Someday I'll get around to doing that math for you. I don't like doing math with a headache or when I'm tired, so we're looking at the end of spring or mid-summer. 
Nope. As long as you are 1.5 diameters away from the next hole or one diameter from an edge, there isn't a stress riser.
Nope. The only issue is when the canisters are dirty. In a closed loop system, it is zero head. The pvc restriction is insignificant.
In a closed loop, gravity doesn't apply. You don't have to oversize the drain side. You can use the size that is on the pump or a size larger.
Again, the simple answer is that it is a closed loop. You don't have to worry about it.
For open loop systems, yes it is only the vertical distance.
Not really. It is perceived that way because there is a lot of stuff there. Designed well, Chris will have a good running system.
The RUGF system will have very little restriction at all. Again, attention to details during the design phase is what determines success and failure. The surface area of the gravel bed is large enough so that any restriction is negligible.
Actually, if you wanted to split hairs, "head" and "pressure" don't belong together. Head is measured in vertical feet and pressure is measured in pounds per square inch. You can use either head or pressure to talk about performance lost from various restrictions, but not both in the same discussion. It is about the equivalent of doing math with metric and English units without doing the conversions. I hope that makes sense.


dawnmarie;3867298; said:As far as a stress fracture, is that likely in acrylic ?
Nope. As long as you are 1.5 diameters away from the next hole or one diameter from an edge, there isn't a stress riser.
JakeH;3872171; said:but those pumps will lose substantial flow by having to push thru the canisters, then up thru all that PVC with 240G of water pushing back down on it. Again, I imagine it would work but I think you should expect the pumps to flow like there's 9' or 10' of head.
Nope. The only issue is when the canisters are dirty. In a closed loop system, it is zero head. The pvc restriction is insignificant.
dawnmarie;3872407; said:I was careful to size the drain to provide gravity powered GPH in excess of the pump capacity so as to maximize the potential of the pump.
In a closed loop, gravity doesn't apply. You don't have to oversize the drain side. You can use the size that is on the pump or a size larger.
dawnmarie;3872407; said:If the return pipe/RUGF is sized to adequately flow the capacity of the pump(s) would I not still calculate maximum head pressure as the vertical distance between the outlet of the pump and the surface of the water in the tank ? What am I missing ?
Again, the simple answer is that it is a closed loop. You don't have to worry about it.
For open loop systems, yes it is only the vertical distance.
JakeH;3872779; said:Head pressure stated by the mfr. will be straight pipe with no obstructions. You plan to put some serious obstructions in the way of that pump.
Not really. It is perceived that way because there is a lot of stuff there. Designed well, Chris will have a good running system.
JakeH;3872779; said:...but if you're adding under gravel returns I would expect your actual head pressure to be significantly higher...
The RUGF system will have very little restriction at all. Again, attention to details during the design phase is what determines success and failure. The surface area of the gravel bed is large enough so that any restriction is negligible.
JakeH;3875254; said:The chart for your pump lists head height, not head pressure.
Actually, if you wanted to split hairs, "head" and "pressure" don't belong together. Head is measured in vertical feet and pressure is measured in pounds per square inch. You can use either head or pressure to talk about performance lost from various restrictions, but not both in the same discussion. It is about the equivalent of doing math with metric and English units without doing the conversions. I hope that makes sense.
dawnmarie;3878561; said:...then it's time to shoot the engineer.
