I am designing a CLS for a 360 Gal acrylic tank (8'Lx24Wx36H)
I have purchased a Barracuda pump with 1.5" inlet and outlet.
After bends, valves and bulkheads, the return will end up in spray bars along the back. Based on pipe cross-sectional area, 1.5" = (2x1")=(4x3/4")=(8x1/2") =(16x3/8") = about (32x1/4") (these are rounded approximations)
So if my spray bars have 16 x 3/8" holes, the velocity through them will be about the same as the velocity out of the pump.
Pump out put = 3750 GPH - in the 1.5" pipe. Using an online calculator I get a velocity of about 11 ft/sec. 11 ft/sec from a 3/8 " hole seems too strong to me. If I double the holes, I can cut the velocity in half.
Q1) What is a recommended range of velocity out of a spray bar?
Q2) Are my calculations and assumptions correct?
Q3) is a 3/8" hole normally used in a spray bar?
Thank you,
Dave
I have purchased a Barracuda pump with 1.5" inlet and outlet.
After bends, valves and bulkheads, the return will end up in spray bars along the back. Based on pipe cross-sectional area, 1.5" = (2x1")=(4x3/4")=(8x1/2") =(16x3/8") = about (32x1/4") (these are rounded approximations)
So if my spray bars have 16 x 3/8" holes, the velocity through them will be about the same as the velocity out of the pump.
Pump out put = 3750 GPH - in the 1.5" pipe. Using an online calculator I get a velocity of about 11 ft/sec. 11 ft/sec from a 3/8 " hole seems too strong to me. If I double the holes, I can cut the velocity in half.
Q1) What is a recommended range of velocity out of a spray bar?
Q2) Are my calculations and assumptions correct?
Q3) is a 3/8" hole normally used in a spray bar?
Thank you,
Dave