Updated: May 5, 2026 — by Sino-Inst Engineering Team
A dew point meter for compressed air tells you the moisture floor your dryer is actually delivering, expressed as pressure dew point (PDP). For instrument air on a 7 barg system, PDP must sit at or below the ISO 8573-1 humidity class your downstream equipment requires — typically Class 2 (-40 °C PDP) for pneumatic controls and Class 4 (+3 °C PDP) for general plant air. Get it wrong and you get rusted manifolds, frozen valve actuators, and contaminated paint lines.
This guide covers what PDP is, the ISO 8573-1 humidity classes that drive sensor selection, how to size and place a probe, and the 4 mistakes that cause field readings to drift within months.
Contents
- What is pressure dew point and how is it different from atmospheric dew point?
- ISO 8573-1 humidity classes: which one does your application need?
- Which dryer technology hits which PDP?
- Where should you install a dew point probe in a compressed air line?
- Calibration and drift: why a 1-year-old sensor reads 8 °C high
- Featured dew point meters for compressed air
- FAQ
What is pressure dew point and how is it different from atmospheric dew point?
Pressure dew point is the temperature at which water vapour condenses out of compressed air at the line pressure. Atmospheric dew point is the same temperature measured after the air has been expanded back to 1 atm. The two numbers are not interchangeable — a sample at 7 barg with a +3 °C PDP corresponds to roughly -23 °C atmospheric dew point, a 26 °C gap.
This matters because compressed air specifications are written in PDP, but cheap psychrometric instruments often report atmospheric dew point. If you take a hand-held meter, vent the sample, and read -23 °C, you have not exceeded ISO 8573-1 Class 4 — you have met it. Reading the wrong column on the spec sheet has flunked more compressed-air audits than any actual dryer fault. Always confirm whether the figure is at line pressure or after expansion.
ISO 8573-1 humidity classes: which one does your application need?
ISO 8573-1:2010 defines seven humidity classes. The class number you have to meet depends on what the air feeds, not on the dryer you happen to own. Pick the class first, then the sensor range falls out of it.
| Class | PDP target | Typical use | Sensor range needed |
|---|---|---|---|
| 1 | ≤ -70 °C | Pharma, semiconductor, breathing air | -100 to -40 °C |
| 2 | ≤ -40 °C | Instrument air, paint spray, food packaging | -80 to -20 °C |
| 3 | ≤ -20 °C | Plant control air in cold climates | -60 to 0 °C |
| 4 | ≤ +3 °C | General plant air, pneumatic tools | -20 to +20 °C |
| 5 | ≤ +7 °C | Light pneumatic load (refrigerant dryer) | -10 to +20 °C |
| 6 | ≤ +10 °C | Coarse air, agitation | 0 to +30 °C |
| X | User-defined | Process-specific | By spec |
One mistake to watch: a Class 2 sensor (-80 to -20 °C) loses resolution above -20 °C, so it cannot reliably tell you whether you have exceeded Class 4. Spec to your worst-case PDP target plus 20 °C of headroom, not your best-case.
Which dryer technology hits which PDP?
The dryer fixes the floor your sensor will see; pick the right pair so the sensor sits in the middle of its calibrated range.
- Refrigerant dryer: +3 to +10 °C PDP. Cheapest, used for Class 4–6.
- Heatless desiccant dryer: -40 °C PDP nominal, -70 °C achievable. Class 2 standard, Class 1 with tight switching.
- Heated desiccant dryer: -40 to -70 °C PDP, lower purge loss than heatless.
- Membrane dryer: -20 to -40 °C PDP for low-flow point-of-use.
If your specification calls for Class 2 but you only own a refrigerant dryer, no amount of sensor calibration fixes that — you need to add a desiccant tower. The dew point meter for compressed air is a diagnostic tool, not a corrective one. For broader gas-dew-point context (CO₂, N₂, hydrocarbons), see our guide to what gases a dew point meter can detect.
Where should you install a dew point probe in a compressed air line?
Install the probe at least 2 metres downstream of the dryer outlet and upstream of any after-filter that might trap moisture. Sensor response time is dominated by gas exchange around the polymer film, not by the electronics, so use a sample cell with a constant 1–2 NL/min purge to reach 90 % response inside 5 minutes. Without the purge, dead-end probes can take an hour to settle after a flow upset. The same straight-run logic that shapes flow-meter placement applies — see our upstream and downstream straight pipe guide for the underlying sampling principle.
Three placement rules from field installations:
- Mount the probe horizontally, never sensor-down. Liquid water collecting on the polymer destroys the calibration in hours.
- Use stainless or PTFE in the sample line. PVC and rubber outgas plasticisers that load the sensor.
- Keep the sample line under 5 m. Long lines act as moisture buffers and slow the reading.
For background on differential pressure across the sample cell, see our static vs dynamic pressure guide.
Calibration and drift: why a 1-year-old sensor reads 8 °C high
Polymer-capacitive dew point sensors drift by 2–3 °C per year in clean air and 5–10 °C in oily air. Four practical errors accelerate that:
- Skipping the after-filter. Compressor oil mist coats the polymer and shifts the calibration warm.
- Wet exposure. A single bulk-water hit can damage the dielectric layer permanently.
- Neglecting auto-cal cycles. Modern sensors run a 200 °C bake every 24 h to drive moisture out; if power is interrupted, drift compounds.
- Annual factory cal that ignores process conditions. A sensor returned for cal at -40 °C reference will not match a +3 °C process. Cal at the band you actually run in.
For pressure-side troubleshooting that often masquerades as dew point drift, our pressure transmitter installation guide covers the same impulse-line issues from the moisture side.
Featured dew point meters for compressed air

Dew Point Transmitter 608 Series
In-line probe, -80 to +20 °C PDP, 4-20 mA / RS485 Modbus, ±2 °C accuracy.
FAQ
What is the dew point limit for compressed air?
It depends on the ISO 8573-1 class your downstream equipment requires. Instrument air is usually Class 2 at -40 °C PDP; general plant air is Class 4 at +3 °C PDP. There is no single number.
How do you measure the dew point of compressed air?
With a polymer-capacitive sensor mounted in a sample cell at line pressure, with 1-2 NL/min purge through the cell. Allow 5-15 minutes for the reading to settle on each new measurement.
What is the difference between pressure dew point and atmospheric dew point?
Pressure dew point is measured at line pressure; atmospheric dew point after expansion to 1 atm. PDP is the higher number — 7 barg air at +3 °C PDP equals roughly -23 °C atmospheric dew point.
What is the best dew point for instrument air?
ISA-7.0.01 calls for instrument air at least 10 °C below the lowest ambient temperature the air will see. In most temperate plants this means -40 °C PDP (Class 2); in arctic service, -70 °C PDP (Class 1).
How often should a compressed air dew point sensor be calibrated?
Annually for clean instrument air, every 6 months for plant air with oil-lubricated compressors. Send the sensor back at the PDP band you actually operate in, not the factory default.
Can a dew point meter be installed downstream of an oil filter?
Yes — and it should be. Place the probe after the coalescing oil filter but before the after-filter; oil mist on the polymer is the fastest way to ruin the sensor.
What gases other than air can a dew point meter measure?
Nitrogen, hydrogen, CO₂, natural gas and most non-corrosive process gases — calibration constants are gas-specific.
Need help picking a dew point meter for your dryer and ISO 8573-1 class? Our engineers can quote and ship within 24 hours — message us with your line pressure, target PDP and flow rate.
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Wu Peng, born in 1980, is a highly respected and accomplished male engineer with extensive experience in the field of automation. With over 20 years of industry experience, Wu has made significant contributions to both academia and engineering projects.
Throughout his career, Wu Peng has participated in numerous national and international engineering projects. Some of his most notable projects include the development of an intelligent control system for oil refineries, the design of a cutting-edge distributed control system for petrochemical plants, and the optimization of control algorithms for natural gas pipelines.


