Hello
I am concerned about the following issue.
I easily undertand when a valve closes the loads that this produce in pipe. The first loads begins just against the valve that closes and it is propagated upstream the valve, with the wave of pressure.
But I do not undertand when a pump trips...
Thank you very much for your answers
To summ up the anwer to my questions are:
Conslusion of the second question:
-The check valve is going to close when the SDV totally close, even though the pump is runnin at nominal r.p.m.
To my first question I am not very sure of the answer, is...
Hello everybody
I need some help about two questions:
1) Is posible for a swing check valve to close before the flow reverses because of the dropp of fluid velocity? I think it is not posible, but some of my collegues think it is.
2) I have the following instalation:
Pump(centrifugal) -...
Thank you very much BigInch for your answer. In the manual I didn't see anything about it. I will run a test job and try to check when i have a litle more time at work.
Thank you very much.
Hello
Id like to Know what formula aplies Bosfluids to calculate unbalance force produce by water hammer in straight section of the pipe system.
I know the sofware is based in characteristic method to find the the velocity of the wave of presure produced by water hammer, but I want to know the...
I found out the mistake!!!
I had an element "orifice" next to other one, and this resulted in a non linear working of the model, this was the reason of a bad operation of my model. Thanks every one for your help.
Off course the velocity changes if i close the valve, but i am saying that i select the option transient but i do not make the valve closes. I kipt the position of the valve 100 per 100 open all the time, and the flow changes, and produces unbalance forces...i do not understand...
Hello
I am studying the surge because of close of valve. I need to calculate the unbalance force in the pipe, when a valve closes in 30 sec. I get a steady state. Then I select the option "transient", but I do not anything, I let the valve still openned, and the flowrate and the pressures...
