PulseGuard Pulsation Dampers
PulseGuard: Guarding Against Pulsation
Pump Pulsation Dampers
Fluid Flow Control Animations

Pulsation Damper Information PDF Pulsation Damper PDF PG31 Printable Version

Pulsation Dampers - Allow for "Overlap" of One Displacement to the Next

This is dependent on the volumetric efficiency, due to compressibility of your system liquid.
This may radically effect the level of flow fluctuation, and pressure pulsation.

  If in this example, left, the pump was a triplex then the flow would come to a complete halt between strokes. This is because a rotary driven reciprocating pump sucks & discharges for 180° of rotation and the next displacement begins after 120°. The overlap on triplex at 100% efficiency is therefore 60°. At 77.512% the calculation shows that the 60° has been lost, hence with no overlap the flow will come to a halt between displacements. It will be as "pulsatious" as a duplex.

By the same calculation as the example; if the efficiency was 85% then the lost angle would become 48°. With a "Quin" a new displacement should begin every 72 degrees (360/5), and as discussed above a triplex should displace every 120°. 120° minus 72°=48°. But at 85% efficiency, 48 has been lost, so a Quin can cause as much flow fluctuation as a perfect Triplex if the quin has low volumetric efficiency.
THEREFORE, A three headed diaphragm metering pump may produce flow fluctuations as bad as, or worse than, a duplex pump or double acting simplex pump. A quintuplex, or 5 plunger pump, may produce flow fluctuations as good as, or worse than, a good triplex pump, it all depends on volumetric efficiency.Consequenty, where N(squared) is a divisor, you would have to treat a triplex N(squared) as 2x2=4, not 3x3=9.

In pump literature aka "Velocity Jump" causing "Joukowsky shock"
This phenomenon is best served by a "close coupled" cavitation preventer aka "suction stabilizer"

You can reduce "Velocity Jump Shock" to a generally insignificant figure, in 4 simple steps:-
  1. Select a damper with an ID 12 times the diameter of the inlet connection.
  2. Have an outlet 1/2 the area of the inlet.
  3. Increase the volume by 3 x the in-efficiency.
  4. Decrease the cushion pre-fill pressure proportionately to the volume increase, from 80% of system pressure to as low as 50%

The combined effect of mass acceleration, velocity jump, pressure wave acoustics, fittings and pipe resistance all in a time dependent frame, along with valve action, and pump characteristics maybe modeled for you by:- software. This is not a free service. Please complete input data set tabulation.

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