula that can be used for Kv (metric).
It concerns a Cv calculation for a gas flow trough a control valve. The formula is:
Cv = [Qg * (SpGrg * T)^0.5] / [1360 * ([P1 - P2]*P2)]
This is for sub critical flow.
Cv = capacity coefficient for fully open control valve
SpGrg = specific gravity gas compared to Mw air
Qg = gas florate ft^3/h at 14.7 psia and 60 deg F
T = flowing temperature, deg R
P1/P2 = in/out pressure in psia
I used the following conversions;
Kv = 0.862 Cv
Qg = 0.0283168466 m3/h
T = 5/9 K
P = 0.0689475729 bar
I would expect a clean outcome, however, the Pressure factors do not cancel out. Substituting R for P-X does not help.
I used WolframAlpha for conversion - what am I missing here? See attachment for overview