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Pressure · 2.2

Pressure transmitters: choosing the range, damping and overpressure rating

26 October 2026 · 9 min read · IEC 60770-1, NAMUR NE43

In short

Pressure transmitters are the workhorse of any plant, and most are specified from the same few datasheet lines: range, sensor limit, overpressure, damping and failure mode. Each has a rule, and getting them wrong shows up later as nuisance trips, slow trips or a damaged sensor after the hydrotest.

Where this matters

How it works

Range against process data

Line up the process values and place them on the range:

% of span = (P − LRV) / (URV − LRV) × 100

The usual targets are normal at 50–75 %, maximum operating below about 90 %, and trip and alarm points inside the range with margin, never at the very end.

Sensor limit and overpressure

The sensor's URL must be at or above the URV, with turndown kept sensible (article 1.4). The overpressure limit is the pressure the transmitter survives without a shift. It must be above the design pressure, and also above the test pressure if the transmitter stays connected during the hydrotest. Otherwise, isolate it or remove it.

Damping

Damping is a first-order lag with time constant τ:

step: reading reaches 63 % in τ, 95 % in 3τ ramp at rate R: lag = R × τ

A 2 s damping sounds harmless, but on a pressure rising at 1 bar/s the reading trails the real pressure by 2 bar.

Failure mode

Set the failure direction to upscale (≥ 21 mA) or downscale (≤ 3.6 mA) per NAMUR NE43, so the DCS or SIS reacts the safe way. For a high-pressure trip, upscale failure trips the plant, and the reverse fails to trip. The choice comes from the safety review.

What the standards and practice say

Worked example: a pump discharge transmitter

InputValue
Normal / maximum operating12 / 15 barg
High-pressure trip18 barg
Design pressure / hydrotest (1.5 ×)20 / 30 barg
Pressure rise rate on blocked outletabout 1 bar/s

Step 1, range. Try 0–25 barg. Normal 12/25 = 48 %, maximum 15/25 = 60 %, trip 18/25 = 72 %. All are inside the range with margin. (0–20 barg would put the trip at 90 %, too close to the end.)

Step 2, sensor. The URL must be at least 25 bar, and the overpressure limit at least 30 barg if the transmitter stays in during the hydrotest. A common 0–70 bar sensor gives a turndown of 70/25 = 2.8 : 1. That's fine.

Step 3, damping.

Damping τLag on a 1 bar/s riseReal pressure when the reading hits 18 barg
0.2 s0.2 bar≈ 18.2 barg
2 s2 bar≈ 20 barg (at design pressure)

Step 4, failure. This is a high trip, so set upscale failure, and alarm on the failure current in the SIS.

What this example shows

When it fails: the fixes in order

  1. Noisy reading: fix the cause first (pulsation, a poor tapping or a gas pocket). Then use a snubber. Add damping last, and only on indication.
  2. Nuisance trips: check that the range puts the trip well inside it, and use a voting arrangement (2oo3) rather than heavy damping.
  3. Shifted after the hydrotest: recalibrate, then change the procedure or the sensor rating.
  4. Reading pinned at 20.5 mA: the range is too small for the process. Re-range from fresh process data.

Common mistakes

Checklist

Quick reference

Further reading

The example values are illustrative. Use the project's process data, the hydrotest procedure and the safety review for real settings. NAMUR and IEC are named for identification only.