I have a Mag 9.5 on the way for a return pump for my 65 gallon. Probably should have gone bigger, but when I set up a larger tank in the near (I hope :wink: ) future, I will be using it to drive a DIY skimmer.
I was using a head loss calculator, and got all confused. Here are the numbers I entered:
950 gph
4.5' vertical
(3) 90 degree elbows
0 horizontal run
And the friction factor for 3/4" pipe
Ended up with 4.5' vertical head loss and a little over 6' head loss due to friction.
If I use the same numbers, only change the friction factor from that of 3/4 to that of 1/2, I end up with 4.5' vertical head losss, 0 friction loss.
Question 1 : How can 1/2" pipe have no friction loss?
Question 2 : I am assuming a Mag 9.5 isn't going to push 950 gph through a 1/2" pipe. Is this correct? Can't seem to find anything about how much pipe diameter affects flow rate (other than changing velocity).
Question 3: I feel really dumb for not being able to figure this out, but what size should my return line be?
Thanks!
I was using a head loss calculator, and got all confused. Here are the numbers I entered:
950 gph
4.5' vertical
(3) 90 degree elbows
0 horizontal run
And the friction factor for 3/4" pipe
Ended up with 4.5' vertical head loss and a little over 6' head loss due to friction.
If I use the same numbers, only change the friction factor from that of 3/4 to that of 1/2, I end up with 4.5' vertical head losss, 0 friction loss.
Question 1 : How can 1/2" pipe have no friction loss?
Question 2 : I am assuming a Mag 9.5 isn't going to push 950 gph through a 1/2" pipe. Is this correct? Can't seem to find anything about how much pipe diameter affects flow rate (other than changing velocity).
Question 3: I feel really dumb for not being able to figure this out, but what size should my return line be?
Thanks!