dianad
Mechanical
- Dec 27, 2007
- 66
Hi,
I'm facing the following problem: in the project, i've calculated the pressure drop along a closed circuit. The calculations gave me aprox. 3,5 mH2O of pressure drop. This was calculated for a optimal flow of 240 lt/h. After the installation was made, the max flow that the pump was able to provide was 120 lt/h. The first thing that i thought was that the circuit pressure loss was much greater than th one i've calculated in the project and therfor the pump was working in a lour point of the pump curve, so that it could overcome that loss.
After this i've started to think much deeper in this, and i've figured another reason, that i would like to see commented. In this circuit, the pressure vessel is installed after the pump. I wonder if the pressure is limited by the expansion vessel defined pressure, wich may not be enough to overcome the circuit pressure loss.
I would like to hear some comments about this.
Thanks!!
I'm facing the following problem: in the project, i've calculated the pressure drop along a closed circuit. The calculations gave me aprox. 3,5 mH2O of pressure drop. This was calculated for a optimal flow of 240 lt/h. After the installation was made, the max flow that the pump was able to provide was 120 lt/h. The first thing that i thought was that the circuit pressure loss was much greater than th one i've calculated in the project and therfor the pump was working in a lour point of the pump curve, so that it could overcome that loss.
After this i've started to think much deeper in this, and i've figured another reason, that i would like to see commented. In this circuit, the pressure vessel is installed after the pump. I wonder if the pressure is limited by the expansion vessel defined pressure, wich may not be enough to overcome the circuit pressure loss.
I would like to hear some comments about this.
Thanks!!