Maple - yes the big expansion tank is mounted right beside the boiler in the barn. Its about 18" x 48" tall, and has a bladder to separate the air/water. I read the pressure on the air side using the Schrader valve. I will check it next time I burn when it is hot to see what the pressure changes to.
How do I know what the lowest system pressure is? I guess it would be at the inlet side of the boiler circulator, but I have no way to measure the water pressure there. Be real nice to have pressure taps on either side of that circulator to tell what is going on in regards to head and flow.
Again - I inherited this system with the house less than a year ago. These are very unusual around here (northeast TN), so the only help I get is from this forum and you guys are awesome.
Jim - the idea of putting two circs in series may just work. Garn design manual states 6 to feet per second maximum velocity. For 1", this puts me at 11 to 14 or so gpm. Pressure loss charts are almost all at 60F, but I found one that shows the pressure drop is less as water temperature increases. Should I calculate the pressure drop for the return and supply lines differently since one runs about 160F and the other is around 110F? Also - is this the delta T that you are referencing? Thanks for the TACO curves.
How do I know what the lowest system pressure is? I guess it would be at the inlet side of the boiler circulator, but I have no way to measure the water pressure there. Be real nice to have pressure taps on either side of that circulator to tell what is going on in regards to head and flow.
Again - I inherited this system with the house less than a year ago. These are very unusual around here (northeast TN), so the only help I get is from this forum and you guys are awesome.
Jim - the idea of putting two circs in series may just work. Garn design manual states 6 to feet per second maximum velocity. For 1", this puts me at 11 to 14 or so gpm. Pressure loss charts are almost all at 60F, but I found one that shows the pressure drop is less as water temperature increases. Should I calculate the pressure drop for the return and supply lines differently since one runs about 160F and the other is around 110F? Also - is this the delta T that you are referencing? Thanks for the TACO curves.