model TE 5 MD-SC , and that pump has a 1/2" discharge but is rated at a higher PSI and will get 858 GPH at 15" head pressure. I see that the TE 5.5 MDQ-SC has a 1' discharge, and puts me in the same boat as the IWAKI, but not the TE 5 MD-SC.
It is not so much that I can't change my return plumbing to 1", I can do it. But I custom built my canopy when I added my Metal Halide lights, and drilled the canopy and hard plumbed it with 1/2" PVC, and really don't want to have to remove the canopy, redrill and replumb, if I can accomplish the same thing just by upgrading to the TE 5 MD-SC pump that has the same 1/2" discharge but a higher PSI rating and consequently more flow at the same head pressure.
So, what is the main advantage to me replumbing for 1" ? If the TE 5 MD-SC has a 1/2" discharge, and is rated at 858 GPH at 15" head, will the flow be better with a 1" discharge pump that is rated for the same flow? I am not sure I am clear on this. I guess what I am asking is, is 850 GPH thru 1" plumbing any better, and why, than 850 GPH thru 1/2" plumbing.
I see the advantage to replumbing at 1" for a pump that would give me over 1000 GPH, but if I can keep the plumbing at 1/2" with the TE 5 MD-SC at 858 at 15' head, and double my flow from the sump return to 850 GPH, and then add a closed loop using the 4 MD-SC, which I can mount higher at the back of the canopy, and get another 700 GPH thru the closed loop I am not sure I understand any advantage. So if there is any real advantage that I am missing, other than possibly using more electricity to run the higher pressure rated pump, I would appreciate the explanation of the advantage that I am missing...
I also just reread your answer, and think I understand something else. You are saying, if I plumb from the 1" discharge of the pump up to the first Tee, and it doesn't get reduced to 1/2" until the first tee, which happens to be above the waterline of the main tank, that in effect reduces head pressure??? Am I understanding that correctly? I was always under the impression that it didn't matter where the reduction was made and that the reduction would have the same effect on flow... but I can see how it makes sense that if all of the vertical head pressure was plumbed at 1" up to the first tee, the reduction would have less effect, since the pump would be pumping against the vertical head pressure at 1" and not reduced until after the vertical head pressure was overcome.??? Am I getting this at all?? LOL
Thanks, so much...
Dave