mechanicalchad
Mechanical
- Jul 15, 2004
- 36
Hi There,
I have inherited the engineering on an upstream oil skimming tank site that utilizes four tanks in series, each tank having a pipe that forms an inverted u within the tank such that the suction side of the inverted u pulls from the bottom of the tank at around 2 feet then goes upwards to the crest of the u at a height x (x varying in each tank but around 5.488 m in the first tank to 3.962 m in the last tank) and then back downards to our nozzle at 2 feet elevation (I've attached a digram of the first two tanks for reference). The inverted U and nozzles are NPS 4.
As explained to me, the idea is that it will pull heavy fluid from the bottom of tank so that with each successive tank you have less light ends being passed along. The inverted U was to stop the flow from one tank to the next when the level dropped below the crest of the U similar to a stand pipe.
It seems to me that since the inlet and outlet will remain fully flooded that I would have a siphon effect drawing down my levels until the tanks are equalized. I've been told that as the fluid slows the siphon will break. Does anyone have any experience with this that they could share some thoughts? I understand the Froude number can be used to determine whether it will be self venting, but will this work if it is fully flooded on both inlet and outlet? I'm wondering do I need to install a siphon break at the crest of the inverted U?
Any ideas or thoughts are muchly appreciated.
Thanks in advance,
Chad
I have inherited the engineering on an upstream oil skimming tank site that utilizes four tanks in series, each tank having a pipe that forms an inverted u within the tank such that the suction side of the inverted u pulls from the bottom of the tank at around 2 feet then goes upwards to the crest of the u at a height x (x varying in each tank but around 5.488 m in the first tank to 3.962 m in the last tank) and then back downards to our nozzle at 2 feet elevation (I've attached a digram of the first two tanks for reference). The inverted U and nozzles are NPS 4.
As explained to me, the idea is that it will pull heavy fluid from the bottom of tank so that with each successive tank you have less light ends being passed along. The inverted U was to stop the flow from one tank to the next when the level dropped below the crest of the U similar to a stand pipe.
It seems to me that since the inlet and outlet will remain fully flooded that I would have a siphon effect drawing down my levels until the tanks are equalized. I've been told that as the fluid slows the siphon will break. Does anyone have any experience with this that they could share some thoughts? I understand the Froude number can be used to determine whether it will be self venting, but will this work if it is fully flooded on both inlet and outlet? I'm wondering do I need to install a siphon break at the crest of the inverted U?
Any ideas or thoughts are muchly appreciated.
Thanks in advance,
Chad