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Issue with pump shut down-Bentley Hammer

Hi ,

I am performing the pump shut down at a pumping station. The issue that I have is the transient pressure fluctuations do not reflect what is expected. There is no high pressure/ pressure spike in the result. I have sent you the model package. Would you please take a look and advise accordingly.

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  • Thanks Jesse for the prompt reply,

     

    The scenario that I working on is the one that you mentioned ( "LIWA EAST WEST_OP-2 (peak)").

     I have adjusted some setting as you suggested, they are helpful, so thanks for notifying me for them.

    The model is large and this is what was provided to us by another consultant, so we may use the skeletonized later. I provided the packed zip including the results so that you do not have to resimulate this . Just a quick background: the model includes 8 pumps which 4 of them supply the west side and the other 4 supply the east side.

     

    The main issues that I have:

     

    • I simulated all pumps shut down after time delay. It seems so the pump rundown is well working see the snapshot below. At the discharge side we expect to have the static pressure (or very close to that one with small fluctuations) once the transient pressure is damped (say a few minutes after pump shut down). However, this is not the case here. The snapshot below shows the transient pressures at J23709 (the discharge point for the west side), as you see the transient pressure intends to be stabilized around 40 m while the final pressure should be close to 7 m (157 (water level at reservoir-at suction side)-150 (the node elevation at discharge side)). This is not due to instability in results or short time simulation. I got pretty the same results with time step 0.005 and  the duration of 500 s. This my main concern  as we know that the transient pressures should be reached to static pressure after pressure dampening for the scenario of pump shut down. Do you have a reason for that?

     

     

     

     

     

     

     

    2- As you see from the snapshot above, we do not have too much fluctuations at the discharge point. I understand that the pump inertia may be high or we have too much pressure as the initial conditions, but we do not have the pressure spike even the same as steady state pressure?

     

    Would you please pass on your comments?

  • Hello Vali, please see the reply I just posted a few minutes ago. Here it is again:

    The snapshot below shows the transient pressures at J23709 (the discharge point for the west side), as you see the transient pressure intends to be stabilized around 40 m while the final pressure should be close to 7 m (157 (water level at reservoir-at suction side)-150 (the node elevation at discharge side)). This is not due to instability in results or short time simulation. I got pretty the same results with time step 0.005 and  the duration of 500 s. This my main concern  as we know that the transient pressures should be reached to static pressure after pressure dampening for the scenario of pump shut down. Do you have a reason for that?

    It sounds like you might be thinking about the differential head and not the pressure. After the pumps shut down, the check valve in the pumps closes since the downstream tank is at a higher elevation than the upstream reservoir.

    If you graph hydraulic grade instead of pressure you will see that it settles at around 200 m (physical elevation of the junction of 150 m plus pressure head of 50 m), which is roughly equal to the hydraulic grade at the downstream tanks (the boundary conditions connected to the junction after the pumps shut down and the check valve closes.)

    2- As you see from the snapshot above, we do not have too much fluctuations at the discharge point. I understand that the pump inertia may be high or we have too much pressure as the initial conditions, but we do not have the pressure spike even the same as steady state pressure?

    This screenshot shows the trend of pump impeller rotational speed. When the check valve closes, the flow and speed will be zero.

    On the topic of pressure returning to steady state pressure - this will only happen if the pumps turn back on, or if an upsurge occurs from vapor pocket collapse or wave reflection.


    Regards,

    Jesse Dringoli
    Technical Support Manager, OpenFlows
    Bentley Communities Site Administrator
    Bentley Systems, Inc.

Reply
  • Hello Vali, please see the reply I just posted a few minutes ago. Here it is again:

    The snapshot below shows the transient pressures at J23709 (the discharge point for the west side), as you see the transient pressure intends to be stabilized around 40 m while the final pressure should be close to 7 m (157 (water level at reservoir-at suction side)-150 (the node elevation at discharge side)). This is not due to instability in results or short time simulation. I got pretty the same results with time step 0.005 and  the duration of 500 s. This my main concern  as we know that the transient pressures should be reached to static pressure after pressure dampening for the scenario of pump shut down. Do you have a reason for that?

    It sounds like you might be thinking about the differential head and not the pressure. After the pumps shut down, the check valve in the pumps closes since the downstream tank is at a higher elevation than the upstream reservoir.

    If you graph hydraulic grade instead of pressure you will see that it settles at around 200 m (physical elevation of the junction of 150 m plus pressure head of 50 m), which is roughly equal to the hydraulic grade at the downstream tanks (the boundary conditions connected to the junction after the pumps shut down and the check valve closes.)

    2- As you see from the snapshot above, we do not have too much fluctuations at the discharge point. I understand that the pump inertia may be high or we have too much pressure as the initial conditions, but we do not have the pressure spike even the same as steady state pressure?

    This screenshot shows the trend of pump impeller rotational speed. When the check valve closes, the flow and speed will be zero.

    On the topic of pressure returning to steady state pressure - this will only happen if the pumps turn back on, or if an upsurge occurs from vapor pocket collapse or wave reflection.


    Regards,

    Jesse Dringoli
    Technical Support Manager, OpenFlows
    Bentley Communities Site Administrator
    Bentley Systems, Inc.

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