Finally, I've read to the end of this thread. *whew*![]()
I may have missed a couple of things through all the friendly bantering. But I think the basic question is how come we get less head pressure through these manifolds of smaller pipes.
First, to sort of answer Organicreefer's question about flow--here is the approximation that I use:
The change in pipe dia is equal to the change in volumetric flow squared (assuming linear velocity is unchanged). Paul hit on it when he talked about the AREA of a pipe rather than it's diameter.
When calculating head pressure on a manifold. Each port is calculated separately. That is, head pressure from the pump would be equal at all ports if the manifold were horizontal. Vertical manifolds start with the pressure losses at the level of the port--this is why you need an even number of ports--it really helps with balancing the system.
Total approx head pressure can be calculated by the following:
1/total= 1/port 1 + 1/port2 + 1/port3 + etc....
BTW, too little head pressure can be just as bad as too much. The best thing to do is to get a pump curve (from the manufacturer) for the pump and design your system around the pump curve.



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use 1.5 inch pipes,don not reduce below one inch ,reduce at the last possible point= the best way



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