So, I went to the sticky here and used the TACO calculator to see if I can figure out my head and flow requirements so I can pic an appropriate circulator pump....
My total heat load requirements are 100Kbtu/hr., and my ideal delta T is 20 degrees. Thus my target flow rate should be 10gpm.
If I then proceed to size the pipe....I should have had 1.25 dia pex in my lines, but unfortunately...I have the 1" diameter...
I will stick with target flow of 10gpm.
The total length of my system is 310 linear feet.
Using this formula: HL = k x c x L x (f1.75) to determine my head...(I am ignoring any static head from the 70 foot vertical elevation of the OWB and mech room, OWB is above Mech room)
k= 0.00223 (1" pex) tubing size
c= 0.933, (180 degrees, water)
L= 310 ft
(f1.75) = 56.234...which is value for 10GPM....(i might be using wrong value here as the 1" pex can only flow 7.5gpm at 4ft/sec)
The result is 33 feet head.
Based upon the sizing chart, a Taco 0013 or equivalent should be the pump of choice....is this a reasonable assumption?
I did not factor the head for the flow passing thru the DHW HX and Boiler HX....(I dont know what the facotr here is)...is that a big problem?
Does my math make sense?
Mike
My total heat load requirements are 100Kbtu/hr., and my ideal delta T is 20 degrees. Thus my target flow rate should be 10gpm.
If I then proceed to size the pipe....I should have had 1.25 dia pex in my lines, but unfortunately...I have the 1" diameter...
I will stick with target flow of 10gpm.
The total length of my system is 310 linear feet.
Using this formula: HL = k x c x L x (f1.75) to determine my head...(I am ignoring any static head from the 70 foot vertical elevation of the OWB and mech room, OWB is above Mech room)
k= 0.00223 (1" pex) tubing size
c= 0.933, (180 degrees, water)
L= 310 ft
(f1.75) = 56.234...which is value for 10GPM....(i might be using wrong value here as the 1" pex can only flow 7.5gpm at 4ft/sec)
The result is 33 feet head.
Based upon the sizing chart, a Taco 0013 or equivalent should be the pump of choice....is this a reasonable assumption?
I did not factor the head for the flow passing thru the DHW HX and Boiler HX....(I dont know what the facotr here is)...is that a big problem?
Does my math make sense?
Mike