Two winters later, on a photograph of a filter
The appliance is twenty-six months old, the secondary heat exchanger is blocked, and the manufacturer's engineer has been on site forty minutes, thirty of them taking photographs. One of the in-line filter, opened, with the magnet lifted out beside it. One of a jam jar of system water drawn from the drain cock on the return, held against a white wall. One of the commissioning record, where the section headed cleaning and water treatment carries a tick and nothing else. The claim is refused, and the argument that follows turns on what was done to the water two years ago — a question nobody can now answer.
This is not rare and it is not really a dispute about the boiler. Almost every wall-hung domestic appliance now carries a guarantee conditional on the system it is connected to: cleaned before the appliance goes on, dosed with a corrosion inhibitor at the concentration the manufacturer names, fitted with an in-line filtration device, and re-tested at every service. In the UK the instructions usually discharge that obligation by pointing at BS 7593, and at the appliance's own manual for whatever the code leaves to the manufacturer; on a commercial job BSRIA BG 29, pre-commission cleaning of pipework systems, sets out the same logic at a larger scale.
So the clean is a contractual step carrying an evidence requirement, and the evidence has to be made on the day. Two decisions hold it up: which cleaning operation this system needs, and what number the inhibitor dose is calculated against. The first, wrong, costs a day. The second costs the heat exchanger and the guarantee, silently, two seasons after anyone could still have fixed it for the price of a second bottle.
A jam jar, and the survey you do before quoting
Draw a sample before pricing the job, not on the morning you start it. A drain cock on the return, a clear jar, half a litre and five minutes of standing still tells you more about which operation this system needs than an hour of looking at radiators.
Black sediment that follows a magnet held to the glass is magnetite, the iron oxide produced when oxygen keeps reaching steel. A heavy load means an oxygen source running for years, and the useful question is which one: a feed and expansion tank open to the loft, a failed vessel letting the system go sub-atmospheric as it cools, barrier-free underfloor pipe, or a top-up habit. Brown material staying in suspension is finer corrosion product; water clear but strongly coloured is dissolved product, an old inhibitor or somebody's cleaner from a previous visit. Grey, gritty, non-magnetic solids are building debris, flux and jointing residue, and they matter because the magnetic filter everyone is about to fit will not hold them.
Then walk the system, because access rules a power flush in or out more often than chemistry does. Look for microbore tails, since a bore already half occupied will not pass mobilised debris and may not survive being asked to. Note cast iron columns, which hold a multiple of a steel panel of the same output and have been settling a bed in the bottom for decades. Establish whether an underfloor circuit carries an oxygen barrier to DIN 4726, because a barrier-free loop is a permanent oxygen source no clean will outlive. Two things then change the plan more than anything else: whether the system is open vented or sealed, since a swap frequently converts it, and whether a gravity primary or converted single-pipe circuit has left dead legs where nothing moves at any velocity you can generate.
- Draw half a litre from the return drain point into a clear container and leave it standing.
- Hold a magnet to the outside of the glass and watch whether the settled solids climb it.
- Note the system type and the pressure or static head it runs at now.
- Identify the smallest bore in the distribution, and any underfloor loops with the pipe's barrier specification.
- Locate the drain points, the filling arrangement, and a discharge route for the volume you are about to move.
- Open the existing filter; one nobody has serviced is a survey result in itself, and photograph what is in it.
Chemistry or a machine, and what each one genuinely moves
The trade argues this as a binary and it is not. Several operations are available, they do different work, and on most jobs the right answer is two of them in sequence. What separates them is not how aggressive they are — it is whether they supply velocity, because velocity is what carries loosened material out of a system rather than round it.
A chemical cleanse circulated by the system's own pump means dosing a cleaner, running hot with every emitter open for the dwell the product's data sheet gives, then draining and rinsing. On a system chemically dirty but not physically silted that is the correct answer, and its limit is arithmetic rather than chemical: the circulator was sized for design flow, design flow is a low velocity through the wide part of a radiator, and no chemistry alters the fact that a settled bed lies below the moving water rather than in it. A power flush answers that limit with an external machine supplying far more flow, reversing it, and letting you isolate and agitate one emitter at a time while dumping to waste. It is also the operation most likely to find every weeping compression joint in the building, which is a real cost and belongs in the conversation before the machine comes off the van.
| Operation | What it moves | What it needs on the day | Where it fails |
|---|---|---|---|
| Chemical cleanse circulated by the system's own pump | Deposit the cleaner can disperse, plus whatever the existing flow velocity will then carry to a drain | Cleaner dosed against the measured volume, the system hot with every emitter open, and the dwell the product's data sheet states | Settled beds in horizontal panels and in dead legs, where velocity never rises enough to lift what the chemistry loosened |
| Power flush with an external machine | Settled solids, because the machine supplies flow, reversal and agitation the circulator cannot | Isolating valves that shut on every emitter, a discharge route for the dump volume, and pipework sound enough to be pressurised and reversed | Bore already restricted enough that debris will not pass it; old compression joints and corroded tails that start weeping once disturbed |
| Mains-pressure flush through a temporary connection | Loose material, using the incoming main's own flow and pressure | A main with genuine flow, backflow protection on the connection, and somewhere for the discharge to go | A weak main never reaches scouring velocity, so the exercise dilutes the system rather than cleaning it |
| Emitters taken off the wall and cleaned outside | The bed at the bottom of a heavily silted panel, completely and verifiably | Space to do it, tails that will come apart and go back, and replacement valve seals to hand | Nothing at all about the distribution pipework, the heat source or the underfloor loops |
| Magnetic filter capturing across a heating season | Magnetite generated after the clean, at whatever rate the system goes on generating it | Servicing at the interval the appliance guarantee names, and someone who opens it | Anything already settled, and anything non-magnetic; it is protection afterwards, not a cleaning method |
The order of the day, and the one connection you never flush through
The sequencing matters more than the method argument and gets less attention. Whatever you do, you do it before the new appliance is in circuit — with the old boiler still connected, or through a temporary jumper across the flow and return where it was, but never through the heat exchanger you have just unwrapped. Its waterways are narrower than anything the old appliance had, the whole exercise exists to protect it, and pushing years of accumulated magnetite through it on day one is a self-inflicted version of the failure at the top of this page.
The same logic covers new pipework the swap brings. Copper and press fittings arrive carrying swarf, cutting oil and flux, so make that work up complete, flush it clear on its own, and connect it afterwards. A low-loss header or hydraulic separator goes in after the flush too: it is a low-velocity vessel by design and will collect precisely what you were trying to remove.
Dose last. Inhibitor goes in at the final fill, after the last drain-down anybody intends, and the reason is bookkeeping rather than chemistry — a partial drain to swap a valve afterwards removes an unrecorded share of the treatment and nobody adjusts for it. Where a further drain is unavoidable, recalculate and record the correction.
- Clean with the old boiler in circuit, or through a temporary flow-and-return jumper.
- Work emitter by emitter where the survey called for a machine, until each runs clear on its own.
- Rinse until the discharge matches the incoming fill water, not until a set time has elapsed.
- Fit the appliance, the filter and any separator, with new pipework flushed clear beforehand.
- Refill to the cold fill pressure the height requires, and check the vessel before going further.
- Bring the system to design flow temperature, then dose against the measured volume and circulate.
- Draw the handover sample, test it, and have the appliance certificated by a person registered for the fuel.
The pump you flush with is not the pump you are left with
Two hydraulic questions sit on this job and get conflated. One is temporary: does the flushing arrangement produce enough velocity to carry debris out of the components it is sitting in? The other is permanent, and changes quietly on a swap: does the new appliance's integral circulator have the head to serve the distribution the old external pump was serving?
The second catches people out because the old arrangement is invisible in the quote. A three-speed circulator next to a floor-standing boiler may well have been on its top speed for a decade, and its curve there is generous. A wall-hung appliance arrives with its pump inside it, and what matters is the residual head published in the installation manual — what is left after the appliance's own heat exchanger and internal pipework have taken their share. That is smaller than most people expect, and it is a manufacturer figure rather than a rule of thumb.
So compare before the day. Work out the head the worst circuit needs at the flow it needs, from the friction loss rate for the bore genuinely installed and the equivalent length of the route as built, and put it against that residual head curve; which circuit is the worst one, and how you prove it by measurement, is ground the balancing guide holds. If the appliance cannot serve that circuit on its own pump, the answer is a low-loss header with a secondary circulator, or a system boiler arrangement — a different quotation and a different plant space. Finding out after the old boiler is in the skip is the expensive version.
The same arithmetic has a third use during the clean. Debris only leaves if the water carrying it stays above the velocity at which it settles, and design velocity is well below that — the honest engineering reason a flushing machine exists, and why a chemical cleanse on a silted system produces impressively dirty water at the drain while leaving most of the deposit where it was.
Run this twice with different intentions: once for the head the worst circuit needs, to check it against the residual head curve printed in the new appliance's manual, and once for the temporary flushing arrangement, where you are asking for velocity rather than for design flow.
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
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.
They open the calculator with your figures already in it
Hydronic Circulator Pump Head Loss Calculator: 10 head units — 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 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.
Litres, not bottles
Inhibitor is sold in a container that names a number of radiators, and that proxy is where most under-dosing starts. It assumes a water content per emitter and a distribution, and a boiler swap breaks both: cast iron columns hold a multiple of the assumption, an underfloor circuit adds litres no radiator count sees, and a buffer puts the estimate in a different category. The dose is a concentration in a measured volume, so the volume has to be measured.
A swap also changes that volume in both directions on the same day, which the general system-volume question does not. A floor-standing cast iron appliance can hold tens of litres and it is going out; a wall-hung condensing one holds a fraction of that and is coming in. On an open vented conversion the feed and expansion tank goes with its cold feed. Add a low-loss header, a buffer or a plate exchanger and litres arrive. Total it after the swap, not before.
Build it from component data, as the table below sets out. The distribution is the part people over-weight and it is usually the smallest share — the water is in the emitters and in anything with a tank in its name. The per-metre bore arithmetic is set out in the guide on extending a heating system; what this job needs is the total, measured and dated.
Then verify rather than trusting a count of empty bottles. Test the concentration after circulating, using the test the inhibitor manufacturer supplies for its own product, or a laboratory sample where the instructions call for one. BS 7593 puts verification and periodic re-testing into the maintenance regime for the reason the opening scene illustrates: what gets argued over later is a measured concentration, and that is either on the record or it is not.
| Component | Where its figure comes from | Why it gets left out |
|---|---|---|
| Distribution pipework | Bore from the tube specification, not the nominal name, times the measured run for each size on the job | Rarely omitted, and usually over-weighted — it is the smallest share on most domestic systems |
| Pressed steel panel radiators | The manufacturer's data sheet for the exact type, height and length installed | Substituted with a single average that is wrong for every double panel and every 300 mm high emitter |
| Cast iron column radiators | Content per section from the maker's data, times the section count, counted radiator by radiator | Treated as one radiator each in a bottle's radiator count, which understates them severely |
| Underfloor heating loops | Loop length from the manifold schedule or the as-built layout, at the pipe's own bore | Invisible to any estimate based on counting emitters on walls |
| The appliance being removed and the one going on | Each unit's installation manual, subtracting one and adding the other | Assumed to cancel out, when a floor-standing unit and a wall-hung one differ by a wide margin |
| Cylinder primary coil | The cylinder manufacturer's published coil content | Confused with the cylinder's stored capacity, which is on the other side of the coil and is not system water |
| Buffer, thermal store or low-loss header | The vessel's own rated volume from its data plate or manual | Added to the job after the dose was calculated, and never fed back into it |
Run each bore on the job separately and keep a running total — this is the distribution share only, and the emitters, the appliance and any store are added to it from their own data before anything is dosed against the answer.
The pipe's inside diameter, not the nominal or outside size.
The total length of pipe run.
Estimated pipe volume needed
0.7573 gallons
- Volume (liters)
- 2.87 liters
- Volume (cubic in)
- 174.95 cubic in
They open the calculator with your figures already in it
Pipe Volume Calculator: 0.7573 gallons — 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 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.
Fill water is a material, and almost nobody specifies it
Every other material on the job arrives with a specification and this one arrives through a hose. What goes in at the final fill decides two failure modes over the appliance's life — scale, from hardness, and corrosion, from oxygen and dissolved salts — and where the clean addresses the history, the fill water addresses the future.
Scale is worse in a new appliance than in the old one, and not because the water changed. Deposition is fastest where heat flux is highest, and a condensing heat exchanger concentrates a large output into narrow waterways with a small water content — the reason it modulates well, and the reason a millimetre of scale in it is not equivalent to a millimetre in a cylinder. VDI 2035 Part 1 handles that by making permissible fill-water hardness depend on the installation rather than on the water alone: the total heating output and the system's specific volume in litres per kilowatt both enter the limit, and the direction of that catches people out. The more litres a system holds for each kilowatt of output, the stricter the permissible hardness becomes, because every one of those litres charges its own hardness through the same heat exchanger surface. Adding a buffer or a thermal store is what usually moves a domestic job into the band where the fill water has to be treated rather than simply run in off the main. Part 2 covers the corrosion side.
Where the main is hard, the two available answers are not equivalent and the difference is regularly missed. Demineralisation through a mixed-bed cartridge on the filling line removes dissolved salts and drops conductivity — the condition VDI 2035 calls low-salt operation, which several manufacturers now ask for by name. Base exchange softening swaps calcium and magnesium for sodium, preventing hardness scale but leaving dissolved solids and conductivity broadly where they were. Softened water is a scale answer, not a corrosion answer.
The chemistry you add has to suit the metals now in the system, and a swap often changes them. An aluminium-silicon heat exchanger is amphoteric and is attacked at high alkalinity, so appliances built with one specify a narrower pH window than an all-steel-and-copper system tolerates; that window is in the appliance's instructions, not a figure to carry over from another manufacturer's job. BS EN 14868 sets out how corrosion likelihood in a closed circulation system is assessed. Read the manual before choosing the cleaner as well as the inhibitor: an acidic cleanser left in contact beyond its stated dwell has ended more aluminium heat exchangers than dirty water has.
The vessel the swap either inherits or has to invent
A swap does one of two things to the expansion arrangement. Either the system was already sealed, leaving a vessel of unknown history to assess, or it was open vented and the swap converts it — at which point the feed and expansion tank goes, the open vent goes with it, and the system loses its only pressure reference. What replaces that is a vessel, a relief valve discharging to a safe visible place, a gauge, and a filling method that can be broken after use.
Where a combination or system appliance has a vessel built in, the manufacturer states the maximum system volume it is good for. That is a straight comparison against the total you measured for the dose — the second job that number does on this page, and the reason to do it properly the first time. Exceed the stated volume and the instructions require an additional vessel; one in parallel on the return at the same pre-charge is the normal remedy, and far cheaper than the alternative reading of the situation, which is a relief valve lifting every cold snap.
The flush is also the most reliable diagnostic for a vessel that has already failed. Repeated draining and refilling puts the system through several full heat-up cycles in a day with somebody beside the gauge, and a perished diaphragm announces itself at once: pressure climbs steeply on warm-up and the relief valve lifts. Pre-charge matching cold fill pressure, and cold fill pressure following the height to the highest emitter, is set out in the guide on extending a heating system. What is specific here is the timing — check it before the inhibitor goes in, because a relief valve lifting after dosing takes an unmeasured share of the dose down the drain with it.
Feed it the post-swap volume and read the answer as an acceptance volume in litres, which is what the appliance's built-in vessel has to be able to take — a different comparison from the maximum system volume the appliance states, and both have to pass before a supplementary vessel is off the quote. The final selection comes from the vessel manufacturer's own acceptance data.
The total water volume held in the closed hydronic loop, including boiler/chiller, piping, and terminal units.
The fraction by which the system water expands in volume across its full operating temperature swing.
The fraction of the tank's total volume that is actually usable to accept expanded water, based on the tank's fill and relief pressures.
Minimum expansion tank total (nominal) volume
8.67 gal
This is a simplified sizing approximation — final expansion tank sizing should follow the ASHRAE/hydronic system design method (or the tank manufacturer's sizing software) accounting for actual fill pressure, relief valve setting, and system operating temperature range.
They open the calculator with your figures already in it
Hydronic Closed-Loop Expansion Tank Sizing Calculator: 8.67 gal — 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 expansion fractions offered here are water. A loop charged with 30 to 50 percent propylene or ethylene glycol expands appreciably more over the same temperature swing, and the fluid supplier publishes the figure for the concentration you are running. Size a glycol system on a water fraction and the relief valve opens at design temperature and dumps the glycol you paid for — the system then makes up with plain water and quietly loses its freeze protection.
- A tank of the right volume does nothing if it is precharged wrong. The air side must be set to the system's fill pressure at the tank's own elevation, with the water side empty, before the loop is filled. A tank shipped at 12 psi (83 kPa) and hung on a system filled to 25 psi (172 kPa) has already spent most of its acceptance volume before the water is even warm, and the acceptance factor above has stopped describing it.
- Where the tank ties into the loop is not a sizing question, but it decides whether the tank works. The connection point is the one place in the system whose pressure the pump cannot change — pipe the tank into the pump's suction side and the pump adds its head to the rest of the loop, put it on the discharge side and the pump subtracts it, which can drop the pressure at the top of the system or at the pump inlet far enough to draw air or cavitate on a tank that was sized correctly.
What stays in the system to keep it clean
The clean is a single event, and the system starts generating deposit again the moment it is refilled. What determines whether that matters is what you leave behind, and the guarantee is specific: BS 7593 puts an in-line filtration device into the regime for a domestic system, and manufacturers name one as a condition. A magnetic filter meets that and works, because magnetite is ferrous.
Be blunt about what it does not do. It holds nothing non-magnetic, so the flux, jointing compound, plastic swarf and scale fragments a swap introduces pass straight through. And it is a consumable duty rather than a component: one nobody opens is a full one, and a full one has stopped capturing. That is why the annual service interval is not administrative — a service which does not include opening the filter has not serviced it.
An air and dirt separator does the complementary job. Rather than holding particles magnetically it drops velocity through a coalescing medium so entrained gas rises out and heavier non-magnetic solids fall into a collection chamber, continuously, without interrupting flow. That makes it the answer for the debris a magnetic filter ignores. The air side of that argument — where gas comes from, and why a system taking it on will not hold a balance — belongs to the balancing guide.
The sizing surprises people, because a separator is not sized by the pipe it connects to. Separation only works well below normal distribution velocity, so the connection is frequently a size or two larger than the pipe either side, and a unit chosen to match the pipe will not separate anything at design flow. Size it from the flow it must handle at the velocity the manufacturer states for its own medium, and let the connection size fall out of that rather than go into it.
Give it the flow that will genuinely pass the separator's position and the maximum velocity from the unit's own literature; the answer is a minimum connection diameter, and where that comes out larger than the pipe it sits in, the calculation is working rather than failing.
The hydronic system's design flow rate through the separator.
The maximum velocity through the separator's connection for effective air and dirt removal — commonly around 0.3 m/s (about 1 ft/s).
Minimum connection diameter
5.73 in
Effective air/dirt separation requires low velocity at the separator itself — confirm the manufacturer's rated maximum velocity and connection size for your specific separator model rather than assuming a generic value.
They open the calculator with your figures already in it
Hydronic Air/Dirt Separator Sizing Calculator: 5.73 in — 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 — 5.73 in — 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
- Position beats size here. Air leaves solution where the water is hottest and the pressure lowest — on most systems the boiler or chiller outlet, upstream of the circulator. Put the same separator on the cool return and it sees air still dissolved and passes it straight through. No connection diameter compensates for the wrong location; the low velocity sized here only earns its keep once the bubbles actually exist.
- This is a connection diameter, not a pressure drop. Every separator adds head to the circuit — the vessel, the coalescing medium inside it, and the expansion and contraction at each end — and none of that comes back from a velocity formula. A pump selected on pipe friction alone can land short of its duty point once the separator, the strainer and the dirt the separator will eventually be holding are all counted in.
- The dirt half is a different problem from the air half. What blocks a modern condensing boiler's heat exchanger is magnetite — fine ferrous sludge that a gravity pocket catches poorly and a magnet catches well — and no velocity calculation tells you whether you need the magnetic version. Nor does it size the dirt pocket or set how often it is flushed: a separator that is never blown down is a reservoir, not a filter.
The clean has a finish line, and it is a sample rather than a clock
Nothing here is finished at a time. It is finished at a water condition, and the difference is why so many flushes stop early with everyone satisfied. Debris leaves the pipework quickly because velocity there is highest, so a sample at the boiler drain point runs clear long before the system is clean — the emitters and the dead legs give up their contents last, if at all, and they are where the deposit was.
Sample at the end of the system as well as at the plant, and compare what comes out against a jar of the incoming fill water standing alongside it; that comparison is what turns an opinion into a reading. Where the appliance instructions state parameters to be met at handover — appearance, pH, conductivity, chloride, inhibitor concentration — those are the acceptance criteria. Then photograph the sample, photograph the filter contents at first service, and keep both with the paperwork, because the scene at the top of this article is an evidential contest and evidence made on the day beats recollection two years later.
| What the sample shows | What it is | What it changes |
|---|---|---|
| Black solids settling within minutes, climbing a magnet held to the glass | Magnetite from oxygen-driven corrosion of the steel in the system | Keep going; a system still shedding this has not finished, and the new heat exchanger is the next place it collects |
| Brown suspension that will not settle out | Finer iron oxide still mobilised by the cleaner and still in circulation | Rinse until it clears — inhibitor dosed into mobilised solids is a wasted dose |
| Clear water, strongly coloured, with nothing to settle | Dissolved product: cleaner still present, or an old inhibitor from a previous regime | Rinse toward the conductivity of the fill water before the new treatment goes in |
| Grey cloudiness or fine gritty non-magnetic solids | Flux, jointing compound, swarf and building debris, largely from the new pipework | The magnetic filter will not hold it, so this is a separator and strainer question, not a re-flush |
| An oily film on the surface | Cutting oil, thread compound, or press-fit lubricant residue | Needs a cleanser rated for it; left in, it fouls a coalescing medium and gets blamed on the separator |
| Conductivity well above the incoming main | Dissolved salts concentrated by years of top-up, or a softened rather than demineralised fill | Argues for a demineralised fill at refill rather than for another bottle of anything |
| Inhibitor concentration below the product's stated level after dosing and circulating | The dose went in against an underestimated volume, or a drain-down followed it | Re-dose against the measured litres and record the corrected figure — this is the number a claim is settled on |
Systems that cannot be cleaned, and the value of saying so first
Some systems will not come clean and no operation on the table changes that. A microbore distribution already occluded to the point where a machine cannot establish flow is one. Barrier-free plastic underfloor pipe is the clearest case: oxygen diffuses through the pipe wall continuously, magnetite generation restarts the day you refill, and the only durable answer is hydraulic separation with a plate exchanger so the ferrous components sit on the other side. A corroded steel emitter holding water only because the sediment inside it is doing the sealing will discover that during the flush, in a room with a carpet in it.
Put this in the quotation rather than in an apology. A manufacturer will not warrant a heat exchanger against a system that cannot meet the water-quality condition, so a system in that state changes what the job is: separation, partial re-pipe, emitter replacement, or in the honest cases a conversation about the distribution being at the end of its life. All of those are easier to have while the old boiler is still on the wall and working than at four o'clock on a Tuesday with a hole in the plaster where it used to be.
The record that answers the engineer in two years' time
Everything above produces one artefact, and it is the artefact the opening scene was missing. The record needs the measured system volume and how it was arrived at; the cleaning operation, the product, and the contact time it actually had; the handover sample result against whatever parameters the appliance instructions state; the inhibitor product and the dose in litres against volume; the filter make, model and position; the vessel size, pre-charge and cold fill pressure; and the date with a name against it. In the UK the Benchmark commissioning checklist supplied with the appliance is the format the manufacturer expects, and its water treatment sections are the ones that decide a claim.
Register the appliance inside the manufacturer's window, and tell the customer in writing what the guarantee is conditional on: an annual service that includes opening the filter and testing the water, and no change that adds volume without a re-dose. A radiator added by somebody else in year three dilutes the treatment as effectively as a leak does, and the customer is the only person in a position to know it happened.
The last thing worth doing costs nothing. Keep the survey photographs, the sample photographs and the test results with the record. A refused claim is decided on what can be evidenced, and the day spent cleaning a system properly is worth exactly what you can later prove about it.
What the clean needs settled before the old boiler comes off the wall
None of this is a material list. It is the small set of measured figures that decide which cleaning operation the system needs, what the treatment is dosed against, and what the record will say two winters from now.
- A settled sample from the return, with a magnet held to the glass — Separates magnetite from non-magnetic building debris in seconds, and that distinction is what chooses between chemistry and a machine.
- Post-swap system volume, totalled from component data — Distribution by bore, emitters from their data sheets, the new appliance's own content, the cylinder coil and any store — one number that the dose, the vessel check and the makeup rate all read from.
- The appliance's residual head curve from its installation manual — The integral pump replaces whatever external circulator was on the wall, and a swap can lose head without anyone noticing until a far room goes cold.
- The head the worst circuit needs at its design flow — Friction loss rate for the bore actually installed, scaled by the equivalent length of the route as built, compared against that residual head curve before the quote is issued.
- Incoming main hardness, and whether the fill is to be demineralised — Softening prevents scale but leaves the dissolved salts; demineralising drops conductivity, which is the condition several manufacturers now ask for by name.
- Existing vessel size and pre-charge, or the vessel the conversion needs — Checked with system pressure off the vessel, and compared against the volume limit stated for any vessel built into the new appliance.
- Filter and separator selection with their positions marked on the record — The separator is sized from flow and separation velocity rather than from the pipe it connects to, and the filter is a serviceable duty rather than a fitting.
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.
