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Notes from the loop · coolant filtration

How often should a liquid cooling loop be filtered?

The interval is not a date.

Change-out at terminal differential pressure, 35 psid against a 60 psid element maximum · coolant sample every 50 to 100 days · side-stream at 5–15 % of circulating volume


Two questions get confused here. One is whether the element is loaded, and the other is whether the fluid is still in specification. Different answers, different instruments.

We supply the loop between the coolant distribution unit and the cold plate. Neither of those two parts is in the catalogue.

Ask for the specification sheet

Portable side-stream filtration cart with its differential-pressure gauge and hose connections

Side-stream filtration cart · the gauge leg is the instrument the interval comes from

01 / The side-stream split

Size the split, and the turnover time follows

What the split is for

A side-stream loop diverts 5 % to 15 % of circulating volume from the main header, filters it and returns it downstream of the take-off. Full-flow inline filtration of the whole volume costs more energy and a larger footprint, which is why the split exists. The split is a design decision, and it sets the turnover time.

Worked on a 4,800 L loop

At 10 % of volume per hour that is 480 L/h, a full turnover every 10 hours. Published guidance puts the practical band at a full turnover every 6 to 12 hours. At 10 % per hour a contaminant slug takes hours to reach the element, which is why filtration problems arrive slowly.

Take-off, element, return
Side-stream filtration loop Main header running left to right with a take-off at 5 to 15 percent of circulating volume, a filter element, a pump and a return downstream of the take-off. main header element 5–15 % return, downstream

Loop 4,800 L · 10 %/h = 480 L/h · turnover 10 h · published band 6–12 h

02 / What loads an element

Why two loops of the same volume load differently

Production residue in pipework

Scale and swarf left in pipework and heat exchangers from the build.

Reaches the loop at first fill

Abrasion from pumps

Particles shed by pumps and mechanical components under continuous running.

Continuous while running

Installation and sealing residue

Material left by the assembly and sealing steps, carried into the fluid.

At commissioning

Ageing of the fluid itself

Inhibitor depletion and glycol breakdown raise conductivity and organic load.

Months, accelerated by heat

Element rating moves the rate too. Bag filtration at 1–10 µm takes the bulk load, cartridges at 0.5–5 µm do the fine polishing, and a 5 µm element blinds quickly unless it sits downstream of a bulk stage.

That is why the change-out number is a differential pressure and not a date.

03 / The pressure window

The change-out figure needs the maximum beside it

Differential-pressure window for a PP pleated depth cartridge, and the instrument that reads it.
Condition Value
Clean 2 µm element0.17 bar (2 psid)
Recommended change-out35 psid (2.4 bar)
Maximum differential60 psid (4.1 bar) at 20 °C
Cartridge temperature rating80 °C (176 °F)
Transmitter ranges±125 Pa · ±500 Pa
Transmitter accuracy±0.2 % of span
Transmitter resolution±0.02 % of span
Read at operating temperature
Differential pressure against element life A curve rising from 2 psid when clean, crossing a 35 psid change-out rule and approaching a 60 psid maximum at 20 degrees Celsius. 60 psid max 35 psid out 2 psid clean element life psid

Differential pressure is read at operating temperature, not at fill temperature.

04 / Commissioning sets the load

A loop is cleanest the day it leaves the bench

Fill cart connected to a manifold during commissioning with hoses routed and a sample bottle on the deck

Commissioning · the day the loop is dirtiest

Free iron from site work

Stainless steel welded, ground or fabricated on site without cleaning and re-passivation to ASTM A380 / A967 practice leaves free iron in the coolant, and free iron fouls microchannel surfaces.

Glycol that separated under vacuum

A glycol blend can partially separate under vacuum, so a sample after a vacuum fill is the only way to know the blend is uniform. Entrained air compounds it: degassing works best at temperatures a loop only reaches under load, so air problems surface weeks after handover.

05 / Coolant quality targets

What the filtration is protecting, as targets

Nine parameters

Loop water-quality targets, labelled for a glycol or facility water loop. Microchannel blockage, scaling and pitting are the failures the rows guard against.
Parameter Target Guards against
Suspended solids, cold plate < 5 µm Microchannel blockage
Suspended solids, rear-door HX < 10 µm Microchannel blockage
Turbidity < 1 NTU Particulate load, optical proxy
pH, glycol or facility water 7.0–9.0 Corrosion and inhibitor effectiveness
Conductivity, glycol or facility water 50–300 µS/cm Dissolved ionic contamination
Hardness < 50 ppm Scaling
Chloride < 50 ppm Pitting in stainless steel
Dissolved oxygen < 2–4 mg/L Corrosion rate
Microbial Zero active growth Biofilm, with biocide residual held

PG25 design basis · 25 % propylene glycol by volume · pH 8.8 · freeze −11 °C · boil 103 °C

06 / Sampling

Sample on a cadence, from the right point

The cadence and the panel

Every 50 to 100 days

Quarterly fits the same band. The sample is drawn from a hot closed loop, not from a drain point.

The laboratory panel

Appearance, glycol concentration, freeze point, pH, reserve alkalinity, OAT inhibitor level, electrical conductivity, ICP metals analysis, anions.

Why reserve alkalinity

It is the buffering capacity that says how much corrosion protection is left. A published PG25 fluid carries 1.4 mL 0.1 M HCl.

ICP metals analysis detects trace metals, which is how active corrosion announces itself before a pH reading moves.

07 / Maintenance schedule

What to write into the maintenance schedule

Change-out · terminal differential pressure for the element in service, not a date · Sampling · every 50 to 100 days from a hot closed loop · Instrument check · differential pressure against a known clean baseline after every element change

Particulate abrasion of a seal face is measured in weeks, and compression set in a seal in months to years. Filtration state is the one input on that list a maintenance team controls week to week.

  • EMS-CF-S08 Side-stream filtration unit, 8 % divert setpoint Vessel to 150 psi (10.3 bar); element change-out 35 psid against a 60 psid maximum. PDF
  • EMS-CF-F1-10 Pleated depth cartridge, 1 µm absolute, 10 in PDF
  • EMS-CF-F5-20 Pleated depth cartridge, 5 µm nominal, 20 in PDF
  • EMS-CF-FP-DP Element differential-pressure monitor Catalogued on the window it spans: 2 psid clean to 60 psid maximum. PDF
  • EMS-CF-WQ-C Contacting conductivity cell Cell constants 0.01 and 0.1 cm⁻¹, ranges 0.04 to 1,000 µS/cm. PDF
  • EMS-FF-FS60 Fill and flush unit, 60 L/min side-stream PDF

Send the loop volume, the current element rating, the differential pressure and the last sample result, and the reply sizes the element from those four figures.

08 / Specification sheet

Send the loop volume and the element rating

Ask for the specification sheet

The reply returns the specification sheet, the dimensional drawing and the datasheet for the code, inside one working day.

Specification request

Ask for the specification sheet

Leave your work email and the model code. One datasheet per model, with position resolution and locating repeatability stated as separate rows.

  • A specification table of at least ten rows per product family, and a downloadable PDF for every model listed.
  • Seal-life data where it decides the choice: permeation rate, compression set and fluid compatibility.
  • One working day for a reply, from an engineer rather than a catalogue autoresponder.
Reply within one working day