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AIR VAVLES

If I used VACUUM BREAKER to protect My pipe from negative Protection Due to Pump Shut Down ...
How can i know the Amount Of Air what entered  the pipe ??
And How Can i KNOW that this amount of Air has got out from my Pipe and can it get out through the other combination air valves on the pipe ??
And is there  a practical number for the amount of vacuum breaker i can use in the line in case of its length  dint exceed 2000 m without making the system unstable ?

Parents
  • To add to Sushma's reply - you may need to look at the air volume time history graph for both sides of the air valve, as the air pocket can sometimes be shown on one or both sides. To see the total air pocket volume over time, enter a number in the "report period" field in the air valve properties, re-compute the transient simulation, then look at the table of details at the end of the Transient Analysis Detailed Report (from the Report > Transient Reports menu). This is mentioned in the "Reporting" section of the air valve modeling reference article that Sushma had mentioned.

    Additionally, here is an article on comparing multiple transient protection strategies using scenarios and alternatives: Viewing HAMMER results for multiple scenarios

    In most cases air valves are already present at local high points in order to bleed out air that accumulates in the system during normal operation, and these devices often supplement other transient protection devices and strategies in order to protect the system during events such as an emergency pump shutdown.


    Regards,

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

Reply
  • To add to Sushma's reply - you may need to look at the air volume time history graph for both sides of the air valve, as the air pocket can sometimes be shown on one or both sides. To see the total air pocket volume over time, enter a number in the "report period" field in the air valve properties, re-compute the transient simulation, then look at the table of details at the end of the Transient Analysis Detailed Report (from the Report > Transient Reports menu). This is mentioned in the "Reporting" section of the air valve modeling reference article that Sushma had mentioned.

    Additionally, here is an article on comparing multiple transient protection strategies using scenarios and alternatives: Viewing HAMMER results for multiple scenarios

    In most cases air valves are already present at local high points in order to bleed out air that accumulates in the system during normal operation, and these devices often supplement other transient protection devices and strategies in order to protect the system during events such as an emergency pump shutdown.


    Regards,

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

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