TurbineBlade
Nuclear
- Aug 23, 2006
- 44
Hi all,
I have two pressure indicators; one in the suction and the other in the discharge sides of the pump. I would like to find out the flow rate of the system. The questions that I have are:
1. Does the DP measurement across the pump reflect accurately to the overall system pressure drop?
2. If I take the DP measurement, convert to head (ft) and read it from the pump curve to get the corresponding Q. Is this correct approach?
3. My system is heavy water, which is 10% heavier than light water, and operate at a higher temperature. I believe that the pump curve from manufacture is generated based on light water at STD condition. When I do the DP to head (ft) conversion based on heavy water density, do I have to further convert the head (ft) to light water density before reading the corresponding Q on the pump curve?
Thank you for your help
Turbineblade
I have two pressure indicators; one in the suction and the other in the discharge sides of the pump. I would like to find out the flow rate of the system. The questions that I have are:
1. Does the DP measurement across the pump reflect accurately to the overall system pressure drop?
2. If I take the DP measurement, convert to head (ft) and read it from the pump curve to get the corresponding Q. Is this correct approach?
3. My system is heavy water, which is 10% heavier than light water, and operate at a higher temperature. I believe that the pump curve from manufacture is generated based on light water at STD condition. When I do the DP to head (ft) conversion based on heavy water density, do I have to further convert the head (ft) to light water density before reading the corresponding Q on the pump curve?
Thank you for your help
Turbineblade