MSurgeon
Mechanical
- May 23, 2002
- 3
Can anyone provide some guidance on the theory on sizing a priming tank.
The priming tank I am considering is in the suction line of the pump. On pump start-up as the pump draws the water level down in the priming tank the reducing air pressure in the top of the tank causes water to be drawn up the suction line in to the top of the tank. The tank is sized so that the water level in the tank remains above the pump suction when a flow into the top of the tank is achieved.
Assuming a perfect gas under at a constant temperature so that P1xV1=P2xV2 I have carried out some calculations that appear to give reasonable results but I can't find any alternative sources of information to confirm if I'm on the right track or not.
Any feedback would be appreciated
The priming tank I am considering is in the suction line of the pump. On pump start-up as the pump draws the water level down in the priming tank the reducing air pressure in the top of the tank causes water to be drawn up the suction line in to the top of the tank. The tank is sized so that the water level in the tank remains above the pump suction when a flow into the top of the tank is achieved.
Assuming a perfect gas under at a constant temperature so that P1xV1=P2xV2 I have carried out some calculations that appear to give reasonable results but I can't find any alternative sources of information to confirm if I'm on the right track or not.
Any feedback would be appreciated