I am designing my system and could use some help with determining head loss for my return pump selections. I am planning a 90 gallon DT. At 5X the volume that is 450 GPH.
Here is what I would like to do.
Here is what I would like to do.
- Trying to cut some up front costs so will be buying Jebao pumps and replacing as I progress in the hobby. I will be selecting DC pumps to give me some flexibility in flow.
- Want redundant pumps. Pump #1 will pump straight back to the DT from the sump. Pump #2 will pump through a manifold that will have a UV Filter and a combination Carbon/GFO Reactor on it, then will go back to the DT.
- I understand the general principals of head loss on a pump. I estimate P1 will have about 5’ vertical, 2’ horizontal and 3 elbows for a total of about 8.2 feet.
- For P2 I am estimating about 10 feet of loss for the additional piping and elbows. What I don’t know how to figure is loss through the UV and the Reactor, and through any flow monitoring device but how do I determine this if those specs are not provided in the sales information?
- The new Jebao MDP series does not have any published performance charts that I can find but the sales info does provide max flow and head height. Am I correct that If the info says max 924 GPH that it is at the pump and that at a max head of 11.5 feet flow will be nearly zero? How do I figure out my in between values? Can I do it through a proportional loss? IE: 924GPH / 11.5 feet = 80.3 GPH/foot, so my 10 foot of head would only be pumping (11.5-10)*80.3=120.5 GPH? I realize this is a straight line graph opposed to a true performance chart which is a curve.

