Where Ha = Atmosphere Head is the head or pressure (pressure is measured in feet of head) on the surface of the liquid in the tank that we are pumping out. In an open system like this, it will be atmospheric pressure, 14.7 psi or 34 feet of water.
Hs = the vertical distance, measured in feet, between the free surface of the liquid to the centerline of the pump impeller. If the liquid is below the pump, this becomes a negative value.
Hvp = the vapor pressure of the liquid at the pumping temperature, expressed in feet of head.
Hf = the friction losses in the suction piping, expressed in feet of head.
To put this formula in simpler terms think of NPSHA as being the result of atmospheric head (pressure) pushing the fluid into the pump. The pump gains additional inlet head or pressure if the liquid level is above the pump inlet or minus head if the liquid level is below the pump. The fluid weight creates the pressure. The pump loses inlet head or pressure from friction loss of the fluid moving through the suction pipe (small pipes or long pipes have a lot of friction). And finally the inlet head or pressure is reduced by vapor pressure. This is an issue if the fluid is evaporates easily or is very hot. So NPSHA is atmosphere head plus or minus
One final note about NPSHR for a pump. Many pump manufacturers provide NPSHR curves for their pumps. This curve is determined in labs using methodology as set forth by Hydraulic Institute. The various points on this curve are determined by restricting the inlet pressure with a valve. The restricted inlet pressure creates loss of flow or cavitation. The NPSHR curve is drawn based upon the pump losing three percent of its rated flow. At various flow points a vacuum reading is taken on the inlet of the pump. These points are plotted below the pump curve showing the minimum inlet pressure the pump needs, but by definition this lost flow really is vapor bubbles and the pump is being damaged. When installing a pump, insure that the inlet conditions are well above the NPSHR requirements of the pump.
Rule #2. REDUCE THE FRICTION LOSSES
When a pump is taking its suction from a tank, it should be located as close to the tank as possible. This reduces friction losses on the NPSH Available. However, the pump must be far enough away that proper piping can supplied to the pump. Proper piping means that a straight shot of pipe is supplied to the pump that is at least ten (10) diameters of the pipe. We can this the 10D Rule. For example a minimum of 20” of straight pipe must be immediately in front of the pump if the inlet pipe is 2” in diameter. Pipe friction is reduced by using a larger diameter pipe. This limits the linear velocity, hence the friction losses. Many industries use 5 to 7 feet/sec., but this is not always possible.
Rule #3. NO ELBOWS ON THE SUCTION INLET
It is never acceptable to install an elbow on a suction flange! There is always an uneven flow in an elbow. When it is installed at the suction inlet of the pump, it introduces an uneven flow into the eye of the impeller. This can introduce turbulence and air entrainment, which may result in impeller damage and vibration. The only thing worse than an elbow on inlet of a pump is two elbows. As mentioned above, the established method of ensuring a laminar flow to the inlet of the pump is using the 10D rule, straight pipe into the pump. This also means no valves, reducers, tees, etc.
Rule #4. STOP AIR OR VAPOR FROM ENTERING THE SUCTION LINE
Always check the suction line for leaks. As the pump operates it creates a partial vacuum, which will suck air into the suction line. This will create an effect similar to cavitation and with the same results. Another source of air in the suction line is the return line in the tank if the pump is re-circulating the fluid through a system. If the return line or supply line is above the tank liquid level, the liquid will become very become aerated. This is a huge issue. Aerated tanks damage the pump just by creating cavitation like conditions for the pump. The fix is to submerge the return or supply line. Return lines in the tank can be to close to the outlet nozzle on the tank and can create the same issue. The solution is relocating the return line or baffling the tank.
The presence of an air pocket in the suction line is another example of a cause for pump troubles, which should never happen. Any high point in the suction line can become filled with air and interfere with proper operation of the pump. This is particularly true when the liquid being pumped contains an appreciable amount of air in the solution or of entrained air and the pump is handling a suction lift. Long suction lines are too frequently installed with improper pitch or with humps and high spots, where air can accumulate. If the liquid supply is below the pump the suction line should run up to the pump. Straight reducers are definitely a no-no. Use an eccentric reducer, mounted with the flat portion on top and sloping portion on the bottom. Install the other way around if source of supply is above pump.
Another common problem is pumping a tank to low or having a short tank that in general has low liquid levels above the outlet nozzle of the tank. If a pump is taking its suction from a tank with low liquid levels, the formation of vortices can draw air into the suction line and hence the pump. Vorticing can be eliminated, by installing a low liquid level sensor to turn off the pump. Alternatively, install a bell-mouth connection on the tank opening to lower the velocity on the tank outlet nozzle, hence lowering the liquid level requirements to keep the tank from vorticing. Or a vortex breaker can be installed on the discharge nozzle of the tank. They look very similar to the drain stopper in a modern bathroom sink, except the diameter of the top round disk on top is 1½ times the size of the ID of the tank discharge nozzle. Placing the tank outlet nozzle near the wall of the tank will also help break a vortex.
The following table shows the minimum submergence required over opening unless some of the suggested solutions mentioned above are employed:
To put this formula in simpler terms think of NPSHA as being the result of atmospheric head (pressure) pushing the fluid into the pump. The pump gains additional inlet head or pressure if the liquid level is above the pump inlet or minus head if the liquid level is below the pump. The fluid weight creates the pressure. The pump loses inlet head or pressure from friction loss of the fluid moving through the suction pipe (small pipes or long pipes have a lot of friction). And finally the inlet head or pressure is reduced by vapor pressure. This is an issue if the fluid is evaporates easily or is very hot. So NPSHA is atmosphere head plus or minusThe following table shows the minimum submergence required over opening unless some of the suggested solutions mentioned above are employed:
Want more information on HS Slurry Pump? Click the link below to contact us.