hgordon
Chemical
- Jan 23, 2018
- 33
Hi there,
I am getting my head around fire pumps which start at a constant speed direct on line.
When a pump starts on an empty system there is no back pressure then the pressure builds from friction or lift.
So to me it starts at max flow then the flow reduces as the pressure builds until say the water meets a dead end.
Visualising that on a pump curve - it doesn't follow a system curve because the pipe system is not constant.
It seems the flow and pressure from pump start until churn would follow the pump curve from right to left, is that right?
So for a period the pump is running way off its curve until the backpressure builds to about 100m head? As per attached jpg.
Of course we would never run a system like this due to the massive water hammer that could occur - this is just theoretical.
We use jockey pumps to keep the discharge primed around the churn pressure. However there is another idea of using a pressure relief 'surge' valve also to help water hammer which I am not sure about, the valve is open on start up to release the initial water surge then closes at a set pressure. What if the relief pipeline has not enough backpressure and the surge valve never closes?? And if the surge valve is set to close at only 1-2bar what is the point in having it? If anyone has any info on the benefits on these surge valves would be apprecaited, this is a Cla Val surge/relief valve.
Thanks,
I am getting my head around fire pumps which start at a constant speed direct on line.
When a pump starts on an empty system there is no back pressure then the pressure builds from friction or lift.
So to me it starts at max flow then the flow reduces as the pressure builds until say the water meets a dead end.
Visualising that on a pump curve - it doesn't follow a system curve because the pipe system is not constant.
It seems the flow and pressure from pump start until churn would follow the pump curve from right to left, is that right?
So for a period the pump is running way off its curve until the backpressure builds to about 100m head? As per attached jpg.
Of course we would never run a system like this due to the massive water hammer that could occur - this is just theoretical.
We use jockey pumps to keep the discharge primed around the churn pressure. However there is another idea of using a pressure relief 'surge' valve also to help water hammer which I am not sure about, the valve is open on start up to release the initial water surge then closes at a set pressure. What if the relief pipeline has not enough backpressure and the surge valve never closes?? And if the surge valve is set to close at only 1-2bar what is the point in having it? If anyone has any info on the benefits on these surge valves would be apprecaited, this is a Cla Val surge/relief valve.
Thanks,