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Cycles of concentration in cooling towers, explained

The one number that decides how much water your tower wastes — and the reason you cannot simply turn it up.

TOWER OPERATIONBY GOTECH CHEMICALPUBLISHED 15 JUL 2026UPDATED 15 JUL 20268 MIN READ
THE SHORT ANSWER

Cycles of concentration is how many times more concentrated your tower water is than your make-up water — in practice, tower conductivity divided by make-up conductivity. Because evaporation removes pure water and leaves the minerals behind, the only way to stop the tower concentrating forever is to throw some water away, which is blowdown. Blowdown equals evaporation divided by (cycles minus one). That formula is why the first few cycles matter enormously and the later ones barely register: going from 3 to 6 cycles cuts blowdown by 60% and total make-up by 20%, while going from 6 to 9 cuts blowdown by only a further 38% of an already much smaller number. The ceiling is set by scale and corrosion chemistry, not by arithmetic.

The idea in one paragraph

A cooling tower rejects heat by evaporating water. Evaporation takes the H₂O and leaves everything dissolved in it behind. So the minerals in your make-up water — calcium, alkalinity, chloride, silica — steadily concentrate in the circulating water. Left alone, they would concentrate without limit until they precipitated onto your heat exchanger. The only defence is to deliberately dump some of the concentrated water and replace it with fresh: blowdown. Cycles of concentration is the ratio you settle at.

You will also see it defined against total dissolved solids. Conductivity is the practical field measurement and tracks TDS closely enough, which is why the controller on your tower is measuring conductivity.

The arithmetic

Three equations do all the work. Evaporation is fixed by your heat load — you cannot reduce it, it is the entire point of the tower:

Cycles  =  tower conductivity ÷ make-up conductivity

Blowdown  =  Evaporation ÷ (Cycles − 1)

Make-up  =  Evaporation  +  Blowdown

The second equation is the whole story. Look at what the (Cycles − 1) denominator does:

CyclesBlowdown as a multiple of evaporationChange from previous row
21.00 × E
30.50 × Ehalved
40.33 × E−33%
60.20 × E−40% from 4 cycles
80.14 × E−29% from 6 cycles
100.11 × E−22% from 8 cycles

This is a curve of diminishing returns, and it is steep. The move from 2 to 4 cycles saves more water than the move from 4 to infinity. If you take one thing from this article: the money is in escaping low cycles, not in chasing high ones. Anyone selling you a programme on the promise of 10 cycles is selling you the flattest part of the curve — and, as below, the riskiest.

Try it on your own tower

CALCULATOR

What are your cycles costing you?

Enter your system. Everything updates live. Nothing is sent anywhere.

 At 3 cyclesAt 6 cycles
Tower conductivity µS/cm µS/cm
Blowdown m³/h m³/h
Make-up m³/h m³/h
Make-up per year
Water cost per year
EVAPORATION (UNAVOIDABLE) m³/h
WATER SAVED PER YEAR
SAVING PER YEAR

Evaporation is estimated as circulation × range × 0.0017, the standard approximation behind the old “1% of circulation per 10°F of range” rule. Drift loss is ignored — on a tower with working drift eliminators it is small enough not to change the conclusion, and leaving it out makes the saving estimate slightly conservative. Default water cost is the WSD trade tariff of HK$4.58/m³; your real figure should include sewage charge, so raise it accordingly.

WhatsApp these numbers to Gotech

Where the ceiling actually is

If the arithmetic says higher is better, why does nobody run at 15 cycles? Because concentrating the water is exactly the thing that causes scale and corrosion. Every cycle you add multiplies the mineral content, and four constraints arrive:

  • Calcium carbonate scale. As calcium and alkalinity concentrate, the water crosses from dissolving CaCO₃ to depositing it. This is the binding constraint on most Hong Kong towers, and it is the thing the Langelier Saturation Index is designed to predict.
  • Chloride and corrosion. Chloride concentrates along with everything else and attacks passive films — it is the classic driver of pitting and of stress corrosion cracking in stainless. The EMSD criterion is below 200 mg/L. Ten cycles on a 20 mg/L make-up gets you there on its own.
  • The Code's own conductivity criterion. Part 2 of the Code of Practice gives an indicative criterion of conductivity below 1,500 µS/cm. On typical Hong Kong make-up water this is often what caps you first — and it is why the calculator above warns you when your target would breach it.
  • Suspended solids. Higher cycles concentrate dirt, not just dissolved minerals. Dirt feeds biofilm and gives scale somewhere to nucleate.

So the real question is never “how high can cycles go”. It is “how high can cycles go on this water, with this treatment, on this metallurgy” — and that is a chemistry answer, not a spreadsheet answer.

Why so many towers sit at 2 or 3 cycles

In our experience it is almost never a deliberate decision. It is usually one of these:

  • The conductivity setpoint was never revisited. Somebody set it at commissioning, possibly conservatively, possibly for a different make-up water, and it has been bleeding away ever since.
  • The controller is not actually controlling. A fouled conductivity probe reads low, so the valve never opens — or reads high, so it never closes. A bleed valve passing continuously will hold a tower at low cycles forever and nothing on the log sheet will say so.
  • Fear, following a scale incident. Someone scaled a chiller once, so the response was to bleed hard permanently. That treats the symptom of an inhibitor problem by paying a water bill in perpetuity.
  • Nobody owns the number. The O&M contractor assumes the treatment provider is optimising it; the treatment provider assumes the setpoint is the client's decision.

Every one of those is cheap to find. Measure make-up conductivity and tower conductivity on the same visit and divide. If the answer is under 3, there is money on the floor.

The part that is not about water

Water is the obvious saving, and on the trade tariff it is a real but modest number. Three larger effects usually ride along with it:

  • Chemical cost. Every m³ of blowdown carries your inhibitor and biocide down the drain with it. Halving blowdown roughly halves the chemical you are throwing away to hold the same residual.
  • Sewage charge. Blowdown is discharged, and discharge is charged. Your true cost per m³ is the water tariff plus the sewage charge, which is why the calculator lets you set the figure rather than assuming it.
  • Make-up heating and treatment load. Fresh make-up arrives with fresh hardness and fresh oxygen. More make-up is more of both.

And the counterweight, stated plainly: if raising cycles causes scale, none of these savings survive contact with the energy bill. A thin film of calcium carbonate on a condenser costs more in compressor energy than the entire water saving is worth. Cycles optimisation that is not paired with an inhibitor programme capable of holding the new chemistry is not optimisation. It is a bet.

What to do with this

  1. Measure both conductivities — make-up and tower — and calculate your actual cycles. Not the setpoint. The reality.
  2. Verify the controller. Clean the probe, calibrate it, and confirm the bleed valve seats. A passing valve makes every other number a fiction.
  3. Get a full make-up water analysis. Calcium, alkalinity, chloride, sulphate, silica. Without it, any target cycles figure is guesswork.
  4. Model the limit, do not guess it. Work out which parameter caps first — usually LSI, chloride or the 1,500 µS/cm criterion.
  5. Move in steps and watch. Raise the setpoint, hold it, watch inhibitor residual, corrosion coupons and approach temperature. Then move again.
  6. Write it down. The setpoint, the reason for it, and the water analysis it was based on — so the next person does not inherit a mystery.
Gotech has treated Hong Kong water systems since 1982. This article is general guidance, not a compliance certification for your site.

Frequently asked questions

What is a good cycles of concentration for a cooling tower?

There is no universal number, because the ceiling is set by your make-up water chemistry, your metallurgy and your treatment programme, not by a rule of thumb. Many towers run at 2 to 4 cycles and 6 or more is often achievable. What matters is which parameter caps first — commonly calcium carbonate scale potential, chloride, or the EMSD Code's indicative conductivity criterion of 1,500 microsiemens per centimetre.

How do I calculate cycles of concentration?

Divide the conductivity of the circulating tower water by the conductivity of the make-up water. Both readings should be taken on the same visit with the same calibrated instrument. Conductivity is used as a practical proxy for total dissolved solids.

How much water does increasing cycles actually save?

Blowdown equals evaporation divided by cycles minus one, so the savings are front-loaded. Going from 3 to 6 cycles cuts blowdown by 60% and total make-up by about 20%. Going from 6 to 9 saves far less in absolute terms. The largest savings come from escaping low cycles, not from chasing high ones.

Can high cycles of concentration damage my system?

Yes. Concentrating the water is what causes scale and corrosion. Higher cycles multiply calcium and alkalinity, which drives calcium carbonate deposition on heat transfer surfaces, and multiply chloride, which attacks passive films and drives pitting. Cycles should only be raised alongside an inhibitor programme capable of holding the resulting chemistry.

What is blowdown in a cooling tower?

Blowdown is the deliberate dumping of part of the concentrated circulating water so it can be replaced with fresh make-up. Evaporation removes pure water and leaves the dissolved minerals behind, so without blowdown the tower would concentrate without limit until minerals precipitated onto the heat exchanger. Blowdown equals evaporation divided by (cycles minus one), and make-up equals evaporation plus blowdown.

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