Symptoms pointing to entrained air (→ air separator):
Gurgling, rushing or knocking noise from pipework, especially at high points
Pump cavitation: a sound like gravel in the pump volute, vibration, seal and impeller damage
Erratic or drifting flow‑meter readings (most meter technologies are gas‑sensitive)
Air locks: sections of pipework that will not circulate
Air vent discharge that is frequent and continuous
Localized cold‑plate temperature variation across identical racks
Symptoms pointing to dissolved gas / corrosion (→ deaeration):
Water samples turning rusty, brown or black; visible magnetite on a magnet
Rising conductivity over time (from ~10 µS/cm for DI fill toward hundreds or thousands, indicating ionic accumulation from corrosion and make‑up water)
Falling pH as glycol degrades and corrosion products acidify the fluid
Progressive fouling of heat exchangers and cold plates with no obvious ingress route
Recurring filter loading — differential pressure across the strainer climbing steadily
Long service life with no degassing ever performed
Symptoms pointing to both: most real systems, unfortunately. Which is why well‑designed plants install an air/dirt separator in‑line and treat the fill water properly, adding a vacuum degasser where the asset life and the value of the protected equipment justify it.
Air and dirt separation in‑line on the return side, with stainless‑steel internals, at the point of lowest velocity and highest temperature. Combined air + dirt + magnetic units are the sensible default, especially on retrofits.
Automatic air vents at every high point. Cheap, and they prevent air locks.
Correct fill water quality. This is the cheapest form of deaeration there is. Filling with deionized or softened water and an appropriate inhibitor package removes a large share of the problem before it starts.
Filtration matched to the cold plate. The engineering rule is that the filter's absolute rating should be substantially finer than the smallest flow channel in the circuit. With 50–100 µm features in some components and 200–300 µm cold plate channels, secondary‑side filtration at 25 µm — and in some designs down to 5–10 µm — is what the equipment vendors specify.
The loop contains carbon steel or aluminium anywhere in the circuit
The protected equipment is high‑value — GPU racks at 120 kW and above certainly qualify
Asset life expectations exceed five years, which is most AI infrastructure planning horizons
Make‑up water quality is variable or the site is on a water supply with high dissolved solids
You are commissioning a large system volume where the initial oxygen charge is substantial
The specification or the consulting engineer references VDI 2035 or an equivalent closed‑loop water quality standard
You are retrofitting an existing facility into AI duty, and the loop's corrosion history is unknown. In that case: degas to remove the existing oxygen load, and install magnetic separation to capture the magnetite already circulating. Doing one without the other leaves the problem half‑solved.
Will an air separator remove dissolved oxygen?No. This is the single most important point in this article. An air separator acts on gas that has already come out of solution and formed a bubble. Gas still dissolved at the molecular level passes straight through untouched.
Is a vacuum degasser worth the cost?It depends on what it is protecting. Against a copper‑and‑stainless secondary loop with a good inhibitor package and DI fill water, the marginal benefit is smaller. Against a mixed‑metal loop with carbon steel, an uncertain fill history, and 10 MW of GPU equipment downstream, it is one of the highest‑return items in the whole plant.
How long does degassing take?It is a cyclic process. Residual levels fall progressively over hours of operation, with the whole system volume passing through the machine multiple times. The equipment is sized on system volume and target treatment time — expect a continuous side‑stream duty rather than a one‑shot treatment, particularly during commissioning.
Where should the air separator be installed?On the return side, where fluid is hottest (lowest gas solubility, so bubbles are coming out of solution) and velocity is lowest (so bubbles can rise). Installing it on the cold supply side is a common error that materially reduces effectiveness.
Does glycol change gas behaviour?Yes. Glycol solutions hold gas differently from pure water, and glycol degradation products can affect both pH and gas release. Glycol also increases viscosity, which slows bubble rise — one more reason to specify a proper microbubble separator rather than relying on gravity in a plain tank.
Do I need both on a new build?On a new build with a clean, all‑stainless‑and‑copper secondary loop, DI fill water and a good inhibitor package: an air/dirt separator plus automatic vents is usually sufficient, and deaeration can be justified for the facility water system where carbon steel is present. On a retrofit or a mixed‑metal system, specify both.
How do I verify it is working?Measure. Dissolved oxygen can be sampled and measured; conductivity and pH should be trended from commissioning; filter differential pressure should be logged. A loop with effective gas and dirt management shows stable chemistry and slowly declining filter loading after the initial commissioning flush. A loop without it shows the opposite.
Commonly referenced targets for AI cooling technology water systems — confirm against your equipment vendors' published requirements, which take precedence:
| Parameter | Typical target |
| pH (inhibited PG25) | 7.5–9.0 (fresh‑fluid specifications may allow a wider band) |
| Conductivity, initial fill (DI water) | ≤ 10 µS/cm ; PG25 as supplied typically < 1 500 µS/cm |
| Conductivity, in service | Trend it; investigate sustained rise |
| Chloride | Keep as low as practicable — commonly < 50 mg/L in liquid cooling loop specifications; stainless grade selection sets the practical ceiling |
| Particulate | ≤ 50 µm maximum, tightening to ≤ 25 µm on current‑generation platforms |
| Dissolved oxygen (post‑degassing) | < 0.1 mg/L achievable with a vacuum degasser |
| Microbiological count | Initial fill very low; operating limit commonly < 100–1 000 CFU/mL |
Two notes on these limits. First, chloride deserves special attention because it, not oxygen, is what drives pitting and stress corrosion cracking in stainless steel — a subject covered in depth in our materials guide Liquid Cooling Reservoir Materials: 304 vs 316L Stainless Steel. Second, PG25 at 25 % concentration is generally biostatic, but below roughly 10 % glycol the glycol itself becomes a food source for microorganisms, so underdosed loops can develop biological fouling.
Air separators, dirt separators, magnetic separators and vacuum degassers are all inexpensive relative to the equipment they protect. The cost of getting gas management wrong shows up years later, as cold plate fouling, as degraded heat exchanger performance, and as an unplanned coolant change‑out on a live AI cluster.
Tell us your system volume, coolant specification, materials of construction in the loop, and whether this is a new build or a retrofit, and we will recommend the right combination of separation and deaeration equipment — with sizing, installation location and water chemistry targets documented.
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