Years ago, making a pump selection meant sitting down with large printed catalogs and flipping through them until you reached a pump curve that fit a project’s hydraulic requirements. Today this process is made much easier through the use of electronic pump curve catalogs. One of the most well-known developers of electronic pump catalogs is Engineered Software and their pump selection software pump-flo. Another popular option for pump selection software is Intelliquip.
All of the curves in this article were generated by Pump-Flo’s web-based pump selection software.
What is a Pump Curve?
A pump curve is a graphical representation of the performance characteristics of a pump.
A pump curve provides a wealth of information regarding the performance capabilities of a pump. Information is plotted on an x-y graph where the x-axis is measured in units of flow and the y-axis is measured in units of head, power, and NPSHr.
For the sake of example, today we’re going to look at a selection made for the following design condition: 1,000 GPM at 100 ft.
Here is one possible pump selection that might be a good fit for that operating condition:
Head & Flow
The first piece of information provided by a pump curve is the flow that the pump will develop at any given operating head. The curve that provides this information is called the pump performance curve. Some pump curves only provide a single pump performance curve, but most will provide the maximum performance the pump is capable of achieving with a full-trim impeller, the minimum performance the pump is capable of achieving with a minimum-trim impeller, and the performance provided by the design-trim impeller.
The design-trim impeller is the impeller trim the pump selection software has selected as the closest fit to the design condition provided. In this case, the design-trim is 16.3125”, the max-trim is 17” and the minimum-trim is 15”. We know this by looking at the left-hand side of the curve where these three numbers appear.
Considering the design trim curve we see that at zero flow, also known as shutoff or dead-head, the pump will develop about 130 ft of head. This is the head the pump would develop if it were operating against a closed valve.
Keep in mind that the actual pressure measured between the pump and the closed valve might exceed this value because a pump ADDS head to the liquid being pumped. In other words, if this pump were operating at shutoff with suction pressure of 20 feet the total head experienced at the pump discharge flange would be 150 ft (20 ft + 130 ft).
Considering the design trim impeller, we see that the following things are true:
- Shutoff (a.k.a. zero-flow or dead-head) occurs at about 130 ft.
- The design condition falls very close to the pumps best-efficiency-point (BEP).
- Provided there is adequate NPSHa, the pump will operate down to approximately 60 ft of head and produce a flow of approximately 1380 GPM at 60 ft.
The maximum (17″) and minimum (15″) trim curves also tell us the possible conditions that the pump could be modified to meet in the future by installing an impeller of a larger or smaller different trim.
In addition to head and flow, most pump performance curves will also provide efficiency information.
The efficiency of a pump is the relationship between the input horsepower required to drive the pump at a given operating condition, and the water horsepower being created by the pump.
If a pump were 100% efficient then the input power required would be equal to the water horsepower being generated by the pump. However, since no pump is 100% efficient, every pump will require more input power than it will generate in water horsepower.
In the case of this pump, the best-efficiency-point (BEP) falls at approximately 1075 GPM at 95 Ft, and efficiency at BEP is 84.1%.
The Preferred Operating Range
Special attention should be paid to the location of BEP relative to the operating condition. Pumps run best at or near BEP. For this reason the Hydraulic Institute (HI) has defined a pumps Preferred Operating Region (POR) as flows from 70% to 120% of flow at BEP for most centrifugal pumps.
The POR for this pump stretches from approximately 750 GPM to 1290 GPM which is 70% to 120% of 1075 GPM.
It is best to select a pump that will operate most of the time in the POR since this will have implications for pump life and power consumption. For some pumps with high specific speed (Ns) impellers, the POR is smaller – 85% to 110% of BEP. You can read more about specific speed in our article about pump casings and impellers.
The Allowable Operating Range
There is another region of operation that is defined by the pump manufacturer rather than by a standards organizations such as HI: the Allowable Operating Region (AOR). In our example curve, the AOR is indicated by the portion of the curve shaded in light yellow. This is the region that the pump manufacturer has determined comprises all of the points that this pump can operate at continuously.
While it is preferable to select pumps to operate within the POR, pumps should always be selected to operate within the AOR without exception. Very short-term operation outside of the AOR might be acceptable, but the pump manufacturer should be consulted before selecting a pump that will see intermittent operation outside the confines of the AOR.
Minimum Continuous Stable Flow & the System Curve
The example pump performance curve above has two more items which should be mentioned.
First, the red line on the left hand side of the pump curve is the Minimum Continuous Stable Flow (MCSF) line. This is the point beyond which the pump manufacturer has determined the pump should not be allowed to operate for any extended period of time.
Second, the blue curve beginning at 0 GPM and 0 Ft and extending through the design condition is the System Curve and represents the operation of the system in which the pump is being applied.
System curve information should be provided by the Engineer designing the pump system. In the pump selection software, the system curve can be manipulated by manually entering data points, and is particularly useful when evaluating the variable-speed performance of a pump.
Net Positive Suction Head Required (NPSHr)
The next part of the pump curve is the Net Positive Suction Head Required (NPSHr) curve. The NPSHr curve provides information about the suction characteristics of the pump at different flows. The x-axis is still measured in flow units, but the y-axis is now measured in feet of NPSHr. Each point along the curve identifies the NPSHr required by the pump at that flow to avoid cavitation issues that would be damaging to the pump and would have a negative impact on overall pump performance.
Looking back at our example design flow of 1,000 GPM we can see that this pump will require approximately 7 ft of NPSHr at that condition. A typical safety margin between Net Positive Suction Head Available (NPSHa) and required (NPSHr) is 5 ft. So in this case it would generally be recommended that this pump not be applied in applications where NPSHa at the design flow of 1,000 GPM is less than approximately 12 ft.
Generally speaking NPSHr does not vary dramatically between variations in impeller trim which is why we do not see separate curves for the minimum and maximum impeller trims. Those curves are actually present, but they are overlaid by the design-trim NPSHr curve.
The final portion of the pump curve is the power curve. Once again the x-axis is measured in units of flow, but the y-axis is now measured in power units. In this case the unit of measurement is horsepower, but in the case of an application measured in metric units, power is typically measured in kilowatts. This curve tells us how much power the pump will demand at any particular flow point. This information is useful in ensuring the selected motor is suitably sized, and is also useful when calculating power consumption costs.
At our design flow of 1,000 GPM, we can see that power demand is approximately 30 HP and that power demand is greatest at approximately 1,300 GPM. Based on this information, if the pump were to be driven by an electric motor, most pump manufacturer’s would recommend that the next largest motor rating be used. In this case that would be a motor rated for 40 HP.
Power demands vary considerably depending on the impeller trim. This is why separate power curves for the minimum and maximum impeller trims can also be seen in the power curve. This information is useful if the customer would like to size the drive unit to allow a future increase in capacity without requiring replacement of the drive unit. In that case, the customer could chose to size the drive unit for the maximum trim power curve, and at a later date the capacity of the pump could be increased by installing a maximum trim impeller without requiring replacement of the drive unit. In the case of our example pump curve, the motor required by the design trim impeller will be adequate to cover the power demanded by the maximum trim impeller, but this will not always be the case.
When combined, these three curves are called the composite pump curve, and they provide the information we need to determine if a particular pump is a suitable selection for the hydraulic requirements of an application. Understanding the information communicated by each part of the curve is critical to ensuring that the pump selected is a good fit for the application’s hydraulics.
4 thoughts on “How to Read a Pump Curve”
“The first piece of information provided by a pump curve is the flow that the pump will develop at any given operating head”
I think it is more accurate to say ” ..the generated head at any given flow”
since the variable in the x-axis is always the independent variable.
Very good article. Refer to the Pump Performance Curve, it would be clear for reader if the Pump Curve are labelled. Eg the Blue Curve from 0,0 –>100,1000 this iscalled “Pump Performance Curve” ? The other convex curve, these called “Impeller Curves”, and intersection gives the impeller choice for the pump performance?
– is this correct statement?
The quesry is on the NPSH (available)
If the water level is below the pump centre then shouldnt the NPSH (available) = 33 feet (Atmos Pressure) – suction head ?
Thank you. This article has been very helpful it simplifies Pump Curves.