OK, so I've done some more research and have decided that an OM 4-way would cost me too much friction loss. (Unless Paul at Oceans Motions emails me back and says I'm wrong, which he might do).
Well, since his job is to sell you stuff, I can imagine the response. However, the OM 4-way, cannot do any other, than create friction loss.
Question: I've been reading lately that people are downgrading their return pumps to 3x-5x DT volume, generally aiming for the same GPH-rating as their skimmer pump. Correct/wise or no?
This is an extremely involved subject, the pursuit of which draws out more "creative" science, than just about any other facet of this hobby, save that concerning live rock, and DSBs.
The bottom line is: it is an attempt to justify the use of smaller pumps (read less power consumption,) without consideration for other needs of the system; based on the lack of knowledge of how a skimmer works, what it does and does not do, and the parameters that govern its efficiency.
[QUOTE}Regarding the closed loop, I downloaded the head loss calculator available online from many places (RC, others). I used the Sequence 3600 pump instead of the Reeflo Dart because I figured they should be similar if not identical - same maker, GPH rating, etc. The calculator gave me a feeling for how much flow I lose using different sizes of pipe, number of elbows (45/90), etc. However, one thing I'm not sure about is how the number of exits comes into play. If I have a Dart behind the tank, and I pump water through two outlets in the back panel of the tank (one on each side), then have a spraybar connected to each outlet running to the front of the tank with 4 exits each, do I lose flow by using the multiple-port spraybar? Should I just have two outputs with 1.5" pipe ending at the tank's rear wall? (I'm not planning on having an ugly spraybar, just thinking about going over the top with a manifold on each side of the tank. The idea is that it can be easily changed over time since it's not incorporated into the tank, rock structure, etc. The outputs would be just barely under the water level. Your thoughts, Uncle? I want to get as close to 3600 GPH out of this Dart as I can.[/QUOTE]
Flow calculators are inaccurate and misleading. For one, you need a starting velocity in the pipe size being used. For this you need the a lot more information, that cannot be input to the calculator.
For instance: you have a dart that starts a @ 3600 gph @ 0'. Fine. So you add up all your fittings, lengths of pipe, sizes etc etc etc. But you still have one thing missing. You have the vertical lift, cross sectional area, etc. but you don't have the actual flow rate, the pump will provide, in the plumbing system you have designed, you cannot figure the velocity, and the friction loss varies with velocity. Without that, the numbers are useless.
This problem is solved in the opposite direction. You start with a flow rate, from that the friction loss can be calculated, added to the vertical lift and velocity head, arriving at a specification for a pump that will provide the XXXX gallons per hour @ YY foot of dynamic head. This is the way pump fed plumbing systems are designed. The other way is just guesswork, although it is a rather complex calculus model to arrive at the final figure.
If you want 3600 gph through your system, you are going to need a bigger pump. I am sure you know that. That pump would need to flow 3600 gph, @ YY foot of dynamic head. So you begin your friction loss calculations @ 3600 gph. 60 gpm on most friction loss charts. The pump would probably be at least above 4000 gph @ 0'. The goal is < 5' of head per 100' of pipe. The complexity of aquarium plumbing examples I see all the time, far exceeds this due to pipe size, and number of fittings, horizontal runs; the classic example was here on RC, where a 14' vertical lift equated to 42' of dynamic head, running the pump about a foot below the shut off point.
The number of exits, just complicates things. To a point. For a closed loop to be of any benefit at all, it must exit at multiple points. The top of the tank being least effective--the sump return/overflow deals with that. Multiple points through the bottom/back of the tank. But every fitting, length of pipe, reduction in pipe size, loc-line fittings, reduces the output from the pump. With a closed loop there is no static lift, and that is too your advantage. But still without a very large pump, you are going to come up way shy of the target flow rates for a tank this size.
For me, I would run the dart on the main return, and were I inclined to do a closed loop, the pump for it would be much larger than a dart. That is the problem with closed loops: large pumps--aside from the limited adjustability.