A supplier brought to my attention that I had an unusually high velocity going through a check valve in a PS design I was working on...Pump is split case, 10" suction x 8" discharge. Design point is 2604 gpm at 177'. Service is raw (high quality) water, 60 deg F - nothing out of the ordinary. Coming off the pump flange face, I have a 90 bend, and then check after the bend. I increase to my line size after the check.My line velocities are fine, however, the velocities through the check are rather fast (15 fps at operating point, - higher at peak flows). What is typical max velocity through a check?Further, while the pumps are VFD driven, the nature of the application is that the flows could be low - with cycling at off peak times. What is the MIN velocity needed so that I dont get 'flutter' (not sure of the word) of the check?Probably use a tilted disc type or air cushioned swing.A check valve should correctly be dimensioned by flow (eg fluid velocity) rather than dimension, both to give the smallest flow loss and to have the best soft closing properties to avoid pressure peaks when closing.By variable flow (soft stop and start by pumps, and motor regulation of flow) we see increasing cases where check valves are 'mis-selected' and causes problems and unnecessary large power losses when pumping.You will need a certain straight length before and after the check valve at this velocity to have a proper laminar even flow.If you select a valve 'from the upper shelf', for example a soft closing nozzele check valve similar to or as sample given below, you will find that 3 to 4 m/s ( 9 to 12 feet a second - see brochure for max) is a normal flow , and that the very low pressure loss may give a very reasonable payback time for the extra cost of the long-life construction.Water mains are normally lower than this, about 1 -2 m/s, 3 m/s when cleaning.

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