Good answer TD2K! I've tried to estimate dp's due to pluagge and it is not easy. What do you think about the following? It seems to me it should be possible to calculate the equivalent reduced diameter resulting from pluggage of a screened filter (screen free area x % pluggage and back calculate for equivalent reduced diameter); then determine the velocity (total flow/reduced diameter calculated), this velocity is also equal to the velocity thru a mesh opening; then calculate the resistance factor(k = f x L/D) based on the length (i.e. = thickness) of the mesh plus k = 1.5 for the inlet and exit losses for the opening in the mesh; and then use Crane's equations to calculate pressure drop thru the mesh opening which has to be equal to the drop across the entire filter. If the dp calcuated this way isn't correct - at least its one way to determine intake velocity versus pluagge and coreclate it with required pump submergence for example. Thanks for any input, I've just been playing around with this type of problem recently. I recall seeing some specifc equations expressely for calculating screen mesh dp but cannot recall where or when I saw them. I would be interested in knowing how close or far away my proposal is from the real dp.
Regards, Charlie D. The more you learn, the less you are certain of.