How important is it to actually maintain the recommended 2 ft/sec minimum flow velocity to entrain air bubbles? Some posts, both here and elsewhere seem to indicate a slower velocity is acceptable or even desirable.
It seems like a pretty good balancing act between loop length, dT, and flow rate for a decent length of either 3/8 or 1/2 inch pex.
~900 feet total for the zone.
~18k btu design load for the zone
For 1/2 inch pex, flow needs to be above 1.1 gpm which leaves a long loop length and the resulting high head, several short loops length and small delta T, or short length, low head, low flow.
3/8 pex drops the required flow nicely, while increasing head for the same loop length.
Thanks.
It seems like a pretty good balancing act between loop length, dT, and flow rate for a decent length of either 3/8 or 1/2 inch pex.
~900 feet total for the zone.
~18k btu design load for the zone
For 1/2 inch pex, flow needs to be above 1.1 gpm which leaves a long loop length and the resulting high head, several short loops length and small delta T, or short length, low head, low flow.
3/8 pex drops the required flow nicely, while increasing head for the same loop length.
Thanks.

T=30F, 33,000 btuh; and I supply at 100F via a mixing valve from a 1000 gal storage tank at 192F maximum. I supply the manifold via a plate hx and 1" copper Sides A & B directly from storage, basic air scoops on Sides A & B, and boiler supply to storage is 1-1/4" copper with a Spirovent. Floor is kept at constant 61F +/- 1F. Typical btuh average/day during winter (+25F to -30F) is 12,000 - 18,000. With 100F supply, tank storage maximum is 767,000 btu, which means I have 2+ days of stored btu's. Low temp supply possibility makes a big difference.
sad, there is a better (and ALOT cheaper) way, but that is the light that they refuse of plain old don't want to see.......through the smoke.