In respect of waterhammer analysis I run AFT's Impulse
software.(www.aft.com for a demo).
The speed of closure of the check valve is something
that one considers to prevent the reverse running of a
pump. A rapid closing valve is preferred in respect of
the check valve as you are sure what position it is
in. With a swing check valve is expected to close you
are never sure that it has not hung up. A tilt check
is a better option. Red Valve have just put out a flap
valve for the water industry that is worth
investigating.
A translational type of valve such as those
manufactured by Mokveld or Mannesmannn close in less
than 0.4 secs. They are not encumbered with
counterweights on lever arms. Experience shows that
they will ameliorate the peaks of a surge. Whereas a
conventional swing check may slam shut when the flow
has reversed and the peak pressure will be
destructively high.
If a pressure transient greater than the design
pressure of the pipeline still occurs then other
preventative measures are required. This may include
faster acting bypass valves, relief valves, surge
tanks, accumulators,etc. The worst case is ususally
when the system power is lost, column separation may
occur, followed by the columns coming together when
flow reverses.
Books by Streeter and Wylie, Boldy, Thorley and
Chaudry are worth reading on this complex subject.
If velocity changed in time T < 2*L/w , sec.
dH = w * V / g , ft of fluid
L Length of pipe, ft.
w is the wave velocity. for water in steel pipes
w=4680 ft/sec.
V is the velocity difference (V2-V1) ft/sec.
g acceleration of gravity, 32.2 ft/sec^2.
Reference: Handbook of Hydraulics. Ernest F.
Brater,
McGraw-Hill.
Itzhak Shdemati
- "SARE, RALPH H."
<SARERH@YANPET.SABIC.com>
wrote:
>
>
> what is the
procedure to predict the pressure rise
> due to rapid
> closure of the check valve?
>
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Received on Mon Aug 27 20:01:00 2001