S
some control algos use (Pressure ratio)/Delta P.
where delta P is dp across flow measuring element and pressure ratio is Pd/Ps.
This is OK when the design conditions remain constant but the delta P (flow measuring device) needs to be corrected by changes in suction pressure, therefore we then get (P ratio)/(DP/Ps)
Surely this is the same as ((P ratio)*Ps)/DP and since pressure ratio is pd/ps, dont we get ((pd/Ps)*Ps)/dp which means the Ps cancels out on the top line and we end up with Pd/DP. Doesn't this infer we dont have to use suction pressure since the change in suction pressure is self cancelling in the error from the flow measutring device (which is a mss flow device) and pressure the pressure ratio
where delta P is dp across flow measuring element and pressure ratio is Pd/Ps.
This is OK when the design conditions remain constant but the delta P (flow measuring device) needs to be corrected by changes in suction pressure, therefore we then get (P ratio)/(DP/Ps)
Surely this is the same as ((P ratio)*Ps)/DP and since pressure ratio is pd/ps, dont we get ((pd/Ps)*Ps)/dp which means the Ps cancels out on the top line and we end up with Pd/DP. Doesn't this infer we dont have to use suction pressure since the change in suction pressure is self cancelling in the error from the flow measutring device (which is a mss flow device) and pressure the pressure ratio