05 · Measurement ranges & flow

Measurement ranges, range selection & volume flow measurement

Which spans ring balances cover, how accuracy depends on the range — and why differential pressure is the classic method for measuring volume flow.

Real calibration data

Frequently ordered measurement ranges

Based on a sample of over 10,000 calibration records from transmitters with electrical output (4–20 mA, LCD) from recent years — real field data showing which spans customers actually order.

−50…0…+50 Pa
18.4 %
−25…0…+25 Pa
9.6 %
−10…0…+40 Pa
8.1 %
0…50 Pa
5.9 %
−100…0…+100 Pa
3.8 %
−20…0…+20 Pa
3.2 %
0…1.000 Pa
3.2 %
0…100 Pa
2.9 %
0…500 Pa
2.8 %
−6,35…0…+6,35 mm W.C.
2.5 %
−300/0/+300 Pa
2.1 %
−500…0…+500 Pa
1.8 %
−5…0…+5 mbar
1.7 %
−200…0…+200 Pa
1.6 %
−20…0…+80 Pa
1.5 %

Source: Rixen Messtechnik · Sample of over 10,000 calibration records from transmitters with electrical output (4–20 mA, LCD) from recent years · Top 15

Available measuring ranges

Nine standard spans — custom ranges on request

Rixen ring balances are available from 40 Pa to 1,800 Pa full span. The scale can be offset symmetrically (e.g. −50…+50 Pa) or asymmetrically (e.g. −10…+40 Pa) — the measuring element remains the same.

Full spanTypical ΔPAccuracyTypical application
40 Pa5–25 Pa±1,5 PaCleanroom, OR airlocks
60 Pa10–40 Pa±1,5 PaCleanroom, laboratories
100 Pa20–80 Pa±1,5 % v. E.HVAC, filter monitoring
160 Pa30–120 Pa±1,5 % v. E.HVAC, duct pressure control
250 Pa50–200 Pa±1,5 % v. E.Fans, filters, ventilation
400 Pa80–300 Pa±1,5 % v. E.Fans, volume flow measurement
600 Pa100–500 Pa±1,5 % v. E.Industrial furnaces, biogas
1.000 Pa200–800 Pa±1,5 % v. E.Draft measurement, pressure vessels
1.800 Pa300–1.500 Pa±1,5 % v. E.High-pressure filters, compressors

Ranges < 100 Pa

±1,5 Pa

Fixed absolute accuracy. At 40 Pa full span this represents ±3.75 % FS — but in absolute terms 1.5 Pa is the relevant threshold, not the percentage.

Ranges > 100 Pa

±1,5 % v. E.

Relative accuracy based on full scale. At 1,000 Pa span this is ±15 Pa — still excellent for industrial draft and filter monitoring applications.

Accuracy in practice — spans below 100 Pa

What ±1.5 Pa really means — and what the data shows

This section applies to spans below 100 Pa. For spans of 100 Pa and above, the specification is ±1.5 % of full scale. Two figures are often cited together without explaining the difference — here is what each one means.

Specification

±1,5 Pa

for spans < 100 Pa

Maximum possible error

This is the worst-case guarantee: at no single point within the measurement range will the error exceed ±1.5 Pa. In practice this maximum typically occurs only at specific points — for example near the endpoints of an asymmetric range — and not uniformly across the entire span.

Typical delivery value

±0,49 Pa

Median error across all calibration points

This is the median of all individual measurement errors across all calibration points from a sample of over 10,000 transmitters delivered in recent years. It shows that most devices perform significantly better than the specification — but it does not mean that every individual point is within ±0.49 Pa. A device with a median of 0.49 Pa can still have individual points up to e.g. 1.3 Pa.

For dimensioning and system design, always use the specification of ±1.5 Pa (or ±1.5 % FS for ranges above 100 Pa) as the basis — not the median. The median shows that Rixen devices typically exceed the specification, but the worst-case guarantee is what counts for safety-relevant applications such as cleanroom pressure cascades.

Range selection

How to choose the right span

01

Determine operating pressures

What differential pressure occurs during normal operation? What is the conceivable maximum? The range should show the normal value at 50–70 % of scale — not at the upper stop.

02

Include a safety factor

Pressure spikes during start-up, valve slams or filter changes can briefly reach 2–3× the nominal pressure. The ring balance survives mechanical overload without drift.

03

Check accuracy requirements

For cleanroom pressure cascades with 10–20 Pa difference between stages: choose the 40 Pa or 60 Pa range — ±1.5 Pa absolute applies there. For boiler draft measurement ±1.5 % FS at 600 Pa is sufficient.

Volume flow measurement

Differential pressure and volume flow: the quadratic relationship

Wherever flow passes through a constriction — orifice plate, nozzle, Pitot tube, Venturi — Bernoulli's principle creates a differential pressure that is proportional to the square of the flow velocity.

Bernoulli / orifice equation

ΔP = k · Q²
Q = √(ΔP / k)

ΔPdifferential pressure [Pa]

Q  — volume flow [m³/h or m³/s]

k  — device coefficient (geometry, fluid, temperature)

Effect of the quadratic law

Halving the volume flow reduces the differential pressure to one quarter — not one half. This is the most common source of errors when selecting measurement ranges for flow applications.

Flow Q [%]ΔP [Pa] *Scale position
25 %6.25 Pa
3 %
50 %25 Pa
11 %
75 %56.25 Pa
25 %
100 %100 Pa
44 %
125 %156.25 Pa
69 %
150 %225 Pa
100 %

* Normalised: ΔP = 100 Pa at Q = 100 %

Lower range limit

In the lower 10 % of the flow range, differential pressure drops to just 1 % of full scale (e.g. 2.5 Pa on a 250 Pa instrument). At this level the reading falls within the instrument's hysteresis and accuracy band — results should be treated as indicative only. For reliable volume flow measurement, the minimum operating point should be at least 20–25 % of Qₐₐₘ (corresponding to approx. 4–6 % of full-scale ΔP). If the process regularly runs in this range, select a smaller measurement span.

Volume flow from differential pressure

Because ΔP = k·Q², the ring balance scale is linear in differential pressure — which corresponds to a quadratic relationship when read as volume flow. The transmitter output is also linear to ΔP. To display Q directly, the BMS or SCADA must apply the square root: Q = k·√ΔP.

Linear ΔP scale

The ring balance displays differential pressure linearly. The transmitter output is proportional to ΔP — volume flow Q = k·√ΔP is calculated in the BMS or SCADA.

Compatible with primary elements

Orifice plate, nozzle, Pitot tube or Venturi as primary element — the ring balance as secondary device.

Long-term stable under differential pressure

The mechanical measuring path without diaphragm remains calibration-stable under continuous differential pressure — no drift from diaphragm fatigue.

Practical example

Bereichswahl für eine Lüftungsanlage

Given

  • Ventilation duct with orifice plate
  • Nominal flow: 3.000 m³/h → ΔP = 150 Pa
  • Minimum flow: 1.500 m³/h → ΔP = 37,5 Pa
  • Short-term peak: 3.600 m³/h → ΔP = 216 Pa

Result

Chosen range: 250 Pa. Nominal flow corresponds to ΔP = 150 Pa (60 % of scale — optimal), minimum flow at approx. 25 % (below 20 % readings become indicative only), peak covered with margin. Accuracy: ±1.5 % FS = ±3.75 Pa at nominal. Volume flow Q = k·√ΔP is calculated in the BMS.

→ RW65, 250 Pa