Thanks Rjukan for the responses and ideas. I see you suggest I remove any flow from the drain directly to the fuge and have all of it go first to the skimmer section. If I understand this right that would mean the only flow to the fuge would come from diverting some flow from the return pump. I was under the impression it would be helpful to have some non-skimmed water in the fuge? Also, do you think it is helpful to have any valves on the drains as a safety measure or for maintenance?
As far as head pressure goes, it is 5’ from the bottom of the sump to the top of the DT. I have read something similar - about 400 gph should be the flow in the sump. I am planning on two K-4s in the DT for added circulation, so not expecting the pump to provide the entire turnover. I definitely want a quieter pump and one that is very dependable. Don’t mind paying a little premium for that. Heard good things about the eheim and so that is why I was planning on that one. The 1262 is rated at 900 GPH, but not sure what it would be after all the valves, bends and head loss. I know there is a calculator on RC, but wanted to get the design right first and then run the math… and would rather rely on all the folks out there that have similar set-ups.
PDAlber â€"œ I will definitely check out the Herbie method. Didn’t realize that was possible with the Tech tanks that have the built in overflows. I would like to keep the gurgling to a minimum. If I recall, that approach will also provide some peace of mind against floods.