Apr 13, 2026
A pump curve is a performance map. It shows how a pump will behave as flow changes. To read it, start by choosing your target flow rate on the horizontal axis, move up to the pump's curve, and then read across the other lines to understand head or pressure, efficiency, power draw, NPSHr, and, in AODD applications, the air pressure and air consumption required to hit that operating point.
Contributors
This blog was developed using insights from PSG® subject-matter experts who regularly help customers size pumps when specs are incomplete, viscosity changes, or system conditions are less than ideal. It also references PSG® manufacturer resources that explain both centrifugal and AODD performance curves.
Pump curves matter because they turn pump selection from guesswork into a system decision. A curve shows what the pump can actually do across a range of operating points, not just what it can do at one ideal condition. That matters because a pump that looks correct on paper can still miss the application if the flow, pressure, viscosity, suction conditions, or air supply are different than expected.
PSG's® Griswold® pump performance curve overview and AODD pump performance curve article both make the same point in different ways: a curve helps you find the pump's usable operating range, not just its theoretical maximum.
The phrase "pump curve" can describe different chart styles depending on the pump technology. If you do not identify the curve type first, it is easy to read the wrong variables and choose the wrong pump.
The two most common curve types your readers will run into are:
Centrifugal pump curves: usually focused on flow, head, efficiency, power, and NPSHr.
AODD pump curves: usually focused on flow, discharge pressure, air inlet pressure, and air consumption.
For a centrifugal example, see Griswold's® complete guide to centrifugal pumps. For an AODD-specific example, see How Understanding AODD Pump Performance Curves Optimizes Operations.
A centrifugal pump curve is usually the chart people picture first. Even if it looks busy, it becomes manageable once you break it into layers.
Here is the basic reading order:
• Step 1: Find the required flow rate on the horizontal axis (usually gpm).
• Step 2: Move vertically until you hit the pump's impeller trim curve.
• Step 3: Read horizontally to the left-hand axis to see how much head the pump produces at that flow.
• Step 4: Check where that same point falls against the efficiency lines to see how efficiently the pump runs there.
• Step 5: Check the power line to understand motor load.
• Step 6: Check the NPSHr line to see what suction margin the pump needs to avoid cavitation.
Griswold® explains this directly in its centrifugal pump guide: the left axis is head in feet, the bottom axis is flow, efficiency is shown on the right axis, power is shown on a separate axis, and NPSHr is plotted in feet below the chart.
If you want readers to understand a curve quickly, these are the terms that matter most:
• Head: the pressure energy the pump adds to the liquid, usually shown in feet of head.
• Impeller trim: the specific impeller diameter that defines that performance line.
• Efficiency: how effectively the pump converts input energy into useful hydraulic work.
• BHP or power: how much horsepower or kilowatts the motor must deliver at that point.
• NPSHr: the minimum suction margin the pump requires to avoid unacceptable cavitation.
Readers often assume the main flow/head line is the whole story. It is not. The supporting lines are what tell you whether the pump can run reliably at that point once real system conditions are considered.
Best Efficiency Point, or BEP, is the operating point where the pump is most efficient. It is also usually the point where vibration, radial load, and mechanical stress are lowest. That makes BEP more than an energy metric - it is a reliability metric.
Griswold notes in its centrifugal pump guide that pumps running at BEP generally see the lowest radial loads and lowest vibration levels, while moving away from BEP increases shaft loading, vibration, and wear.
That is why a good pump selection is usually not the point where the curve says the pump can technically run. It is the point where the curve says the pump can run well.
Some pump curves show more than one impeller trim or more than one speed. These are composite curves. They help you compare multiple operating envelopes on one chart.
A composite curve usually adds:
• Multiple trim lines or speed lines.
• Iso-efficiency lines that arc between trim lines.
• Iso-power lines that help estimate motor load at different operating points.
• A separate NPSHr section tied to the selected trim.
PSG® covers this in Griswold's® composite performance curve article, which explains how published composite data helps estimate head, efficiency, power, and NPSHr for varying trim sizes or speeds.
AODD curves look different because they reflect an air-driven pump, not a motor-driven centrifugal pump. That means the curve is not just telling you what the pump can move - it is also telling you what air supply you must deliver to make that performance possible.
A practical reading order for an AODD curve is:
• Step 1: Find your target discharge flow on the horizontal axis.
• Step 2: Move to the required discharge pressure on the vertical axis.
• Step 3: Use the curved air-pressure line to determine the inlet air pressure needed.
• Step 4: Use the air-consumption line to estimate SCFM required at that operating point.
PSG's® AODD curve article explains that AODD charts typically use flow on the horizontal axis, pressure on the vertical axis, a curved line for air inlet pressure, and another curved line for air consumption in SCFM.
One of the most common misunderstandings in AODD selection is assuming PSI alone determines output. In practice, air-operated pumps need both pressure and air volume. A curve helps reveal that because the operating point is tied not just to discharge pressure, but also to air consumption.
This is exactly why AODD curves are useful in troubleshooting. If the curve says the pump needs more SCFM than the compressor or air plumbing can actually deliver, the pump may never reach the expected flow even if the regulator shows high PSI.
For a broader AODD refresher, see the AODD technology page.
Running a pump away from its best efficiency point accelerates wear on impellers, diaphragms, check valves and internal clearances. When performance starts to drift from what the curve predicts, replacing worn components with genuine parts restores the geometry and tolerances that keep the pump operating where it was designed to.
In diaphragm pump applications, not every curve is interchangeable. Different diaphragm materials and stroke configurations can change the shape of the performance curve. That means two pumps that look similar by size can perform differently depending on how they are configured.
This matters most when readers are trying to compare flow curves from manuals. If they are looking at a rubber curve, a TPE curve, or a PTFE curve, they may be looking at different performance envelopes for the same basic pump size.
A pump curve is only as accurate as the fluid assumptions behind it. Water-like fluids and thick fluids do not behave the same. As viscosity rises, friction losses increase and the required energy to move the liquid increases too. In the real world, that can move the application farther to the right on the curve or even push it off the practical curve entirely.
This is why curve reading should never be separated from the actual fluid. If the application is more viscous than the baseline assumption, the right response is not to force the same point on the same curve - it is to re-evaluate the pump size, the technology, or the piping.
A pump curve tells you what the pump can do. A system curve tells you what the system demands as flow changes. The actual operating point is where those two curves intersect.
That is often missed. Try not to focus only on the pump chart, because the piping, elevation, fittings, static head, and friction losses determine where the pump will really land. In practice, you are never selecting a pump in isolation - you are matching a pump curve to a system curve.
This is also why changing pipe size, reducing restrictions, or changing viscosity can shift the operating point without changing the pump itself.
These are the biggest errors that lead to misapplication:
• Using only the maximum flow number instead of the actual operating point.
• Ignoring BEP and selecting a point far to the left or right of the healthy zone.
• Reading head or pressure correctly but ignoring NPSHr, which can lead to cavitation.
• Comparing AODD curves without accounting for air supply limitations.
• Assuming a water-like curve still applies when viscosity rises significantly.
• Using the pump curve without accounting for actual piping friction and system demand.
If you want real curve data instead of generic diagrams, PSG® offers both educational resources and product-specific performance coverage. Good starting points include Griswold's® 811 ANSI series page for centrifugal performance coverage and product pages like Wilden's® P200 or Wilden's® P400 for specific AODD product information.
For a faster path to the right pump, you can also start with the Pump Finder and then confirm the final operating point against the appropriate performance data.
If you need a simple way to explain pump curves to non-engineers, use this formula: "Pick the flow you need, confirm the pressure or head you must overcome, then check whether the pump can do it efficiently and reliably at that point." That keeps the explanation practical without oversimplifying what the chart is doing.
The curve is not there to show the pump's biggest claim. It is there to show whether the pump can meet the job under real operating conditions.
If you need help matching a curve to a real application, contact the PSG® Store team.
You can also browse by brand: Shop Wilden® and Shop All-Flo®.
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Rob Jack is a long-tenured technical authority in AODD pumps with extensive experience interpreting diaphragm-pump flow curves, material-specific curve differences, and how viscosity changes practical AODD sizing decisions.
Piyush Kapoor is a rotating equipment specialist focused on reliability, selection, and lifecycle performance. His work frequently centers on helping buyers and engineers translate application inputs like flow, pressure, and viscosity into the right pump selection tools and performance data.
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