spliting the overflow line is also an option as saltwatersmac mentions.. feeding the skimmer just what it needs to operate most effecently and the rest to the fuge..
thats why he suggests having the return pump section in the middle, so the water from the skimmer and fuge can be processed and returned without redundance water filtration..
Im wondering if anyone has actually tested if the fuge can remove any more from well skimmed water, like NO3
.. but really alot of the NO3
should be removed by the LR