Hi All,
I have a query which many of us(Junior process engineers) are still confused with:
First of all this is a general query and is not a project specific one.
I have a system with a vessel upstream of a level control valve operated at 140 psig and a vessel downstream of the same control valve operated at 80 psig. Flow through the system is 150000 kg/h(153 m3/h) of water.This means that the piping and other components including the control valve shall be designed in such a way that the maximum pressure drop through the system shall not exceed the pressure differential between the two vessels(i.e 140-80=60 psi). So the question is
" As the % travel of the control valve is changed the pressure drop across the control valve will also change, but the overall system pressure differential remains the same (i.e 60 psi). Then what is the reason that the flow has to decrease or increase as the valve travel increase or decrease. I searched everywhere regarding this and all i got about this is something regarding the relationship between flowrate, resistence and pressure drop. Can you please clarify what is this relationship".
Regards
Che#pet