The plume was chosen from a photograph
A client picks a courtyard fountain the way anyone picks one: from an image. A granite bowl on a plinth, water breaking evenly over the rim, cobble underneath it and no tank anywhere in sight. Nothing in that photograph names a pump, and nothing in the supplier's quotation does either — the bowl comes on a pallet, the plinth comes with it, and the water is somebody else's problem. On a landscape contract that somebody is usually the person reading this.
The courtyard then adds its own constraints, and they are not the ones a pump catalogue anticipates. Three walls and a glazed return, so the space channels wind rather than sheltering from it. Paving already set out to a survey, with one existing gully in the corner that predates the last refurbishment and no drawing of what it connects to. A garden tap on the wall that somebody fully intends to run a float valve off. Occupied windows six metres from where the plume will stand. Every one of those touches a decision that looks purely hydraulic.
The order the job resolves in is the useful thing to fix first. Establish the water volume that is genuinely in circulation. Choose a turnover period and turn it into a recirculation duty. Get the flow and the pressure the chosen nozzle actually wants, which is a separate figure and normally the larger one. Reconcile the two into a single duty point on a single curve, with the delivery run's losses built in. Only then deal with the mains connection — and with the discharge that the mains connection is about to create, which is the part that has stopped more courtyard fountains at inspection than any pump selection ever has.
Six quantities under one cobble deck
What the client sees when the job is finished is stone. What gets bought is a stack of separate items, each measured a different way, and each one wrong on its own terms if it is scaled off the bowl instead of off the chamber. The reservoir is either poured in situ or dropped in as a proprietary basin, and above it sits a load-bearing grate on a frame that has to carry whatever crosses the courtyard — including a scissor lift on the day the glazing gets cleaned.
The number every later figure depends on is the chamber's internal wetted volume, and it is not the chamber's nominal capacity. Support crates, ballast blocks, the pump body, the strainer housing and the cobble that inevitably works its way through the grate all displace water. So does the sump the strainer sits in, which has to stay flooded. Take the volume from the inside faces at the level the water will actually sit at when the display is running, and write it on the drawing, because it is about to be divided by a period and multiplied through the rest of the job.
What is under the cobble on a concealed-reservoir fountain
- Bowl and plinth — sets the plume height and the catch radius the cobble deck has to cover, and arrives as a fixed item with the delivery pipe routed up through it
- Cobble topping — bought by loose volume and converted to a delivered tonne, and deep enough that the grate below it never shows through Gravel Calculator
- Load-bearing grate and frame — carries the cobble plus whatever crosses the courtyard, and is the only access anyone will ever have to the pump
- Reservoir chamber — its internal wetted volume at running level is the figure the turnover duty is divided out of, not its nominal capacity Sump Pit & Catch Basin Concrete Calculator
- Tanked lining — keeps the make-up demand down to evaporation and carry rather than to a slow loss nobody can see Below-Grade Waterproofing Membrane Roll Calculator
- Compacted bed — takes the loaded weight of a full chamber, which is roughly a tonne for every cubic metre of water in it Gravel Base Layer Tonnage Calculator
A chamber poured in situ is walls and a base of one thickness wrapped around a void, and what gets ordered is the difference between the two — settle it before the formwork is cut rather than on the morning the truck arrives.
SettingsSettings for this calculation
Waste is set to 5% by hand. Pick a tier above to replace it, or keep your own figure.
The overall outside length of the pit or basin.
The overall outside width of the pit or basin.
The overall outside height (depth) of the pit or basin.
The thickness of the concrete walls and base.
Extra concrete for spillage.
Concrete volume needed
1.13 yd³
Assumes a simple open-top rectangular box with uniform wall and base thickness — real sump designs often have a sloped or stepped base for pump clearance.
- Outer block volume
- 2.07 yd³
- Interior void volume
- 1 yd³
- Base volume (no waste)
- 1.07 yd³
They open the calculator with your figures already in it
Sump Pit & Catch Basin Concrete Calculator: 1.13 yd³ — shown in imperial, US market. The link sets both, so the result they see is the one on your screen.
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 shape is a plain rectangular box with one thickness for the walls and the base. It adds nothing for a sloped or stepped base under the pump, benching or a flow channel through a catch basin, a haunch at the wall-to-base joint, or walls that thicken toward the bottom.
- No openings are deducted and no cover is added. Pipe penetrations, inlet and outlet knockouts and a grate or frame recess all come off the real pour, while a lid, cover slab or ladder rebate all go on it — neither adjustment is in this number.
- Reinforcement, formwork and waterproofing sit outside the estimate. No rebar, mesh, dowels or lifting anchors are counted, their displaced volume is not taken off the concrete, and there is no allowance for blinding under the base, tanking, or concrete lost into over-break where a wall is poured against soil instead of a form.
- This is a quantity, not a structural design. It does not check the thickness you entered against soil and groundwater pressure on the walls, against wheel or buffer loads on the base, or against uplift on an empty pit in a high water table. Those calls set the thickness; this only prices the thickness you were given.
- It does not size the pit. The interior void it reports is raw geometry, not usable storage between pump float levels, and it takes no view on how much sump depth to leave below the outlet for sediment in a catch basin.
Turnover is the housekeeping number, not the display number
Nobody swims in a fountain, so turnover here is not the regulated quantity it becomes on a public pool. What it buys is prosaic: an evenly mixed reservoir, a strainer that sees the whole body of water instead of one lane of it, and enough movement that debris reaches the sump rather than settling in the corners of the chamber. Pick a period, divide the wetted volume by it, and the recirculation duty falls out.
The period is a judgement, and the two ends of the range fail differently. A short period on a small chamber pushes the pump into a duty the reservoir cannot feed without drawing air off the surface, and the running cost is continuous because a fountain runs whenever the building is occupied. A long period in a sheltered south-facing courtyard produces exactly what a sheltered south-facing courtyard is good at: warm, still, sunlit water, and a green film on the cobble within a fortnight of handover.
There is a health dimension to the same decision that a landscape contract rarely mentions and a facilities manager will eventually raise. A fountain producing a plume produces aerosol, and a decorative fountain is named as a device to be assessed in ASHRAE Standard 188 on legionellosis risk management for building water systems, with ASHRAE Guideline 12 covering the same ground in more practical terms; in the United Kingdom the duty runs through the HSE Approved Code of Practice L8 and the HSG274 guidance beneath it. Circulation is not a control measure on its own — cleaning frequency, the treatment regime and the distance to openable windows and air intakes are — but a reservoir that stagnates is the condition every one of those documents is written about, and the turnover period is where that starts.
Then read the result for what it is. Volume divided by a period is an average recirculation rate. It is not the instantaneous flow the display asks for, and on almost any fountain with a jet in it the display figure is the larger of the two. The pump is bought against the larger one, and the turnover figure survives as the check that says whether the chamber is being properly worked at the flows the display leaves it running at.
Wetted volume divided by the period you choose gives the recirculation half of the pump's job — the half that can be settled on the drawing board, before any nozzle data has arrived from the supplier.
The total water volume held in the fountain or water feature basin.
How many hours the pump should take to circulate the full basin volume once.
Required pump flow rate
11 gal/min
Target turnover time varies by water feature type and desired visual effect (a display fountain jet may need a much higher instantaneous flow than this average turnover rate suggests) — this is a baseline recirculation sizing check, not a substitute for the fountain nozzle/jet manufacturer's specific flow and pressure requirements.
- Flow rate
- 660 gal/hr
They open the calculator with your figures already in it
Decorative Water Feature Pump Flow & Turnover Calculator: 11 gal/min — shown in imperial, US market. The link sets both, so the result they see is the one on your screen.
Add the equipment this sizes
This result is a specification — 11 gal/min — 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
- Flow is only half of a pump selection, and head is the half never asked for. A pump's headline flow is its output at zero lift, and it falls away as water is pushed higher and through more pipe, fittings and filter — so a pump advertised at the rate shown here can deliver a fraction of it once it is lifting into a raised bowl through a long, undersized line. Add the static lift to the friction losses and read the flow off the pump's curve at that total head.
- The volume being turned over is not the volume that has to be in the basin. A feature loses water continuously to evaporation and to wind carrying spray off the display, and the reserve that keeps the pump submerged between top-ups is a separate quantity from the turnover volume. A pump that gulps air because the sump has dropped an inch is the most common way a fountain fails, and it usually takes the pump with it.
- Turnover only buys clarity if something is filtering. This is the rate at which water passes the pump, not a rate any filter can handle — push more through a filter than it is rated for and debris goes straight past it while the head loss climbs. On a filtered feature it is often the filter's rated flow, not the turnover target, that caps the pump.
The nozzle publishes pressure; the pump publishes head
A display nozzle is specified as a pair of numbers for every plume height it can produce: a flow, and a pressure measured at the nozzle inlet. Those pairs are not transferable between nozzle families. An aerated or foam jet entrains air and swallows several times the flow of a smooth-bore jet standing at the same height, because most of what you can see is not water. A cascade or weir is specified per metre of lip rather than per jet, so its flow scales with the length of the edge and a long lip is the thirstiest thing in the courtyard — and past a couple of metres the awkward part stops being the pump and becomes holding that edge level enough for the sheet to break evenly along all of it. Take the pair off the manufacturer's table for the exact model and orifice, at the height the client signed off, and treat any generic figure as a placeholder to be replaced.
The two datasheets in front of you will not be in the same units, and that is where the arithmetic quietly goes wrong. Nozzle tables are published in bar or in psi at the inlet. Pump curves are published in metres or feet of head. A foot of water column weighs 62.428 pounds on every square foot beneath it, which spread over 144 square inches is 0.4335 psi, so a psi is 2.3067 feet of head at that reference temperature, and a bar is very close to 10.2 metres. Convert one side before either is read off a chart, and record which of the two figures the pump was selected against, because the next person to look at this will assume the units they use themselves.
Wind decides whether any of it survives contact with the courtyard. An enclosed yard between tall elevations does not produce still air; it produces a downdraught along one wall and a channel along another, and a plume that behaves on a calm commissioning day drifts onto the paving in October. The catch radius the cobble deck has to cover is conventionally set well outside the plume height as a rule of thumb rather than as a code requirement, so take the spray envelope from the nozzle manufacturer's own data, and specify a wind switch on the controller where the plume is tall enough for drift to reach a doorway or a car.
Nozzle tables give a pressure at the inlet and pump curves give head, so one of the two has to be converted before they can be read against each other on the same chart.
The water pressure in PSI.
Equivalent feet of head
115.3 ft of head
They open the calculator with your figures already in it
PSI to Feet of Head Calculator: 115 ft of head — shown in imperial, US market. The link sets both, so the result they see is the one on your screen.
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
- Head is counted from wherever the gauge is, not from the ground. A basement tank reading 50 psi converts to 115 ft, but a fixture 25 ft above that gauge has already spent 10.8 psi of it before a tap opens and sits at about 39 psi at rest. Read the pressure and the point you care about as a pair, or the converted figure describes a place nobody is showering in.
- A well or booster system does not hold one pressure, so a single converted figure describes one moment of the cycle. A 40/60 switch runs everything between 92 and 138 ft of head, and a sprinkler zone or top-floor shower that performs at cut-out can fade badly just before the pump restarts. Convert the cut-in pressure, not the cut-out one, when what you want is the worst the system will do.
Building the duty head out of the run you actually have
Total head for this pump is a short list, and each item on it has to come off the installation rather than off a habit. Static lift is measured from the lowest operating water level in the chamber to the nozzle exit, not from the still level, because the reservoir draws down the moment the display starts and water is held in the air, on the bowl and in the delivery pipe. Then friction through the delivery run, the equivalent length of every bend and tee in it, the strainer at its dirty condition rather than clean, any isolating or regulating valve, any ultraviolet or filtration unit in the circuit, and finally the pressure the nozzle itself demands. That last item is a demand, not a loss, and it is the one people leave out because it does not look like resistance.
The delivery run on a courtyard job is short and unusually convoluted, which is a bad combination. It leaves the chamber, turns to clear the grate frame, runs under the paving to the plinth, and then goes vertically up through a stone column with two more turns in it to reach the nozzle. That is a handful of metres of pipe carrying eight or ten fittings, and on runs of that shape the fittings are frequently worth more head than the pipe. Convert them to equivalent lengths, add them to the measured run, and only then work the friction — a bore chosen to fit the plinth's core hole rather than the flow is the standard way this ends badly.
With the duty flow and the duty head settled, read the curve rather than the headline. A pump delivers where its curve meets the system, and the useful question is whereabouts on its own curve that lands: ANSI/HI 9.6.3 sets out preferred and allowable operating regions for rotodynamic pumps precisely because a machine running far from its best efficiency point is loud, short-lived and wasteful even when the flow number is correct. Throttling a display back with a bypass to the chamber is legitimate and common on fountains, since it gives the commissioning engineer a way to trim the plume, but a pump bought two sizes up and then strangled is an energy decision made by accident. Where the pump is dry-mounted in a side chamber rather than submerged in the reservoir, suction conditions become a live question too, and ANSI/HI 9.6.1 on net positive suction head margin is the document that governs it.
Friction in the delivery run is the part of the duty head nobody can see, and on a short courtyard route full of turns it regularly outweighs the lift from the chamber to the nozzle.
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
They open the calculator with your figures already in it
Domestic Water Pipe Friction Loss Calculator (Hazen-Williams): 17.96 ft — shown in imperial, US market. The link sets both, so the result they see is the one on your 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.
The top-up is a cross-connection, and the category decides the device
A fountain loses water continuously and visibly. Evaporation off a warm plume, carry onto the paving, splash into the cobble, and every litre that leaves on the coat of a dog that got in. So there is a top-up, and whatever joins the mains to that basin is a cross-connection between a potable supply and an open body of water that birds land in. It is the regulated part of this job, and it is decided by a classification somebody else makes, not by what is convenient to fit.
In the United Kingdom the classification runs through the fluid categories of the Water Supply (Water Fittings) Regulations 1999 and BS EN 1717, with the WRAS Water Regulations Guide as the working reference. An ornamental pond or fountain sits at the severe end of that scale, and at the severe end a mechanical backflow device is not accepted protection at all — the route is a physical air gap into a break cistern, Type AA to BS EN 13076 or Type AB to BS EN 13077, with the feature drawing from the cistern rather than from the main. That changes the job substantially: a cistern needs a position, a level above the feature or its own boosting, an overflow of its own, and frost protection. Confirm the category with the water undertaker in writing before anything is ordered.
In North America the same question is asked differently and answered by the authority enforcing cross-connection control. A decorative pond or fountain is normally classed as a health hazard, which points at an air gap or at a reduced pressure principle assembly to ASSE 1013 and AWWA C511, or to CSA B64.10 in Canada, with the approved model taken from the enforcing authority's own list. The Foundation for Cross-Connection Control and Hydraulic Research's manual is the widely adopted reference behind those lists. This is the branch of the decision that puts a relief port on a landscape contract.
Either answer has a physical consequence the client needs to see on a drawing before the paving is set out. A break cistern is a box that has to go somewhere and be reachable. A reduced pressure assembly has to stand above grade in an enclosure that meets ASSE 1060 for outdoor fluid-conveying components, never in a pit or a chamber where a flood could submerge its relief port, and never buried under the cobble with everything else. In a courtyard designed to look uninterrupted, that is a visible box against a wall, and it is a conversation with the designer rather than a fitting to be hidden on the day.
A relief port is a design flow with a start time, not a drip
The reduced pressure principle works by holding the zone between two check valves below the inlet pressure, and a differential relief valve dumps that zone to atmosphere the instant the margin closes. On a fountain top-up the conditions that close it are ordinary and frequent. The supply drops because a hydrant is flowing or the courtyard tap has been opened flat out to fill a bucket. Backpressure arrives from the feature side on a hot afternoon. And, most characteristically for this application, the branch spends almost its entire life at zero flow — a float valve admits a trickle for a few minutes a day — so the first check sits in stagnant water and fouls, and a fouled check is precisely what makes the relief lift.
What comes out when it lifts is not a weep. A relief valve on an assembly of any size discharges immediately at a rate measured in litres per second and keeps discharging until somebody attends, which on a landscape contract with no building management system means until a tenant complains. Take the rated relief discharge from the manufacturer's published data for the exact model and size — Watts and Zurn Wilkins both publish it for their reduced pressure families — and use orifice arithmetic as a sanity check on the order of magnitude, and as a way of asking what happens if the driving head at your site is higher than the datasheet assumed.
Outdoors adds a failure the plant room never sees. A relief that weeps intermittently through January puts a sheet of ice across a courtyard threshold, and the first person to find it will be walking on it. ASSE 1060 grades enclosures by exactly this: whether the enclosure is merely a cover, or is insulated, or is heated to keep the assembly and its discharge above freezing. Choose the class against the site's design low temperature and against how long the courtyard goes unvisited, and check the enclosure's own drain outlet as a hydraulic component rather than as a hole — on more than one enclosure the moulded outlet is the narrowest point in the entire discharge path.
One thing must not be done, and it is the tidiest-looking option available. Do not pipe the relief into the fountain reservoir. It removes a visible discharge from a paved courtyard, it appears to solve the drainage problem for nothing, and it converts the assembly's own defence into the cross-connection it exists to prevent: a chamber filling from a stuck float valve rises to submerge the outlet, and the open path from the feature back toward the main is complete. The discharge is atmospheric by design and has to stay that way.
Orifice area, discharge coefficient and driving head bracket what a relief port can produce, which is the figure to test the enclosure outlet and the courtyard gully against before either is committed to.
The open cross-sectional area of the relief valve's discharge orifice.
An empirical factor accounting for orifice flow contraction and friction losses.
The pressure head driving flow through the relief valve orifice, expressed as a water column height.
Relief valve discharge flow
36.8 gal/min
Confirm the actual relief valve orifice area and discharge coefficient from the specific backflow preventer manufacturer's data — this is a general orifice-flow estimate, not a substitute for the manufacturer's rated relief capacity.
- Discharge velocity
- 913.37 ft/min
They open the calculator with your figures already in it
Backflow Preventer Relief Valve Discharge Calculator: 36.77 gal/min — shown in imperial, US market. The link sets both, so the result they see is the one on your screen.
Add the equipment this sizes
This result is a specification — 36.8 gal/min — 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
- Takes the head as given and does not derive it. During a genuine relief event the driving head is the supply-side pressure at that instant, not a static column — a 70 psi (483 kPa) main is about 50 m (164 ft) of water, not the 3 m (10 ft) the field opens on — and because flow goes with the square root of head, an assumed head that low understates the discharge by roughly a factor of four.
- Says nothing about how the discharge is piped. Relief from a reduced-pressure assembly must reach the drain through an air gap and never a direct connection — hard-piping it into the waste system rebuilds the exact cross-connection the assembly was installed to prevent, and it also means a relief event pushes into the drain instead of showing itself on the floor where someone notices it.
Finding a courtyard drain that can take it
Courtyards are hostile to this. There is often exactly one outlet, it was sized for rainfall on a small paved area, and it may sit above a podium or a basement deck where the drainage is a designed system with no spare connections in it. A relief event is not rainfall: it is a sustained full-bore discharge from a single opening with no diversity and no duration limit. Sizing the route on drainage fixture units, or on the yard's rainfall allowance, is the mistake that produces a flooded threshold rather than a wet patch.
Fall is what usually runs out first. The enclosure stands above the paving so the assembly can be tested, its outlet is a fixed height above that, and the gully invert is wherever it was set decades ago. Between the two is a courtyard whose crossfalls were designed to be barely perceptible underfoot, which means the developed length is long and the drop across it is small. Work the slope over the actual run before the enclosure position is fixed to a wall, because moving a box on a drawing costs nothing and moving it after the paving is bedded costs a week.
Then get the destination agreed rather than assumed. Discharging clean water to a surface water sewer or to a watercourse is not automatically permitted and is a question for the drainage undertaker; BS EN 752 is the framework for drain and sewer systems outside buildings, and an indirect waste arrangement indoors is governed by the adopted plumbing code rather than by preference. Where a soakaway is proposed, BRE Digest 365 sets out how one is designed and tested — and be honest that a soakaway hides the fault completely, so a fouled check can run for weeks with nothing visible to report. If the discharge cannot be seen by someone, specify a float alarm instead, or accept that the first symptom will be a water bill.
| Route | What it has to satisfy | Where it fails in a courtyard |
|---|---|---|
| Existing yard gully or slot channel | The full rated relief flow on top of whatever rainfall is already running to it | Sized for the paved area's rain, and frequently the only outlet the yard has |
| New trapped gully with an indirect connection | An air gap above the receptor and a branch carrying the flow at the fall available | Shallow paving crossfalls and a fixed invert leave no drop to work with |
| Enclosure outlet piped to daylight | An outlet bore matched to the relief flow, discharging somewhere it will be noticed | The moulded outlet is often the narrowest point in the whole path |
| Soakaway or gravel pit | Infiltration proven by test, and acceptance that the discharge will be invisible | A fouled check runs for weeks with nothing to see and nobody to tell |
| Into the fountain reservoir | Nothing — it turns the relief port itself into a cross-connection | A chamber filling from a stuck float valve submerges the outlet |
| Indoors to a floor receptor | The undertaker's consent and a physical route through finished ground | Means breaking into paving and crossing a threshold that was never detailed for it |
The enclosure has to stand where the assembly can be tested and the gully sits where it has always sat, so the slope between those two fixed inverts is what decides whether the route works at all.
The pipe invert (bottom interior) elevation at the upstream end of the run.
The pipe invert elevation at the downstream end of the run.
The horizontal (plan-view) distance between the upstream and downstream structures.
Pipe slope
2.33 %
Minimum slope requirements depend on pipe size and expected flow (to maintain self-cleaning velocity) per your local drainage design standard — confirm the calculated slope meets your pipe size's minimum requirement.
They open the calculator with your figures already in it
Storm Drain Pipe Slope Calculator: 2.33 % — shown in imperial, US market. The link sets both, so the result they see is the one on your screen.
What this calculation does not cover
- A slope that works hydraulically still has to fit in the ground. The upstream end needs enough cover over the crown for the pipe class and the traffic above it, and the downstream end has to arrive at an invert the outfall, manhole or existing sewer can actually accept — so on a long run the grade is normally dictated by whichever of those two ends is fixed. A percentage chosen freely can bury the outlet below its receiving structure or leave the head of the run too shallow to drive over.
- Inverts are taken as a pair with nothing between them. Chain several runs together and every structure adds a drop of its own: manholes are commonly benched with the outgoing invert 30 to 60 mm (2.4 in) below the incoming one to cover head loss through the chamber, and more where the pipe changes direction or size. Carry a downstream invert straight into the next run as its upstream figure and that fall quietly disappears across the system.
- This is design slope on paper, and what gets accepted is the as-built line. A flexible pipe laid on poorly compacted bedding, or across a soft spot, settles between structures into a belly that ponds water no matter what the two end elevations say — which is exactly what a CCTV survey is looking for. Bedding, haunching and trench compaction are invisible to this arithmetic.
Power to a wet chamber, across a paved yard
A fountain is not a general outdoor circuit and is not treated as one. BS 7671 covers basins of fountains within Section 702, alongside swimming pools, with IEC 60364-7-702 behind it; the National Electrical Code addresses fountains in Article 680, Part V. Between them they govern residual current or ground-fault protection, equipotential bonding of conductive parts around and in the basin, and what may be installed within the zones measured from the water. A submersible pump in a chamber under a public courtyard sits squarely inside that scope, and the requirements are not satisfied by a weatherproof socket and good intentions.
The run itself is the other half. From the panel or consumer unit inside the building, across the courtyard, into a chamber under the paving is a long circuit on a conductor somebody will be tempted to keep small because it has to be drawn through an existing duct. Voltage drop over that length is what decides whether the motor starts cleanly against a full chamber on a cold morning, and the two rule sets treat the limit differently: BS 7671 gives figures in Appendix 4 — three per cent for lighting and five per cent for other uses from the origin of a low voltage installation — while the National Electrical Code carries its three per cent branch-circuit figure as an informational note rather than as a requirement. Check the drop against whichever applies, and check it at starting current rather than running current.
A pump in the far corner of a paved yard is a long run on a conductor chosen to fit an existing duct, and the drop across it is what decides whether the motor starts under load in winter.
Copper, or aluminum — the metal printed on the jacket (CU or AL).
The size printed on the jacket: an AWG number up to 4/0, then kcmil.
Single phase — including a 240 V circuit and DC — or a balanced three-phase circuit.
The distance from the panel to the load, one direction only.
The expected current draw of the load in amps.
The nominal circuit voltage — line to line for three phase.
Voltage drop
1.936 V
- Voltage drop
- 1.61 %
- Voltage at the load
- 118.06 V
- K constant, Ω·cmil per ft
- 12.9
- Conductor area, circular mils
- 6,530
They open the calculator with your figures already in it
Wire Gauge Voltage Drop Calculator (Copper or Aluminum, AWG to 1,000 kcmil): 1.94 V — shown in imperial, US market. The link sets both, so the result they see is the one on your screen.
Add the equipment this sizes
This result is a specification — 1.936 V — 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
- VOLTAGE DROP IS NOT AMPACITY, and the two are different questions with different answers. A conductor can stay inside the 3% suggestion and still be too small to carry the current without overheating, and it can be thermally adequate and still drop too much over a long run. Both checks have to be made, and only one of them is made here.
- The K constants are DC resistance at 75 °C (167 °F) for uncoated copper and for aluminum, the basis of NEC Chapter 9 Table 8. The table's size-by-size resistances differ from the single constant by a percent or so either way, and the table is not reproduced here. A conductor running cooler drops a little less and one at a 90 °C (194 °F) rating a little more; tinned (coated) copper has its own, slightly higher resistance.
- Treats the circuit as resistive, which is close for lighting, heating and most branch circuits. On a large AC feeder, and above all one in steel conduit feeding an inductive load, the conductor's reactance adds to the drop and the power factor matters; Table 9 of the same chapter carries the AC figures and is not reproduced here.
- Three phase assumes a balanced load and gives the drop between lines. A single-phase load taken from one line to neutral of a three-phase supply is a single-phase circuit: choose single phase and the line-to-neutral voltage.
- Aluminum conductors need terminations and devices listed for them; the code does not let dissimilar metals be joined except in a device listed for the purpose. Nothing here checks a termination, a lug or a splice.
- The 3% and 5% figures are suggestions in the code's informational notes rather than requirements, though a local amendment, an equipment maker's instructions or a specification can make a tighter figure binding.
What to prove before you leave, and what to leave behind
Commissioning a fountain is mostly a matter of watching it for longer than feels necessary. Run the display through a full drawdown and confirm the reservoir still covers the strainer at the lowest level it reaches, with the make-up isolated so the chamber cannot quietly hide a shortfall. Set the plume with the trimming valve and record the position. Then leave it running and come back in an hour with the wind up, because the drift that puts water on the paving is not visible in the first five minutes.
The paperwork is short and it is the only thing that will still exist in ten years. Record the chamber's wetted volume at running level, the turnover period chosen and the duty it produced, the nozzle model with its flow and pressure at the agreed height, the pump model and where the duty point sits on its curve, the classification the water undertaker or cross-connection authority assigned, the assembly or air gap arrangement installed with its rated relief discharge, and where that discharge goes. A page with those figures on it is what lets the next contractor service the feature instead of guessing at it, and it is what an inspector asks for first.
- Measure the chamber's internal wetted volume at running level, with crates, ballast and pump displacement deducted.
- Choose a turnover period and convert it to a recirculation duty, then set it aside as a check rather than as the selection.
- Take flow and inlet pressure for the exact nozzle and orifice at the signed-off plume height, and convert pressure to head.
- Build the duty head from lowest operating level to nozzle exit, adding fitting equivalent lengths and the strainer at its dirty condition.
- Select against the curve and confirm the duty point sits inside the pump's preferred operating region, not merely on the curve.
- Get the fluid category or hazard classification for the top-up confirmed in writing before ordering any device.
- Take the rated relief discharge from the manufacturer's data for that model, and size the enclosure outlet and the receiving route on it.
- Work the fall from the enclosure outlet to the existing gully invert over the real developed length before fixing the enclosure position.
- Check the pump circuit for voltage drop at starting current, and confirm bonding and residual current protection against the fountain provisions.
- Run the display for an hour in wind, then record volume, turnover, nozzle data, duty point, classification and discharge route on one page.
The figures that have to exist before a pump is ordered
Six numbers decide this feature, and three of them belong to somebody outside your own office who will take a fortnight to answer. Start them early and select the pump last.
- Wetted volume at running level — Internal faces of the chamber at the level the water sits at with the display on, less crates, ballast, pump and strainer displacement.
- Turnover period, chosen and written down — Kept as the housekeeping check on the reservoir, not as the selection figure — the display flow is normally the larger of the two.
- Nozzle flow and inlet pressure at the agreed height — From the manufacturer's table for the exact model and orifice, with the pressure converted to head before the pump curve is opened.
- Duty head built from the real run — Lowest operating level to nozzle exit, plus fittings as equivalent length, plus the strainer dirty, plus the nozzle's own demand.
- Fluid category or hazard classification for the top-up — In writing from the water undertaker or the cross-connection authority; it decides between a break cistern with an air gap and a mechanical assembly.
- Rated relief discharge and the fall available below it — The manufacturer's published relief flow for that model, worked against the drop from the enclosure outlet to the existing gully invert.
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.
