Scuba_Steve
Premium Member
Hello,
I am working on ideas for a diy automated closed loop wavemaker controller with a microprocessor.
I am leaning towards sprinkler valves. Way cheaper than actuated ball valves. I even have an idea to automate the manual flow adjustment feature.
The issue I am wondering about deals with minimum PSI. To my understanding, sprinkler valves need a minimum PSI to close reliably. 5 PSI is the norm.
According to this website, to achieve 5 PSI at 0 head, the pump would need to be capable of lifting up to 11.55 ft of head. And that is assuming 0 head loss due to pipe/fitting restrictions.
1 vertical foot = 0.433 pounds per square inch (psi)
or conversely
1 psi = 2.31 vertical feet
Yet I have read about people using sprinkler valves in ATO systems, where there is virtually no pressure.
Someone please set me straight and let me know if this is possible using a fairly small pump (750 gph)!
Thanks in advance!
Edit: Btw, I realize a Mag 7 for example creates just about the correct amount of head for the above calculation. There will be multiple valves open at once though. So with 4 valves open, to close one would require 46ft of head capability to get up to 5 PSI, if I am thinking about this correctly.
I am working on ideas for a diy automated closed loop wavemaker controller with a microprocessor.
I am leaning towards sprinkler valves. Way cheaper than actuated ball valves. I even have an idea to automate the manual flow adjustment feature.
The issue I am wondering about deals with minimum PSI. To my understanding, sprinkler valves need a minimum PSI to close reliably. 5 PSI is the norm.
According to this website, to achieve 5 PSI at 0 head, the pump would need to be capable of lifting up to 11.55 ft of head. And that is assuming 0 head loss due to pipe/fitting restrictions.
1 vertical foot = 0.433 pounds per square inch (psi)
or conversely
1 psi = 2.31 vertical feet
Yet I have read about people using sprinkler valves in ATO systems, where there is virtually no pressure.
Someone please set me straight and let me know if this is possible using a fairly small pump (750 gph)!
Thanks in advance!
Edit: Btw, I realize a Mag 7 for example creates just about the correct amount of head for the above calculation. There will be multiple valves open at once though. So with 4 valves open, to close one would require 46ft of head capability to get up to 5 PSI, if I am thinking about this correctly.
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