Rick,
You did somethign evil with that reply. You prompted me to open my Fluid Mechanics book again after years of it being retired... I read just a enough to be dangerous.
What you said is essentially true. For an abrupt pipe opening (which is what we usually have), there is a noticeable headloss due top separation. On an abrupt pipe inlet (squared with wall of the vessel), eddy currents develop just inside the fitting, which create more headloss. In a rounded pipe inlet (looking at a cross sectino of the wall being penetrated, the inlet has a radius that leads into the pipe, rather than abrupt ends like PVC), there is no separation (depending on pipe diameter and flow), so the head loss is much lower. One inside the pipe, headloss is added by the walls of the pipe (dependant on the coefficient of friction for the given medium). This can be overcome by using a larger diameter pipe to feed the CL pump (drill a 1 1/2" hole and cone down to a 1" for a 1" inlet on the pump, without abrupt edges like bushings). The eddies may still occur, but since the diameter is larger than the diameter that is needed at the pump, it does not create as much headloss. It would take some careful planning to reduce the headloss to near zero at the pump inlet, but it can be done. The friction of the pipe and the fittings create the bulk of the headloss on the return trip to the tank. By using larger diamter piping than the pump is designed for, you can reduce headloss because of this in most cases.