NPSH and the validity of siphoning effect
NPSH and the validity of siphoning effect
(OP)
We have a project which is to construct and additional storage tank for sulfuric acid adjacent to the existing tanks. It has been proposed that the existing transfer pumps be used for the additional tank so as to avoid additional cost. It turned out that the said proposal is plausible because the available NPSH is still greater than the NPSH required by the pump. This calculation is based on the fact that the height of the suction pipeline is constant from the tank to the pump, what will happen if there is a need to construct an overhead piperack for the suction line, and the said piperack is higher than the low-low level of the tank?, what is the static head to be considered, will it still be the low level of the tank (and holding siphoning effect to be valid) or the height of the pipe rack?
-Thanks in advance, hope you understood the situation
-Thanks in advance, hope you understood the situation





RE: NPSH and the validity of siphoning effect
Good luck,
Latexman
RE: NPSH and the validity of siphoning effect
What would you be doing, if you knew that you could not fail?
RE: NPSH and the validity of siphoning effect
Good luck,
Latexman
RE: NPSH and the validity of siphoning effect
By the way, the pump is centrifugal.
BigInch, please elaborate on putting a booster at the tank
RE: NPSH and the validity of siphoning effect
Good luck,
Latexman
RE: NPSH and the validity of siphoning effect
What would you be doing, if you knew that you could not fail?
RE: NPSH and the validity of siphoning effect
Good luck,
Latexman