Water supply

Recirculating Domestic Hot Water: Buying Back the Ninety Seconds

The wait at the furthest tap is a pipe volume divided by a flow rate, and every method of shortening it costs heat around the clock.
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Ninety seconds is a measurement, not a complaint

Somebody opens the tap in the furthest ensuite and stands there. The water arrives cold, stays cold for a minute and a half, then turns hot. They report a fault with the hot water system. There is no fault with the hot water system.

What they are waiting for is the water already standing in the pipe to leave. That water cooled to room temperature hours ago, and none of it can be reheated in place — it has to be pushed out of the tap and down the drain first. The wait is therefore the internal volume of everything between the heat source and the outlet, divided by the flow rate the outlet will actually pull. Both halves of that are measurable, and neither has anything to do with the size of the cylinder.

The arithmetic explains the things that seem inconsistent. A basin tap waits far longer than a bath tap on the same pipe, because the basin pulls a fraction of the flow through the same volume. A 22 mm run waits roughly twice as long as a 15 mm run of the same length, because it holds roughly twice as much. And a house replumbed with generous pipe to cure a pressure complaint has just made every wait longer.

Say the number out loud before promising anything. If a survey shows fifty litres standing in the run to the far bathroom, no pump setting and no control strategy will produce instant hot water there; the honest conversation is about how much of that wait you can remove and what the removal costs to run.

Everything standing between the heat source and the outlet has to leave before hot water appears, so the wait is that volume divided by what the tap can pull — measure the run and the ninety seconds stops being an opinion.

The pipe's inside diameter, not the nominal or outside size.

The total length of pipe run.

Estimated pipe volume needed

0.7573 gallons

High confidence
Volume (liters)
2.87 liters
Volume (cubic in)
174.95 cubic in

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.

0.75 in
Schematic, drawn to the proportions you entered — not to scale on screen.

What this calculation does not cover

  • The figure is the contents of a straight bore and nothing else. Fittings, valve bodies, meters, strainers and any water standing in a cylinder or tank at the end of the run are not counted, and the pipe wall is excluded — so this is not the volume of pipe material, and not the space the pipe occupies in a chase or trench.
  • Volume scales with the square of the bore, so an inside diameter that is 9 per cent out produces a volume 19 per cent out. Published inside diameters differ by material, schedule and class for the same nominal size, and the calculator takes whatever figure you type at face value — it has no way of knowing that a half-inch pipe was entered at half an inch.
  • It assumes the run is completely full of liquid over its whole length. Gravity drains, waste stacks and sewers are designed to flow part full, and a system that has not been purged holds air at its high points, so both contain less than this number says.
  • It answers how much the run holds, not how long the wait is. Turning that volume into a hot-water delay needs the fixture's flow rate as well, and the real delay runs longer because the first hot water gives up heat to the pipe wall and to whatever surrounds it. No time calculation happens on this page.
  • Nothing here is a sizing or a support check. Velocity, friction loss and pressure drop are separate calculations, and a long run that holds a comfortable volume can still be too small to deliver flow. The contents also weigh whatever that volume of water weighs, which bears on hanger spacing and is not assessed.

Three ways to get the water back, and what each one really is

A dedicated return is the proper answer: a separate small-bore pipe from the far end of the hot main back to the heat source, with a pump keeping the whole flow leg warm. Every outlet teed off that main is then a short branch from hot water, and the only wait is the branch itself. It costs a second pipe through the whole building, which is why it is decided at design stage and almost never retrofitted into finished construction.

A crossover arrangement uses the cold main as the return. A thermostatic valve under the furthest fixture opens while the water reaching it is cool, letting the pump push cooled hot water into the cold pipe, and closes once hot arrives. It needs no second pipe, which makes it the retrofit of choice, and it has one consequence nobody mentions at the sale: the cold water at that fixture is lukewarm for a while after each cycle, and in a single-bathroom dwelling that is the tap people drink from.

A thermosiphon return has no pump at all and relies on the density difference between the hot flow and the cooling return to drive circulation. It works in tall buildings with vertical loops and short horizontal legs, and it barely works anywhere else. Where one already exists and performs, leave it. Do not design one into a modern well-insulated horizontal layout and expect it to move water.

There is also the option of not building a loop. Shortening the run, relocating the heat source, dropping a small point-of-use heater at the outlying fixture, or reducing the bore of the final leg all attack the volume side of the equation instead of the flow side, and on a single distant fixture they are frequently cheaper to install and always cheaper to run.

A warm loop is a heat emitter you did not specify

The moment a loop circulates, every metre of it is losing heat to the space around it, continuously, whether or not anybody is drawing water. That loss does not stop at night, it does not stop in August, and in a building with a cooling load it gets paid for twice — once at the heat source and again at the chiller.

The scale surprises people. A loop is typically the longest run of hot pipe in the building, and unlike a heating circuit it is hot for far more hours of the year. On many commercial buildings the annual standing loss from the recirculation loop exceeds the useful heat delivered to the taps. That is not an argument against loops; it is an argument for insulating them properly and controlling when they run.

The return leg counts too, and it is the one that gets forgotten in both the insulation order and the heat loss calculation. It runs only a few degrees below the flow, over the same distance, usually in the same ceiling void, and it is often left bare because it is small. A bare 15 mm return alongside a well-lagged 28 mm flow can contribute a startling share of the loop's total loss.

Everything that touches the pipe drains it as well. Uninsulated valve bodies, unlagged sections through fire-rated walls, bare pipe where it crosses a support, and the hundred short gaps where the sleeve stops for a bracket all add up. Loop loss is not distributed evenly along the run — it concentrates at the places the insulation stops.

Sizing the circulation rate from the loss, not from a catalogue

Loop flow has one job: carry enough heat around the circuit to replace what the circuit is losing, so the water arriving back at the heat source is only slightly cooler than the water that left. That makes the sizing a heat balance. Take the total heat the loop loses, decide the temperature drop you will accept between the source and the furthest point, and the flow follows directly.

The temperature drop is the design decision, and it is a genuine trade. A tight drop of a couple of degrees delivers hot water at the far branch and demands a high circulation rate, with all the velocity, noise and erosion that brings. A generous drop of eight or ten degrees needs very little flow and delivers water at the far end that a mixing valve may struggle to work with — and that a water safety plan may not accept.

The number that comes out is small. Loop flows for typical dwellings and small commercial buildings land in the range of a few litres per minute, which is a fraction of the flow to a single shower. This is why so many loops are grossly overpumped: the smallest circulator on the merchant's shelf is often several times the duty the loop actually wants, and its lowest speed setting is still too fast.

Overpumping is not harmless. It raises velocity in a pipe that runs continuously, accelerates erosion at every elbow, makes the loop audible in quiet rooms, and increases the heat loss by holding the whole circuit closer to the source temperature. Undersizing simply means the far end runs cool. Between the two failures, the far end running cool is the one you can diagnose from the ground.

Loop flow is set by the heat the circuit loses and the drop you will accept at the far end, which is why a pump chosen off a shelf usually runs several times faster than the system wants.

The total standby heat loss from the entire hot water recirculation loop.

The maximum temperature drop allowed between the water heater and the farthest fixture on the loop.

Required recirculation flow

0.379 gal/min

Medium confidence

Heat loss depends on your pipe insulation level, length, and ambient temperature — calculate it from your specific piping layout (or use a manufacturer's heat loss table) rather than assuming a generic value.

Add the equipment this sizes

This result is a specification — 0.379 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

  • Treats the allowable temperature drop as a free choice, and it is a hygiene limit before it is a comfort one. The temperature that suppresses Legionella growth has to hold at the coldest point on the loop, which is the return — so the drop, which this page will accept as far as 15 K (27 °F), is fixed by that floor and by the flow temperature above it, not by how lukewarm the far tap is allowed to feel.
  • One total flow says nothing about where it goes. A loop with several risers or branch returns sends nearly all of it up whichever path offers least resistance, and the others go cold while the pump delivers exactly the total calculated here. Balancing valves — thermostatic, or manually set and commissioned — are what split it, and the branch flows they are set to are a separate calculation from this one.
  • The flow still has to fit the pipe. A recirculation return is limited by water velocity rather than by whether the flow will physically pass: hot water moving too fast erodes a copper pipe wall from the inside, and returns show it first because they run continuously for the life of the building. Sizing the return off this flow means checking it against the velocity limit for the pipe material, which can force a larger return than the flow alone suggests.

Counting the loop before choosing anything

The pump does not see metres of pipe. It sees resistance, and resistance comes from the straight run plus everything installed in it. On a recirculation return that second part is substantial: the loop passes an isolating valve at every branch tie, a balancing valve at every riser, a check valve, a strainer, and a turn at every structural obstruction between the far bathroom and the plant room.

The standard way to handle this is to convert each fitting into the length of straight pipe that would produce the same loss, add those lengths to the measured run, and treat the total as a single equivalent length. It is an approximation and it is a good one, provided the equivalent lengths come from a table for the right bore and the right fitting pattern. A long-radius bend and a moulded elbow of the same nominal size are not the same fitting.

Walk the route to count them. A loop drawn on a schematic has four bends; the same loop installed has fourteen, because the pipe went around a duct, dropped under a beam and came back up in a riser cupboard. On a retrofit this walk is the survey, and the fitting count that comes out of it is usually the single largest correction to the head estimate.

Count the branch tie-ins as fittings too, even where the branch is dead during circulation. Every tee the loop passes through costs something, and on a building with twenty outlets that is twenty tees on a pipe carrying only a few litres per minute.

A return leg is mostly fittings — a tee at every branch, an isolator at every riser, a turn at every obstruction — and the only tidy way to carry them into a head figure is as extra metres of pipe.

The total count of 90° elbow fittings in the piping run.

The straight-pipe length that produces the same friction loss as one elbow.

The total count of tee fittings where flow branches off the run.

The straight-pipe length that produces the same friction loss as one branch-flow tee.

Total fitting equivalent length

12 ft

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

What this calculation does not cover

  • Totals fittings, not the components that usually dominate the head. A coil, heat exchanger, strainer, balancing valve or control valve is published as a pressure drop at a stated flow - feet of head or kPa, not an equivalent length - and on a typical hydronic circuit those together exceed the whole pipe-and-fitting figure. A pump chosen from this total plus the straight pipe alone lands short, and the shortfall turns up as the branch that will not balance.
  • One path, not a system. Pump head is set by the INDEX circuit, the single worst route from the pump out to the furthest or most restrictive terminal and back, so the fittings that belong in this box are the ones along that path only. Adding up every elbow in the building inflates the total enormously and buys a pump that overpumps every other branch; the parallel branches get balanced down to the index circuit, they do not add to it.

Head, and why the bigger pump makes it worse

With an equivalent length in hand and a friction rate for the bore at the design flow, the head the loop demands is a multiplication. That number, paired with the flow from the heat balance, is the duty point, and it is what a circulator should be selected against.

Both figures are usually tiny. Domestic and small commercial loops commonly want a fraction of a metre of head at a few litres a minute, which sits far to the left of most pump curves. Selecting the pump by its maximum head or by the pipe size of its connections lands you somewhere near the middle of the curve, where it will deliver several times the flow the loop needs at a velocity the copper will not tolerate for twenty years.

Modern electronically commutated circulators solve part of this by modulating, and a constant-temperature control mode suits a hot water loop better than the constant-pressure modes written for heating circuits. What they cannot solve is a pump whose smallest output still exceeds the duty. Where that happens the correct answer is a smaller pump or a balancing valve deliberately set to add resistance, and the second of those is the one that gets used because it is on the shelf.

Bear in mind that the loop's resistance changes over its life. Scale narrows the bore, a strainer partially blinds, a balancing valve gets nudged. A duty point sitting on a steep part of the curve moves a long way when resistance changes; one sitting on a flat part barely moves. That is worth a glance at selection time.

Head is what the circuit demands of the pump, so take the friction rate for the bore you have, scale it by the equivalent length you just counted, and the duty point stops being a guess.

The friction head loss per 100 ft (or 100 m) of pipe run, from a pipe sizing chart or a Hazen-Williams friction loss calculation at the design flow rate.

The straight pipe length plus the equivalent length of all fittings, valves, and equipment in the circuit's index (longest/most-resistant) run.

Total pump head required

10 head units

Medium confidence

Friction loss rate must come from your system's actual pipe sizing chart or Hazen-Williams calculation for the design flow rate — this calculator only scales that rate by total equivalent length; it does not calculate the friction loss rate itself.

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 on its own selects no circulator. A pump is chosen where the required head and the design flow meet on its curve, so this figure has to be carried forward with the same flow rate the friction loss rate was read at — two systems needing identical head at very different flows take entirely different pumps.
  • Plain water is assumed. A 30 to 50 percent propylene glycol charge is thicker and heavier, raising circuit friction at the same flow and cutting the flow any given pump delivers, so a snowmelt slab or a freeze-protected loop sized from a water friction rate ends up short of flow at the far end of the circuit.
  • In a closed loop the pump lifts nothing — the down-leg balances the up-leg — so building height belongs nowhere in this figure and adding it oversizes the pump. The reverse applies to an open circuit such as a drainback array or an open tank: there the vertical rise from the water surface to the discharge is real head, and it is not included here.

Balancing, or why the nearest riser takes everything

A loop with several risers is several parallel paths, and water takes the easy one. Without balancing, the riser nearest the plant receives most of the circulation and the far riser receives almost none, so the building has a hot water problem in exactly one wing and a plant room that appears to be working perfectly. The complaint reads as a capacity failure and it is a distribution failure.

Static balancing valves fix this by adding measured resistance to the short paths until every path sees a similar drop. They work, they hold their setting, and they require a commissioning visit with a differential pressure meter and a set of valve charts. They also assume the loop always runs at the design flow, which stops being true the moment a variable-speed pump modulates.

Thermostatic balancing valves take a different approach: each one throttles itself to hold its own branch return at a set temperature, so the flow distributes itself according to where the heat is actually being lost. On multi-riser buildings they are usually the better answer, and several types include a periodic full-open thermal disinfection position, which matters where the water safety plan calls for one.

Whichever type is fitted, they need to be found and reached later. Balancing valves buried above plasterboard ceilings with no access panel are, functionally, fixed orifices. Schedule them, label them, and record the commissioned setting on the label as well as in the file.

  1. Bring the loop up to normal operating temperature with all branches open and the pump at design speed.
  2. Work outward from the plant, recording the return temperature at every branch tie-in.
  3. Throttle the branches running hottest — they are the ones taking more than their share — and let the far branches recover.
  4. Repeat the circuit; each adjustment changes the ones you already set, so two or three passes is normal.
  5. Verify the total flow at the pump still matches the duty, and re-check the furthest branch last.
  6. Label every valve with its final setting and photograph the label in place.

The pipe that never rests

A recirculation return is one of the few pipes in a building carrying hot water continuously for its entire service life. That changes which failure modes matter. A supply pipe sees flow for minutes a day; a loop return sees it for every hour of every year, and everything velocity-driven accumulates twenty or thirty times faster.

Erosion-corrosion in copper is the headline. Above a threshold velocity the protective oxide film cannot re-form quickly enough where flow is disturbed, and metal is removed at the inside of elbows, immediately downstream of burrs left by a poorly reamed cut, and at the outlet of partly closed valves. The result is a pinhole in a bend that looks perfect from outside. The velocity limits published for hot recirculating water are markedly lower than the limits for cold supply, and that difference is the whole point.

Scale deposition works in the same direction. Hardness precipitates more readily at high surface temperature, so a loop in hard water furs the return and the heat exchanger faster than the rest of the system, narrowing the bore, raising velocity at constant flow, and pushing the erosion problem along. The two failures reinforce each other.

Check the velocity; do not assume it. The flow from the heat balance and the internal bore of the return give it directly, and if the result is above what the material tolerates in continuous hot service, the answer is a larger return bore or a lower circulation rate — accepting a wider temperature drop at the far end as the price.

Erosion in copper is governed by velocity and a return leg runs at its velocity every hour of the year, so put the loop flow and the return bore through this flow-over-area check; it is labelled for a backflow assembly and the arithmetic is the same one.

The design flow rate through the backflow preventer.

The internal diameter of the pipe at the backflow preventer connection.

Flow velocity

484.1 ft/min

High confidence

Add the equipment this sizes

This result is a specification — 484.1 ft/min — not a quantity. Put the thing it sizes into your project: how many, what you call it, and your supplier’s price.

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

What this calculation does not cover

  • The relief port is the flow that floods plant rooms, and it is not this one. A reduced-pressure assembly is built to dump water to atmosphere when a check fouls or downstream pressure rises, and the rate at full relief can be a large fraction of line flow — far more than a routine floor drain and air-gap fitting will swallow. That receptor is sized from the manufacturer's published relief discharge for the specific model and size, and it is what decides whether a failure is a puddle or a ceiling coming down on the floor below.
  • The velocity limit that bites first usually belongs to the pipe, not the assembly. Copper thins by erosion-corrosion above roughly 8 ft/s (2.4 m/s) cold and about half that on hot recirculating lines, and it thins at the elbow and tee immediately downstream where the flow is still disturbed by the device — with plumbing codes capping velocity for noise on top of that. A figure comfortably inside the assembly's rating can still be outside what the pipe carrying it will survive.

Temperature is a safety parameter here, not a comfort setting

In a building with a written water safety plan, the recirculation loop is not primarily a convenience feature. It is the mechanism that keeps stored and distributed hot water above the temperature at which bacterial proliferation is controlled, throughout the distribution, including at the ends. Turning a loop off to save energy in such a building is a change to the risk assessment, not a settings change.

That places a floor under the temperature drop you are allowed to design for. A return arriving back at the plant well below the flow temperature means part of the loop has been sitting in the range the safety plan exists to avoid. Where a plan applies, the acceptable return temperature is stated in it, and the flow rate has to be sized to hold that figure, not the drop that would have been comfortable.

It also places a ceiling on what reaches the outlet. Storage and distribution at a temperature that manages bacterial risk will scald, so the protection happens at or near the fixture through a mixing valve of the right type, and the blended leg downstream is kept as short as the layout allows. A loop that circulates blended water at a mild temperature throughout the building has removed the scald risk by creating the other one.

Sources for the actual numbers are the adopted plumbing code, the building's own water safety plan, and the recognised guidance the plan cites. They differ by jurisdiction and by building type, and a residential dwelling, a care home and a hotel are three different answers. Confirm which document governs this building instead of carrying a figure across from the last job.

Controls, and the honest arithmetic of the trade-off

Every control strategy trades wait time against standing loss, and the trade is close to linear: the more hours the loop is warm, the fewer seconds anyone waits and the more heat the building loses. There is no setting that removes both.

A time clock is the crudest useful control and often the most effective in a building with a predictable rhythm. It gives instant hot water during the morning and evening windows and full wait outside them, and it cuts loop hours by more than half in most dwellings. Its weakness is that it knows nothing about the building, so a household that changes shift patterns gets the worst of both.

An aquastat on the return runs the pump only when the loop has cooled below a setpoint, which stops the pump churning water that is already hot. It is a genuine improvement over continuous running and is almost always worth pairing with a clock. Demand control goes furthest: a button, a motion sensor or a flow switch starts the pump on request, and the occupant accepts a short priming wait in exchange for a loop that is cold most of the day.

Whatever is fitted, someone has to be told what it does. A demand-control button that nobody explained gets reported as a fault within a fortnight, and the usual remedy applied by whoever attends is to strap the pump to a permanent live. Leave a one-page description of the control strategy in the plant room and another with the occupant.

Control strategies for a recirculation loop, and what each one costs
StrategyWait at the far tapStanding lossWhere it fits
Continuous circulationEffectively noneFull loop loss, every hour of the yearBuildings where a water safety plan requires the distribution held at temperature
Time clockNone inside the window, full wait outside itLoop loss during scheduled hours onlyDwellings and offices with a predictable daily rhythm
Return aquastatNone while the loop is still warmReduced to what holding the setpoint costsMost commercial retrofits, usually paired with a clock
Demand button or occupancy triggerA short priming wait on each callClose to zero between callsDwellings, where a brief wait is an acceptable trade
Thermosiphon, no pumpUnpredictable, and negligible on a horizontal layoutUncontrolledExisting tall vertical loops that already work; not a design choice
Control strategies for a recirculation loop, and what each one costs

What to measure, and what to leave behind

Commissioning a loop is a temperature survey, not a pump test. Bring the system to normal operating condition, then record the flow temperature leaving the plant, the return temperature arriving back, and the return temperature at every branch tie-in. Those readings are the whole diagnosis: a branch return sitting well below the others is a balancing fault, and a system return sitting well below the flow is a flow rate or an insulation fault.

Then repeat the measurement the occupant actually cares about. Time the wait at the furthest outlet with the loop running as it will run, and again with the loop off. The difference between those two numbers is what the system was installed to deliver, and it is the only performance figure the building owner will ever quote back at you.

Write down the pump setting. Circulators get nudged, replaced and reset by people with no knowledge of the balance, and a loop that took a morning to commission can be undone by somebody turning a dial to the maximum in the belief that faster is better. A label on the pump giving the commissioned speed and the design flow prevents most of it.

Hand over the standing loss as well as the wait time. The building owner is buying instant hot water and paying for a heated pipe circuit, and stating both sides of that in the handover turns a future energy query into a decision they already made instead of a defect they discovered.

Walking the loop before anything is priced

A recirculation survey is a walk with a tape, a thermometer and a notebook. These are the readings that let the flow, the head and the control strategy all be settled from one visit.

  • Developed length of flow and return, measured on the route — Walked, not scaled off a drawing; the installed pipe goes around obstructions the schematic never showed.
  • Internal volume between the source and the furthest outlet — Bore by bore along the run, since this is what sets the wait the occupant is complaining about.
  • Fitting and valve count on the return leg — Every branch tee, isolator, check valve and strainer, converted to equivalent length for the head estimate.
  • Insulation condition, metre by metre — Note where the lagging stops as well as where it runs; loop loss concentrates at valve bodies, brackets and wall penetrations.
  • Return temperature at each branch tie-in — Taken with the loop at operating condition; the spread between branches is the balancing brief.
  • Which document governs the temperature regime — Adopted code, water safety plan, or both — and whether this building type is treated differently.
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

  • ASHRAE Standard 188, Legionellosis: Risk Management for Building Water Systems
  • ASHRAE Guideline 12, Managing the Risk of Legionellosis Associated with Building Water Systems
  • ASHRAE Handbook — HVAC Applications, Service Water Heating
  • ANSI/ASHRAE/IES Standard 90.1, Energy Standard for Buildings Except Low-Rise Residential Buildings
  • ASSE 1017 Performance Requirements for Temperature Actuated Mixing Valves for Hot Water Distribution Systems
  • ASSE 1070 Performance Requirements for Water Temperature Limiting Devices
  • ASTM B88 Standard Specification for Seamless Copper Water Tube
  • CIBSE Guide G, Public Health and Plumbing Engineering
  • International Plumbing Code, Chapter 6 Water Supply and Distribution (as adopted and amended locally)

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