SMW265
Mechanical
- May 9, 2013
- 2
Gents, and Ladies,
I am looking to have a concrete answer as to the pump that was selected for the glycol heat recovery system in my building.
I have 2 AHU's that have 9 circuit setters each on them. ( 3 banks of 3),
each coil has a 9.7' drop at the 88.9 gpm.
There are also 2 heat recovery coils which have 6 circuit setters each on them. (2 banks of 3)
a 5.7' drop across them at 133.33 gpm.
if i have a 10" main which breaks off into an 8" sub main, which feeds 9 coil banks from one AHU in parallel, and goes back into an 8" submain to a 10" main.
would i be using the total of 9.7'x 9 for the pump head to be overcome?
or would it just be 1600 gpm at 10'
not sure how to size this.
I understand there is also effective pipe length involved, and I know how to incorporate that, My real question is do i need each individual coil loss added in.
I am looking to have a concrete answer as to the pump that was selected for the glycol heat recovery system in my building.
I have 2 AHU's that have 9 circuit setters each on them. ( 3 banks of 3),
each coil has a 9.7' drop at the 88.9 gpm.
There are also 2 heat recovery coils which have 6 circuit setters each on them. (2 banks of 3)
a 5.7' drop across them at 133.33 gpm.
if i have a 10" main which breaks off into an 8" sub main, which feeds 9 coil banks from one AHU in parallel, and goes back into an 8" submain to a 10" main.
would i be using the total of 9.7'x 9 for the pump head to be overcome?
or would it just be 1600 gpm at 10'
not sure how to size this.
I understand there is also effective pipe length involved, and I know how to incorporate that, My real question is do i need each individual coil loss added in.