Pump Curve 101

Pump Knowledge · Watermain 101

Pump Curve 101
Understanding Pump Head

The complete plain-English guide to reading a pump performance curve — head, efficiency, NPSH, and the best efficiency point — with a 12-question quiz to test what you learn.

Every pump ever made comes with a chart called a performance curve. It looks intimidating — a tangle of arcs, numbers, and crossing lines — but it is really just a map. Once you can read it, you can tell at a glance whether a pump is right for your job, how much it will cost to run, and whether it will last.

This guide assumes zero prior pump knowledge. We start with the single most important idea — pump head — and build up, one piece at a time, until you can read a real curve like the one used in industrial quotes. Whether you are a contractor, a facilities manager, an engineer-in-training, or just trying to understand a quote on your desk, this page is for you.

Start Here

What Is Pump Head?

If you remember one thing from this page, make it this: head is how high a pump can push water, measured in feet.

A pump's job is to add energy to water. We could measure that energy as pressure (pounds per square inch, or PSI), but the pump industry measures it as head instead — the height, in feet, that the pump could lift a column of water straight up.

So if a pump is rated for 150 feet of head, it means: if you stood the pump at the bottom of a tall, thin pipe and turned it on, it could push water up to a height of 150 feet. That is true no matter how fast the water is flowing at that moment.

The elevator analogy

Think of a pump as an elevator for water. Head is the top floor the elevator can reach. Flow (how many gallons per minute) is how many people it can carry per trip. A pump, like an elevator, can carry a full load only to a lower floor, or a light load all the way to the top — but not both at once. That trade-off is the whole reason performance curves exist.

Why feet instead of PSI?

Because head is honest about the pump and ignores the fluid. A pump produces the same head whether it is pumping light gasoline or heavy brine — but it would produce very different pressure readings for each, because pressure depends on how heavy the fluid is. Measuring in feet lets engineers compare pumps directly without worrying about what is flowing through them.

When you do need pressure, the conversion for water is simple:

PSI = Head (feet) × 0.433 So 150 ft of head ≈ 65 PSI for water. (The 0.433 factor changes for heavier or lighter fluids.)

The Number You Actually Size On

Total Dynamic Head (TDH)

A pump doesn't just lift water straight up. It also has to fight the friction of pushing water through pipe, around bends, and through valves. Add it all together and you get Total Dynamic Head — the real workload.

"Dynamic" simply means "while things are moving." TDH is measured under flow, not when the system is sitting still. It is the single most important number when choosing a pump, and it is built from four parts:

  1. Static head — the plain vertical distance from the water source up to where it has to end up. This exists whether the water is moving or not. Lifting water from a well 50 feet down to ground level is 50 feet of static head.
  2. Friction head (friction loss) — the energy lost to friction as water scrapes through pipe, elbows, tees, and valves. This is the sneaky one: it grows with the square of flow. Double the flow and friction loss roughly quadruples. Longer runs, smaller pipe, and more fittings all make it worse.
  3. Velocity head — the energy in the motion of the water itself. Usually small, and often ignored in rough calculations.
  4. Pressure head — any pressure you need remaining at the end, such as a sprinkler or process that requires 40 PSI at the outlet.
TDH = Static Head + Friction Head + Velocity Head + Pressure Head Static head is fixed by geometry. The "dynamic" parts grow as flow increases.
The mistake everyone makes People size a pump on the vertical lift alone and forget friction. A pump might only need to lift water 50 vertical feet, but once you add the friction of a long, narrow pipe run, the real TDH could be 80 feet. Size for 80, not 50 — or the pump will never deliver the flow you expected. Because friction scales with the square of flow, get your pipe length, diameter, and fitting count right before you trust any TDH number.

The Main Event

How to Read a Performance Curve

Here is a real pump performance curve. It looks busy, but every line on it answers one specific question. We'll take them one at a time.

Pump performance curve showing head curves for three impeller diameters, red iso-efficiency islands, a rising NPSHr curve, constant-horsepower lines, and a system curve crossing the operating point.
A complete pump performance curve. Flow runs left-to-right along the bottom; head runs bottom-to-top on the left. Every other line layers more information on top of those two axes.

The two axes: flow and head

Everything starts with two measurements:

  • Flow runs along the bottom (horizontal) axis, measured in gallons per minute (GPM). This is how much water the pump moves.
  • Head runs up the left (vertical) axis, measured in feet. This is how hard the pump is pushing.

Pick any point on the chart and it tells you a flow-and-head pair: "at this many gallons per minute, the pump produces this many feet of head."

The head curves (the arcs sloping down to the right)

The smooth arcs that start high on the left and slope down to the right are head curves. Each one shows the fundamental trade-off: as flow increases, head decreases. Push more gallons and you can't push them as high — exactly like the elevator carrying a heavier load to a lower floor.

You'll usually see several head curves stacked together on one chart. Each represents a different impeller diameter — the spinning part inside the pump. A bigger impeller produces more head (a higher arc); a smaller one produces less (a lower arc). Manufacturers machine, or "trim," the impeller to a specific size to land your job right where you need it. The top arc is usually the largest impeller the pump can hold; the bottom arc is the smallest.

The efficiency islands (the concave lines that loop back)

Those curving lines with numbers like 66, 74, 80, 84 are iso-efficiency curves — "iso" just means "equal." Each line connects all the points where the pump runs at that exact efficiency. The 80 line means "the pump is 80% efficient everywhere along this line."

Think of a topographic map

Efficiency is like a hill, and these are the contour lines around its summit. The peak of the hill is the pump's most efficient operating point. The lines nest inside one another like a target or a topo map — that's why they look concave and loop back on themselves. Move away from the peak in any direction and efficiency drops, so each line wraps around to form a closed island.

Two important truths about these numbers:

  • They are not a fixed set. One pump might show 57–80; a more efficient one might show 66–87. The highest number you see is that pump's peak efficiency.
  • You will essentially never see 100. No pump is lossless. Real pump peaks land in the high 80s to low 90s for large units, lower for small ones.

Where a head curve crosses an efficiency island tells you the efficiency at that operating point. That single fact is how you judge whether a pump is a smart, low-cost choice or a wasteful one.

The Best Efficiency Point (BEP)

The center of the innermost efficiency island — the very top of the hill — is the Best Efficiency Point, or BEP. This is the flow-and-head combination where the pump runs at its absolute best: lowest energy cost, least vibration, longest life.

A good pump selection puts your operating point at or very near BEP. The healthy operating window is roughly 70% to 120% of BEP flow. Run far below BEP and you risk recirculation damage; run far above it and you waste energy and edge toward cavitation. A pump running far from BEP costs more to operate for its entire life.

The NPSH curve (the line climbing along the bottom)

NPSH stands for Net Positive Suction Head. It's about the inlet side of the pump — making sure water arrives with enough pressure that it doesn't boil into vapor bubbles and damage the pump (a destructive effect called cavitation).

  • NPSH required (NPSHr) is the line on the curve — how much suction pressure the pump needs. Notice it rises as flow increases: the harder the pump works, the more it demands at its inlet.
  • NPSH available (NPSHa) is what your system supplies. It is not on the pump curve — it comes from your installation.
The one NPSH rule NPSH available must always be greater than NPSH required (NPSHa > NPSHr), with margin to spare. If it isn't, the pump cavitates — you'll hear it sounding like it's pumping gravel, and it will chew up the impeller over time.

The horsepower lines (gray diagonals)

Some curves add gray diagonal lines labeled with horsepower (75 hp, 100 hp, 125 hp…). These are constant-power lines — they show how much power the pump draws at any flow-and-head point, which tells you what size motor you need.

The system curve (the line rising from the bottom-left)

The line that starts low on the left and climbs steeply to the right is the system curve — and this one describes your piping, not the pump. The pump maker draws the pump curves; you (or your engineer) supply the system curve from your installation's static lift, pipe size, length, and fittings.

It climbs steeply because system head is mostly friction, and friction grows with the square of flow. The single point where your system curve crosses a pump head curve is the operating point — the actual flow and head you'll get in real life. A pump doesn't choose its own flow; it runs wherever its curve meets your system curve. That's a law of the installation.

The goal of a great selection

The whole art of pump sizing is to pick an impeller so that your system curve crosses its head curve right at BEP. When that happens, you get exactly the flow you need at the lowest possible operating cost. The system curve is the tool that tests whether the manufacturer nailed it.

Quick Reference

Every Line, At a Glance

Bookmark this. The next time a curve lands on your desk, here's what each element is telling you.

Head Curves

Arcs sloping down-right. Flow vs. head for each impeller diameter. Higher arc = bigger impeller = more head.

Efficiency Islands

Nested concave loops with numbers. Each connects points of equal efficiency. Innermost = the peak (BEP).

NPSHr Curve

Lower line that rises with flow. The suction pressure the pump needs to avoid cavitation.

Horsepower Lines

Gray diagonals. Power draw at any point — tells you the motor size required.

System Curve

Rises from bottom-left. Describes your piping. Where it crosses a head curve is your real operating point.

Operating Point

The crossing of system curve and head curve. Aim for it to land on BEP.

Glossary

Key Terms in One Table

Term Plain-English Meaning Measured In
Head How high the pump can push water Feet (ft)
Flow How much water the pump moves Gallons per minute (GPM)
Static Head Plain vertical lift, source to destination Feet (ft)
Friction Head Energy lost to pipe, fittings & valves Feet (ft)
TDH Total workload: static + friction + velocity + pressure Feet (ft)
Efficiency How much input power becomes useful work Percent (%)
BEP Flow/head where the pump is most efficient A point on the curve
NPSHr Suction pressure the pump needs (avoid cavitation) Feet (ft)
NPSHa Suction pressure your system supplies Feet (ft)
System Curve Your piping's head demand at each flow A line on the chart
Operating Point Where system curve crosses the pump curve A point on the curve

Put It Into Practice

Now that you can read a curve, here are the pump lines we stock and size. Each is built for a different application — click through to explore, or call us with your flow, head, and fluid for a sized recommendation.

Goulds Water Technology

Residential & Commercial

Well pumps, booster systems, sump and sewage pumps, and end-suction centrifugals for homes, light commercial, agriculture, and municipal water.

View Goulds

Godwin Pumps

Portable Dewatering & Bypass

Diesel and electric Dri-Prime self-priming pumps for sewer bypass, construction dewatering, and flood response — priming from dry up to 28 ft of lift.

View Godwin

Flygt Pumps

Submersible Dewatering

Rugged submersible dewatering, drainage, and sludge pumps for construction, mining, and tunneling, plus emergency and bypass duty.

View Flygt Dewatering

Flygt Concertor

Intelligent Wastewater

Non-clog N-impeller wastewater pumps and the Concertor intelligent pumping system — integrated drive, self-cleaning, and IE4 efficiency for lift stations.

View Flygt Wastewater

Baker Pumps

Submersible & Well Systems

Submersible pumps, ends, motors, and packaged systems — plus pitless and booster systems for water-well and pressure applications.

View Baker

Monitor Pumps

Pitless & Booster Systems

Monitor pitless adapters and booster systems engineered for reliable water-well service and pressurized delivery.

View Monitor

Haight Rotary Gear Pumps

Positive Displacement

Rotary gear pumps for hot oil and industrial PD applications — a different pumping principle for viscous, high-pressure, low-flow duty.

View Haight

Complete Reference

Full Pump Glossary

Every common term used to describe pump performance and data — including ones that don't appear on the curve but show up on datasheets, quotes, and submittals. Grouped by what they describe.

Operating Point

Rated / Duty Point
The specific flow-and-head combination a pump is selected to deliver. The agreed target everything else is calculated around.
Flow (Capacity)Q
How much liquid the pump moves per unit time, in GPM (US) or m³/h.
Differential HeadH
The head the pump actually adds: discharge head minus suction head. The rise across the pump itself, not total elevation.
Shutoff Head
The head produced at zero flow (valve fully closed) — the highest point on a head curve.
Head Rise to Shutoff
How much head climbs from the duty point up to shutoff, as a percent. A steady rise gives stable control and avoids hunting.
Runout (End-of-Curve)
The maximum flow at the far right of the curve, where head is lowest. Running here risks motor overload and high NPSHr.

Efficiency & BEP

Efficiency
The fraction of input shaft power that becomes useful work on the fluid. The rest is lost to friction, turbulence, and recirculation.
Best Efficiency PointBEP
The flow where the pump runs most efficiently — the summit of the efficiency hill.
Flow Ratio (Rated / BEP)
Where your duty sits relative to BEP, as a percent. 100% is right on BEP; the healthy window is roughly 70–120%.
Preferred / Allowable Operating RegionPOR / AOR
Hydraulic Institute bands around BEP. POR is the sweet spot (~70–120%); AOR is the wider tolerable range. Outside AOR shortens life.
Minimum Continuous Stable FlowMCSF
The lowest flow the pump can run continuously without recirculation, vibration, and damage. Never operate below it for long.

Suction & Cavitation

Net Positive Suction HeadNPSH
The suction-side margin against cavitation, in feet.
NPSH RequiredNPSHr
The suction head the pump needs to avoid cavitation. Printed on the curve; rises with flow.
NPSH AvailableNPSHa
The suction head the system supplies. Comes from your installation, not the pump.
NPSH Margin
How much NPSHa exceeds NPSHr. Zero means no safety cushion; engineers typically want a buffer (often 2–5 ft or a ratio above 1.1–1.3).
Cavitation
Vapor bubbles forming and violently collapsing inside the pump when suction pressure drops too low. Sounds like pumping gravel; erodes the impeller.
Vapor Pressure
The pressure at which the fluid boils at its operating temperature. Hotter fluids demand more NPSHa.
Suction Pressure
Pressure at the inlet flange. "Flooded suction" feeds by gravity at positive pressure; "suction lift" pulls liquid up from below.

Speed & Geometry

Speed (Rated)
The actual running speed under load, in RPM.
Synchronous Speed
The theoretical motor speed set by electrical frequency and pole count (e.g., 1800 RPM for a 4-pole motor at 60 Hz).
Slip
The small gap between synchronous and actual speed in an induction motor under load (e.g., 1800 → 1780 RPM).
Affinity Laws
The physics linking speed and trim to performance: flow scales with speed, head with speed squared, power with speed cubed.
Impeller Diameter (Trim)
The machined diameter of the impeller selected to hit the duty point. Bigger = more head.
Trim / Diameter Ratio
The selected diameter as a fraction of the casing's maximum. Trimming much below ~70–75% of max starts hurting efficiency.
Stages
The number of impellers in series. One = single-stage; multiple stack to build higher head (deep wells, boosters).
Specific SpeedNs
A dimensionless-style index describing impeller shape (radial vs. mixed vs. axial flow) from flow, head, and speed.
Suction Specific SpeedNss
A similar index for suction/cavitation behavior. Higher values (above ~11,000) can flag recirculation risk away from BEP.

Power

Hydraulic Power (Water HP)
The useful power delivered to the fluid (flow × head × specific gravity). The theoretical minimum before losses.
Shaft / Brake HorsepowerBHP
The actual power the motor must deliver to the shaft: hydraulic power divided by efficiency. Always higher than hydraulic power.
Power, Maximum (Rated Diameter)
The peak shaft power anywhere along the selected impeller's curve. Drives motor sizing so it isn't overloaded at any point.
Minimum Recommended Motor
The next standard motor frame above the maximum power, with margin (e.g., 112 hp duty → 125 hp motor).
Service FactorSF
How much a motor can run above nameplate continuously (1.15 = 15% overload capacity). A buffer, not a place to live.

Pressure & Fluid

Maximum Working Pressure
The highest pressure the pump sees in service (typically shutoff head plus suction pressure, converted to PSI).
Maximum Allowable Working PressureMAWP
The casing's rated pressure limit, set by material and flange class (e.g., 285 PSI for 150# carbon steel). Service pressure must stay well below it.
Hydrostatic Test Pressure
The factory leak/strength test pressure, usually 1.5 × MAWP.
Specific GravitySG
The fluid's weight relative to water (water = 1.0). Heavier fluids raise pressure and power for the same head.
Viscosity
The fluid's resistance to flow, in centipoise (cP). Higher viscosity lowers flow, head, and efficiency.
Viscosity Correction FactorsCq/Ch/Ce/Cn
ANSI/HI multipliers that derate flow, head, efficiency, and power for fluids thicker than water. All 1.00 for water.
A note on the numbers Typical thresholds above — POR ~70–120% of BEP, Nss ~11,000, NPSH margin 2–5 ft — are common rules of thumb. Exact values vary by standard, manufacturer, and application. Treat them as orientation, not hard limits, and confirm against the specific pump's documentation.

Test Your Knowledge

12 questions on everything above. Pick an answer for each, then hit Score My Quiz to see your results and an explanation for every question.

Question 1 of 12

What does “pump head” measure?

ExplanationHead is the height, in feet, that a pump can raise water — a measure of the pump’s energy output, independent of the fluid’s weight.

Question 2 of 12

Why does the pump industry measure energy as head (feet) instead of pressure (PSI)?

ExplanationA pump produces the same head for any fluid, but different pressures depending on fluid weight. Head lets engineers compare pumps directly.

Question 3 of 12

Roughly how do you convert head in feet to PSI for water?

ExplanationFor water, PSI = head (ft) × 0.433. So 150 ft of head is about 65 PSI.

Question 4 of 12

What is Total Dynamic Head (TDH)?

ExplanationTDH is the full workload — static head plus friction, velocity, and any required discharge pressure. It’s the number you size a pump on.

Question 5 of 12

How does friction loss change as flow increases?

ExplanationFriction loss scales with the square of flow — double the flow and friction roughly quadruples. It’s the part people most often underestimate.

Question 6 of 12

On a performance curve, what happens to head as flow increases along a single head curve?

ExplanationThe fundamental trade-off: more flow means less head. That’s why head curves slope down to the right — like an elevator carrying a heavier load to a lower floor.

Question 7 of 12

Why does a single curve usually show several stacked head curves?

ExplanationEach arc is a different impeller (trim) diameter. A bigger impeller produces more head (higher arc); a smaller one produces less.

Question 8 of 12

What do the nested concave lines labeled with numbers like 66, 74, 80 represent?

ExplanationThey’re iso-efficiency islands. Each line connects points of equal efficiency, nested like a topographic map around the peak.

Question 9 of 12

What is the Best Efficiency Point (BEP)?

ExplanationBEP is the top of the efficiency hill — lowest energy cost, least wear. A good selection places the operating point at or near BEP.

Question 10 of 12

What is the one rule that must always hold for NPSH?

ExplanationNPSHa must always be greater than NPSHr, with margin. If not, the pump cavitates — it sounds like pumping gravel and damages the impeller.

Question 11 of 12

Who provides the system curve, and what does it describe?

ExplanationThe system curve comes from your installation — static lift, pipe size, length, and fittings. The pump maker draws the pump curves; you supply the system curve.

Question 12 of 12

On the chart, what does the operating point represent?

ExplanationA pump runs wherever its head curve meets your system curve. That crossing is the actual operating point — ideally landing right on BEP.

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