VFD vs. Head Tank for Constant Pressure
VFD vs. Head Tank for Constant Pressure
(OP)
Good day all,
I would like to solicit your knowledge and experience regarding pumping systems requiring constant pressure. When would you select a VFD or a head tank? When would you consider each option and why?
Thanks!
IHQ22
I would like to solicit your knowledge and experience regarding pumping systems requiring constant pressure. When would you select a VFD or a head tank? When would you consider each option and why?
Thanks!
IHQ22





RE: VFD vs. Head Tank for Constant Pressure
Head tank.. Are you referring to a bladder tank? There is a recent thread here on Bladder tanks verses VFDs. You should hunt that down.
Heck here's a quick search:
Search results in Eng-Tips
Keith Cress
kcress - http://www.flaminsystems.com
RE: VFD vs. Head Tank for Constant Pressure
Thanks for your answer! By head tank, I mean large elevated tanks where the water is pumped to create constant pressure. They are normally used on industrial sites such as mines.
RE: VFD vs. Head Tank for Constant Pressure
It would help if you could describe the system better.
"Pumping system requiring constant pressure" is rather vague.
Where is the pressure constant? At the pump suction, discharge or at the user interface?
What is the flow range?
Large flow range then static tanks are probably better, smaller range then pumps.
What about losses in the "system"?
As soon as you turn a user on and off it impacts pressure due to frictional flow. If you want the user to have constant pressure then you will need a pumped system or some sort of pressure control from the tank.
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
RE: VFD vs. Head Tank for Constant Pressure
Like always thank you for your contribution to my post. I am not talking about a system in particular. I am only looking for a rule of thumb or guidance as to when each type of system is most appropriate.
Thanks!
RE: VFD vs. Head Tank for Constant Pressure
The other thing to consider is the relative size of header or supply pipe and offtake.
Quite often if people want a constant pressure at different locations you need to really oversize the header so that the friction losses are low in the header for flows at different points.
So man possible permutations of this it's difficult to come up with any standard rules which would apply.
Remember - More details = better answers
Also: If you get a response it's polite to respond to it.