Water supply

Private Well Supply and Pressure Tanks

How drawdown volume and pump cycle rate govern every sizing, setting and commissioning decision on a private well water supply.
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The tank does not store water, it stores starts

A pressure tank on a private well is misunderstood the moment anyone calls it storage. Its water volume is almost irrelevant to supply; a household will drain the largest tank most contractors install in well under a minute of a running hose. What it actually holds is a delay — the interval between the pump shutting off and the pump starting again. Every gallon of drawdown buys a few more seconds of that delay, and the number of seconds is the whole design.

Pump motors fail on starts, not on hours. Inrush current at start is several times running current, and the heat from that inrush is dumped into the windings before the motor comes up to speed and flow past the motor can carry it away. A submersible motor sitting in a well is cooled by water moving up past the shell; during starting there is no flow yet. Stack enough starts close together and the winding insulation degrades, the thrust bearing takes repeated unloaded hits, and the control box or drive capacitors age at the same rate. A motor that runs continuously for hours is under far less stress than one that starts eighty times an hour.

So the working currency on a well job is cycles per hour and minimum run time per cycle. Manufacturers publish a maximum starts-per-hour figure for each motor size and a minimum run time, and those two numbers, not the tank's nameplate capacity, are what the sizing has to satisfy. Larger horsepower motors tolerate fewer starts than small ones — the trend runs the wrong way from what most people assume, because the bigger machine has more rotating mass and more inrush to dissipate. Confirm the figure for the specific motor going down the well rather than carrying a habit from the last job.

There is a second reason this framing matters on site. Almost every complaint a homeowner reports about a well — pulsing showers, a pump audibly kicking every few seconds, a pressure switch that chatters, a system that trips a breaker on hot afternoons — resolves to the same root: not enough drawdown between the cut-in and cut-out points. Diagnose in the language of cycles and the fault becomes obvious. Diagnose in the language of tank size and you end up selling a bigger tank that does not fix a waterlogged bladder or a pressure switch set two psi (0.14 bar) apart.

Because drawdown rather than tank volume is the number that controls cycle rate, work it out before choosing a tank instead of after.

Your well pump's rated flow rate.

The shortest the pump should run per cycle to avoid premature wear.

Recommended tank size

30.3 gal

Medium confidence

Actual drawdown fraction varies by tank precharge pressure and your specific pressure switch cut-in/cut-out settings — check your tank manufacturer's drawdown chart for a precise figure.

Required drawdown
10 gal

Estimated cost — your price

This site holds no price list for this material — local prices vary too much to publish honestly. Enter your supplier's price and the result is costed with it.

What this calculation does not cover

  • The 33% usable fraction is a fixed assumption, not something this calculates. Real drawdown depends on the tank's air precharge and on your pressure switch's cut-in/cut-out settings, and the usable fraction shrinks as the switch band moves higher — so a tank set up at a high pressure band delivers less than this assumes. Check the manufacturer's drawdown chart for the model and switch setting you are actually running.
  • It treats the pump's rated flow as a constant. A pump's delivered flow changes with the head it is working against and rises and falls across the cut-in to cut-out band, so the flow moving through the tank over a real cycle is not the nameplate figure this uses.
  • This sizes a tank against pump cycling and nothing else. It does not look at the well's yield or recovery rate, or at peak simultaneous household demand — a tank large enough to stop short-cycling can still be far too small for a low-yield well or a heavy draw, and that is a storage problem this rule does not address.
  • The fixed fraction describes a captive-air tank (bladder or diaphragm). It does not apply to a galvanized air-over-water tank, whose air charge dissolves into the water and needs periodic recharging, nor to a constant-pressure or VFD system, which is deliberately paired with a small tank and is not sized this way.
  • This is not an installation specification. It says nothing about the tank's pressure rating against the relief valve setting, the stand or floor loading, freeze protection, the tank tee and pipework, or the well and plumbing code requirements that govern the installation.

Drawdown is what the switch differential lets you have

Drawdown is the water that leaves the tank between cut-out pressure and cut-in pressure. Note what that definition excludes: the water still sitting in the tank at cut-in, which never participates, and the air charge, which does the pushing. A tank rated at a nominal volume delivers only a fraction of that as drawdown, and the fraction shrinks as system pressure rises. The same tank on a 40/60 setting (2.8/4.1 bar) gives noticeably more drawdown than on a 50/70 setting (3.4/4.8 bar), because the ratio between the absolute pressures at cut-in and cut-out governs how much of the air charge expands.

This catches people out on jobs with a long vertical run or a demanding fixture group, where the natural instinct is to raise both switch settings. Raising the pair without widening the gap costs drawdown and buys extra cycles. Widening the differential — moving from a 20 psi (1.4 bar) gap to a 30 psi (2.1 bar) gap — recovers it, at the cost of a more noticeable pressure swing at the fixtures. That trade sits at the centre of most commissioning arguments, and there is no universally right answer: a house with thermostatic shower valves tolerates a wide swing badly, while an irrigation-heavy property barely notices.

Pre-charge is the other half. A bladder or diaphragm tank wants its air charge set a couple of psi below cut-in, measured with the tank isolated and drained so the water side is at zero. Set it high and the tank runs out of water early — drawdown collapses and cycle rate climbs. Set it low and water sits permanently in the bottom of the tank doing nothing while the bladder never fully relaxes, which shortens its life. Charge with the pump off and the drain open, every time, and re-check pre-charge whenever the switch settings change. Adjusting a switch without re-charging the tank is one of the most common reasons a system cycles worse after a service visit than before it.

Old galvanised tanks without a bladder behave differently again. The air is in direct contact with the water and dissolves into it steadily, so the tank waterlogs and drawdown falls to almost nothing over months. That is what air volume controls and snifter valves existed to counter. If one of these is still in service, expect the cycle complaint to be seasonal and progressive rather than sudden — and expect the fix to be either restoring the air-charging arrangement or replacing with a bladder type.

A switch is marked in psi and a well is measured in feet, and the two have to be the same statement before a cut-in setting means anything at the wellhead.

The vertical height of the water column, in feet.

Static pressure

43.35 psi

High confidence

1 ft of water at 4 °C = 62.428 lb/ft³ ÷ 144 in²/ft² ≈ 0.4335 psi. Equivalently, 2.31 ft per psi. Assumes clean water at 4 °C. For any other fluid, multiply by its specific gravity.

Head entered
100 ft
Pressure
43.35 psi
Metric equivalent
43.35 psi
Bar
2.99 bar

Add the equipment this sizes

This result is a specification — 43.35 psi — not a quantity. Put the thing it sizes into your project: how many, what you call it, and your supplier’s price.

What this calculation does not cover

  • This is static head only. Friction loss through pipe, fittings, valves and the meter, and the residual pressure a fixture, shower or sprinkler head needs to work, are all excluded. Total dynamic head is static head plus those two, and sizing a pump on this figure alone is how a system ends up short at the top outlet.
  • The factor assumes clean water at 4 °C and the result does not scale for any other fluid. Glycol, brine, fuel oil and hot circulating water all differ in density, so multiply by specific gravity yourself — a strong glycol charge reads low here, hot heating water reads high.
  • It describes a column at rest. Velocity head, a pump running near shut-off, thermal expansion in a closed circuit and water hammer on valve closure can all push real system pressure well above this figure, and it is the peak, not the static value, that splits a fitting or lifts a relief valve.
  • Only the water column's own pressure is counted. Fill pressure in a sealed heating circuit, an expansion vessel's charge, a booster set's outlet pressure or gas pressure above the water in a closed tank all add on top of this number and none of them are in it.
  • This is not a pressure rating check and not a pump selection. It says nothing about the pressure class of the pipe, fittings, cylinder or appliance at the bottom of the lift, and nothing about NPSH available at a pump suction — cavitation is governed by suction conditions, not by the discharge head being converted here.

Pumps are catalogued in feet of head; gauges and fixtures are rated in psi. Converting between them is the moment a pump curve becomes a check you can carry out with a gauge, and it is where a system that looked adequate on paper turns out to be 15 psi short at the top floor.

What the well itself will give you

No tank arrangement can compensate for a pump that outruns the aquifer. Set a pump that delivers more than the well's sustainable yield and it draws the water level down to the pump intake, breaks suction, and either cycles on a low-pressure cut-off or runs dry and cooks the motor. The cycle count then goes vertical for a reason that has nothing to do with the tank, which is why yield gets checked before anything downstream is specified.

The number that matters is not the driller's flush-test figure taken over twenty minutes. It is the rate the well will sustain with the water level stabilised — static level, pumping level, and the drawdown in the borehole itself over a run long enough for the cone of depression to settle. A well that gives a healthy figure for half an hour and half that after four hours will be sized wrong if the short test is believed. Where the well is marginal, the answer is usually a lower-output pump plus atmospheric storage with a booster set, not a bigger pressure tank; the pressure tank cannot manufacture water the formation will not give.

Seasonal variation deserves the same scepticism. Static levels in shallow wells move with rainfall and with neighbouring abstraction, and a system commissioned in a wet spring can start short-cycling on low water in late summer. Record static and pumping levels at commissioning and leave them with the homeowner, because the comparison a year later is what separates a failing pump from a falling water table.

Sanitary construction sits alongside yield as a non-negotiable. Grout seal, casing height above finished grade, a vermin-proof and watertight well cap, and separation distances from septic fields and other contamination sources are governed by state or provincial well-construction codes and local health authorities, and the required distances differ substantially between jurisdictions — verify against the authority having jurisdiction rather than a remembered figure. NSF/ANSI/CAN 61, Drinking Water System Components – Health Effects, is the standard normally invoked for wetted materials; where a pitless adaptor is used, its listing should be confirmed rather than assumed.

Before any pump or tank is specified, this establishes the sustainable yield the aquifer will actually support, which is the ceiling every downstream cycling decision sits under.

The aquifer's hydraulic conductivity.

The undisturbed saturated aquifer thickness far from the well.

The remaining saturated thickness right at the pumping well, after drawdown.

The radius at which h1 is measured (often the radius of influence).

The radius of the pumping well itself.

Estimated well yield

44.7 gal/min

Medium confidence

This is a steady-state estimate assuming a fully penetrating well in a homogeneous, isotropic unconfined aquifer — real dewatering systems are affected by partial penetration, aquifer boundaries, and non-steady flow, and should be verified with an actual pump test.

Equivalent in m³/day
243.51 m³/day
Equivalent in US gallons per minute
44.67 gpm

Add the equipment this sizes

This result is a specification — 44.7 gal/min — not a quantity. Put the thing it sizes into your project: how many, what you call it, and your supplier’s price.

330 ft
Schematic, drawn to the proportions you entered — not to scale on screen.

What this calculation does not cover

  • The equation covers one fully penetrating well pumping on its own. It does not add the drawdown cones of neighbouring wells or wellpoints, so it cannot tell you how many wells an excavation needs or how far apart to set them — in a ring or a line each well delivers less than this figure.
  • Steady state only, in a homogeneous, isotropic, unconfined aquifer. There is no time in the arithmetic, so the higher rate while the cone is still developing and the total volume pumped over the job both sit outside it, as do partial penetration, layered or anisotropic ground, confined and leaky aquifers, and any recharge or no-flow boundary such as a river, a cut-off wall or bedrock.
  • This is a planning-level flow estimate, not a dewatering design and not a pump specification. Screen entrance velocity, filter pack capacity, drawdown available to the pump, suction lift limits, friction losses in the header and discharge run, and standby capacity are all separate calculations, and the yield itself should be confirmed by a pump test before plant is ordered.
  • Nothing here covers the consequences of lowering the water table: settlement of shallow-founded structures and services inside the drawdown cone, migration of fines and piping into the well, or the discharge consent and abstraction licensing the pumped water needs. Where drawdown reaches a neighbour's property, an abstraction, or compressible ground, that is a geotechnical engineer's assessment, not a page of arithmetic.
  • Yield is directly proportional to the hydraulic conductivity you type, and K in natural ground varies by orders of magnitude over short distances and directions. The result carries no uncertainty band around that, and the K box is read as metres per second whichever measurement system the page is set to.

Matching pump output to drawdown so run time survives

Two systems with identical tanks can cycle very differently, because run time per cycle is drawdown divided by the surplus flow — the pump's output minus whatever the house is drawing at that moment. The nastiest case is not a large draw; it is a small one. A single toilet fill valve, a slow-filling humidifier, an underground irrigation leak, or a dripping outside tap draws a trickle that empties the drawdown volume slowly, then the pump starts and refills it in seconds because nearly all its output is surplus. Run time collapses even though total water use is trivial.

Design so that the minimum run time is met at the flow that produces the shortest run — which for a fixed-speed pump falls near half the pump's rated output, where surplus flow peaks against the available drawdown. Check that condition explicitly rather than checking a full-flow case that will always pass. On oversized pumps this single check is what exposes the problem, and the correction is either more drawdown, a wider switch differential, or a smaller pump.

Constant-pressure variable-speed systems change the arithmetic rather than removing it. A drive that throttles the motor down to match demand can hold a run going for long periods instead of cycling, and its tank requirement is much smaller — the tank exists mainly to absorb the small pressure excursions the drive cannot chase quickly enough and to prevent hunting at very low draw. Still fit a tank, still set pre-charge per the drive manufacturer's instruction, which is generally referenced to the drive's set pressure rather than to a mechanical switch cut-in. Below a certain minimum demand these drives shut down and restart, so the low-flow condition remains the one worth testing.

Pump protection belongs in the same conversation because it exists to catch the failure mode cycling causes. Low-yield cut-off devices, motor overload protection, and dry-run sensing all interrupt the start sequence when conditions are wrong; verify each functions during commissioning rather than trusting that it is wired. Electrical installation is governed by the wiring code in force locally — NFPA 70, National Electrical Code, in the United States, and equivalent national codes elsewhere — and submersible motor circuits, bonding and grounding of metallic well components carry specific requirements there.

Run time is stored volume divided by the rate the pump moves it, so the same tank behaves differently behind a 10 gpm pump and a 25 gpm one.

The volume of water to move — a pool, a flooded floor, a tank.

The headline flow on the pump's box or plate — measured with no lift and no hose.

The lift at which the pump's flow falls to zero — on the same plate as the rated flow.

Height from the water surface up to the hose outlet.

The inside bore of the discharge hose — the single most sensitive number here.

Total discharge hose length, including the part lying flat.

Estimated drain time

10.4 hours

Medium confidence

Built on a linearised pump curve and Hazen–Williams hose friction (C = 150). A manufacturer's published curve, where you have one, governs.

Delivered flow at the operating point
21.14 gal/min
Share of rated flow surviving lift and hose
39.88 %
Friction head in the hose
9.13 ft
Total dynamic head
15.63 ft
33 ft
Schematic, drawn to the proportions you entered — not to scale on screen.

What this calculation does not cover

  • The vertical lift is held constant for the whole job and no water is assumed to arrive while the pump runs. In a pool the lift grows as the level drops; in a flooded basement groundwater, rain or a live leak keeps feeding the space. Real time to empty runs longer than this figure, and where inflow matches the delivered flow the level never falls at all.
  • Only straight hose length is charged for friction. Fittings, quick-couplers, a strainer or foot valve, a check valve, kinks, a partly closed discharge and any suction-side pipework all add head that is not in this number. Hazen-Williams with C = 150 is an empirical fit for smooth pipe carrying clean water — silt, debris, cold water or a ribbed corrugated hose all move the real loss away from it, and the formula is at its weakest in bores this small.
  • The pump is modelled as a straight line between the two figures on its plate. Where you have the manufacturer's published curve, that curve governs. Nothing here checks that the pump can prime at your suction lift, that it will hold prime as the water shallows, or that it is rated to run continuously for the hours reported — most utility pumps also stop drawing well before the floor is dry.
  • This is a time estimate, not a decision to empty the pool. It says nothing about hydrostatic uplift on an empty shell, liner shrinkage or collapse, or the groundwater conditions that decide whether a pool can safely be drained at all. Those questions belong to the pool builder and to the shell's own relief arrangements.
  • Where the water goes is outside this calculation. Discharging chlorinated, salt or silt-laden water to a storm drain, a watercourse or adjoining land is regulated in most places, and the receiving drain's capacity may be far below the flow reported here. Confirm the disposal route with the local water authority before running the pump.

Setting the system up on the day

Sequence matters more than any single adjustment. Prove the well first: static level, a sustained draw at the intended rate, pumping level stable. Then set the pump and check amp draw against the motor's service factor rating on all legs, because a motor pulling unevenly at commissioning will not survive high cycle counts. Only after that does the system get pressurised and work on the tank begin.

Charge the tank with the system drained and the water side open to atmosphere, using an accurate low-range gauge rather than a tyre gauge that reads coarsely at these pressures. Bring the pre-charge to its target, close up, and let the pump fill. Read cut-in and cut-out at the tank tee, not at a fixture and not off the pressure switch's own scale, and adjust the switch nuts in the order the switch manufacturer specifies — on the common differential-type switch the two adjusters interact, and turning the wrong one first means chasing both settings around in circles.

Then measure drawdown for real. Close the pump's supply, open a tap, and catch the water that comes out between cut-out and cut-in in a graduated container. That measured figure is the one to record. It exposes a partially waterlogged tank, a failed bladder, a pre-charge error, and a switch differential narrower than the dial suggests, all in a single test that takes a couple of minutes. Compare it against the design drawdown, and if it falls short, fix the cause before hunting elsewhere.

Finish with a cycle count under a controlled small draw — the low-flow case described earlier — and time the run. Write down cut-in, cut-out, pre-charge, measured drawdown, run time, amp draw per leg, static and pumping level, and the date. That record is worth more to the next person on the property than any equipment list, and it turns a future callout from guesswork into a comparison.

Disinfection and water quality close out the visit. Any well opened during the work gets shock chlorinated and then flushed until the residual clears, with a bacteriological sample taken after the residual is gone rather than during it; sampling procedure and acceptance criteria come from the state or provincial health authority. Where treatment equipment sits downstream, remember it adds pressure loss that rises as media loads, which quietly eats into the pressure available at fixtures and can push a homeowner into raising switch settings — straight back into the drawdown trade already described.

Friction in the drop pipe and the run to the tank is subtracted from everything the pump curve promised, and on a deep well it is the larger of the two losses.

The total length of the pipe run.

The design flow rate through the pipe.

The pipe material's Hazen-Williams roughness coefficient.

The pipe's actual internal (bore) diameter.

Friction head loss

17.96 ft

High confidence
2 in
Schematic, drawn to the proportions you entered — not to scale on screen.

What this calculation does not cover

  • Hazen-Williams is an empirical fit to cold water in turbulent flow, roughly 40 to 75 °F (4 to 24 °C) at velocities in the 2 to 10 ft/s (0.6 to 3 m/s) band. Outside that it drifts: glycol-charged loops, hot recirculating mains and low-flow trickles are Darcy-Weisbach problems, where viscosity enters the calculation instead of being absorbed into a single C value. The formula still returns a number for any of them; it is just not the loss you will measure.
  • Head loss is one term of the pressure the fixture actually sees. What is available is the incoming main, less the static lift to the outlet, less this friction, less the fittings, and less every device in the line — a meter, a backflow preventer, a filter and a softener can take 20 to 30 psi (207 kPa) between them. A run whose friction loss looks comfortable here can still open at a shower with nothing left.
  • Velocity is not reported, and velocity is often what sizes the pipe rather than head loss. Copper is normally held near 8 ft/s cold and 5 ft/s or less on hot recirculating lines, because water moving faster erodes the inside of elbows and tees over the years and makes the pipe audible in the wall. A small pipe on a short run can pass a friction check comfortably and still be the wrong size.

Reading a cycling complaint on an existing system

Arrive at a short-cycling well and the fastest route to the cause is measuring drawdown before touching anything. A near-zero drawdown with a healthy switch differential points at the tank: check pre-charge by tapping the schrader with the system depressurised, and watch for water coming out of the air valve, which condemns the bladder outright. A tank that feels uniformly heavy and sounds dead when struck is waterlogged; a healthy bladder tank sounds hollow above the waterline and solid below it, and finding that transition by tapping down the shell is a quick field check.

Adequate drawdown but rapid cycling shifts attention to the flow side. Look for a running toilet, a softener stuck in regeneration, a leaking foot valve or check valve letting the column drain back, or a supply line leak between the well and the building. A check valve failure has a signature: pressure bleeds off with no fixture open, and the pump restarts on a timescale that lengthens as the leak-back path fills.

Pressure that climbs to cut-out and then falls off instantly under load, with the pump clearly running, suggests the well is being drawn down to the intake. Confirm with a water-level reading during the run rather than inferring it. Where that is the finding, the conversation moves to reducing pump output or adding atmospheric storage, and the homeowner needs to hear it framed as a well limitation, not a broken component.

One diagnosis routinely gets missed: a switch differential that has narrowed on its own. Spring-loaded switches drift as they age and their contacts pit, and a system commissioned at a 20 psi gap can be running at 8 psi (0.55 bar) years later with a tank that is otherwise perfect. Measuring at the tee catches it. Guessing from the dial does not, and replacing a healthy tank because of it is an expensive, avoidable outcome that a five-minute measurement prevents.

Longevity, and the numbers worth leaving behind

The economics of getting drawdown right are lopsided. Extra tank volume is a modest one-time addition to a job; a submersible motor replacement means pulling the drop pipe, and on a deep well that is equipment, access and most of a day, plus whatever the wiring and splices need once they are up. Systems sized to comfortably beat the minimum run time routinely outlast their design life, while marginally sized ones fail early in a way that reads as bad luck but is a predictable consequence of cycle count.

Consider two tanks in parallel where a single large one will not fit through the access or will not sit stably. Drawdown adds, pre-charge must be identical on both, and both connect to a common manifold so neither is starved. It also gives a graceful failure mode: one bladder going down halves the drawdown rather than eliminating it, and the resulting complaint arrives well before the motor is destroyed.

Mount the tank so it is not carrying pipework stress. Tank tees hanging on unsupported copper crack, and a tank sitting directly on a wet floor corrodes at the base ring where nobody looks. Give it a stand or a pad, keep the air valve accessible, and leave enough room to get a gauge on the schrader without dismantling anything — the service that gets skipped is the one that is awkward to reach.

Leave the homeowner with three things they can act on: the pre-charge figure and what it is for, the observation that a pump audibly starting every few seconds means something is wrong and should not be lived with, and a note of the annual check — pre-charge with the system drained, and a measured drawdown. Those two measurements catch nearly every developing fault while it is still a tank problem rather than a motor problem, which is the entire point of thinking about a well in cycles.

Field take-off and commissioning checks

Verify against the motor manufacturer's published starts-per-hour and minimum run time, and against the well-construction and electrical codes in force locally.

  • Pressure tank, bladder or diaphragm type — Size on required drawdown at the chosen switch differential, not on nominal volume.
  • Pressure switch with matched differential — Record cut-in and cut-out measured at the tank tee; a wider gap buys drawdown at the cost of fixture pressure swing.
  • Tank tee, isolation valve and drain — Drain must let the water side reach atmosphere so pre-charge can be set correctly.
  • Low-range air gauge and graduated container — Pre-charge measured with the system drained; drawdown measured by catching delivery between cut-out and cut-in.
  • Dry-run and low-yield protection — Function-test at commissioning rather than confirming it is merely wired in.
  • Sanitary well cap and grout seal — Casing height and separation distances set by the state or provincial well code and local health authority.
Open this as a workspace →

Opens the calculators above on one screen with the dimensions from this article already filled in. Quantities only — this site publishes no price list, because local prices vary too much to publish honestly.

Drawn from

  • NSF/ANSI/CAN 61, Drinking Water System Components – Health Effects
  • NFPA 70, National Electrical Code
  • AWWA A100, Water Wells
  • ASME Boiler and Pressure Vessel Code, Section VIII, Rules for Construction of Pressure Vessels

Guidance, not a specification. Local codes, the engineer of record and the product manufacturer’s instructions govern where they differ from anything written here.