|
How to Read a Generic AOD Pump Curve
Step One: Identify your required TDH and flow rate
Total Discharge Head (TDH) is the energy required by your
fluid to make it through all the constrictions, bends, and appliances plus your
required pressure on the outlet side. Flow Rate is your required flux of
material. In the sample application above, TDH is Point A; flow rate is Point
B.
The BPH team can help you calculate TDH and flow rate.
These values are critical in choosing the best pump for your
application.
Step Two: Determine air pressure requirements
AOD pumps run faster with more air pressure. In the sample
application, you’ll be running at 80 PSI. Point C, the intersection of your
required TDH and flow rate lies on the 80 PSI flow curve. Please note that your
required air pressure will, in most cases, be higher than your TDH requirement.
Step Three: Determine your SCFM requirement and ensure your air compressor is
adequately sized
More flow and TDH requires more air. As
you go to the right in a flow curve, the amount of compressed air required
increases. In the sample application, just less than 15 SCFM is required,
(Point C).
Your air compressor is the driving
force behind your pump. It provides air pressure and a flow to make your pump
work at a given pressure. The table below gives the power per SFCM for rotary
compressors.
| Air Supply pressure (PSI) |
Horsepower Per SCFM (Rotary Air Compressor in good condition)
|
| 20 |
0.071
|
| 25 |
0.085
|
| 30 |
0.096
|
| 35 |
0.108
|
| 40 |
0.118
|
| 45 |
0.127
|
| 50 |
0.136
|
| 55 |
0.145
|
| 60 |
0.153
|
| 65 |
0.161
|
| 70 |
0.168
|
| 75 |
0.175
|
| 80 |
0.182
|
| 85 |
0.189
|
|
90
|
0.195
|
| 95 |
0.201
|
| 100 |
0.207
|
In the example, you're running at
80 psi, so will need 0.182 HP/SCFM. The air consumption is just less than 15
SCFM. You'll need a compressor of at least 2.73 HP (0.182 HP/SCFM * 15 SCFM
= 2.73 HP).
How to Read a Centrifugal Pump Curve

Step One: Know and identify your required TDH and flow rate
Total Discharge Head (TDH) is the energy required by your
fluid to make it through all the constrictions, bends, and appliances plus your
required pressure on the outlet side. Flow Rate is your required flux of
material. In the sample application above, TDH is Point A; flow rate is Point B.
The BPH team can help you calculate TDH and flow rate. These
values are critical in choosing the best pump for your application.
Step Two: Select the proper impeller diameter
This refers to choosing the proper flow curve for your
requirements. In the sample
application shown above, TDH and flow rate intersect at Point C, indicating that
a 2” impeller is the correct
diameter
Step Three: Size your motor
For any given (and maintained) TDH, the power the required
horsepower increases. This is because you are looking at the curve. As you follow the curve your BHP may
decrease if the TDH drops off quickly. In the sample application, a 1 HP motor
is recommended, since Point C is to the right of the 0.75 HP curve.
Step Four: Consider your efficiency requirements
Each centrifugal pump curve has a set of gradients for
efficiency. For most pumps, the best efficiency lies about 2/3 down the right
side of a curve. The greater the efficiency, the more power is converted into
flow and pressure. In the sample application, Point C indicates efficiency
greater than 50%.
If several pumps appear to meet your requirements, consider
how much power is needed to move your product. The BPH team can help you choose a pump
with the greatest efficiency in order to keep your long-term power consumption
costs down.
Step Five: Make sure you have enough NPSH
Rule of thumb: If you have a flooded inlet and low
temperature on a non-volatile fluid, you’ll have adequate NPSH the vast majority
of the time.
Fluid must move freely into your pump at your required flow
rate, without help from your pump. Expressed mathematically, NPSHa must be >
NPSHr, where NPSHa is net positive suction head available and NPSHr is net
positive suction head required. NPSH is typically expressed in units of feet of
head. Running a pump with inadequate NPSH is not a good idea. The pump will
cavitate and which will cause severe wear on the impeller and seal.
In the sample
application, the NPSHr required is found at Point D.
Common Pump Terminology
The purpose of this area is to give you a reference for some of the terms used
by pump users and manufacturers. If you don't see something you think needs to
be defined, call us at 888-289-8787 or drop us a note on the "Contact us" page.
| Term |
Definition |
| Air Consumption |
The flow rate of air that is required by an AOD pump or air
motor.
|
|
Air Pressure
|
Air-Operated Diaphragm (AOD) pumps use compressed air as a power source.
Required air pressure is a component of the flow curve. |
|
AOD
|
Air Operated Diaphragm Pump.
|
| Cavitation |
Cavitation occurs when a localized region of pressure is below
the vapor pressure of your process fluid. Your process fluid literally boils
forming bubbles and those bubbles quickly collapse-causing damage to pump
internals. Cavitation is not a problem as long as you have adequate NPSHa.
|
|
Flow Rate
|
Volume of material per unit time. This is usually expressed in units of volume
per time (e.g. gallons per minute or GPM). |
|
Head
|
The pressure in a column of liquid.
Pressure will increase as the height of the column increases. Head
refers to the height in feet; pressure refers to the psi (pressure pounds per
square inch).
|
|
NPSHa
|
Net Positive Suction Head Available. The head that your system
has available is a available on the fluid prior to entering the pump.
This is a function of the conditions in a particular installation and is
expressed in absolute units. Call us at 888-289-8787 for assistance.
|
|
NPSHr
|
Net Positive Suction Head Required. The head that the pump
requires on the inlet side to operate properly and is a function of the pump
and the position on its flow curve.
|
|
PSI
|
Pounds (force) per square inch. A common unit of pressure.
|
|
SCFM
|
Standard cubic feet per minute. A common unit of air flow.
|
|
TDH
|
Total Discharge Head. This is the required discharge pressure
plus friction losses from bends, constrictions and appliances on both sides of
your pumping system.
|
|