Pressure & Level Measurement
Learn gauge, absolute and differential pressure; manometers, Bourdon tubes, diaphragms, strain-gauge, capacitive and piezo-resistive sensors; smart DP transmitters, impulse lines, manifolds and remote seals; and level by DP (hydrostatic), zero elevation/suppression, bubblers, displacers, floats, radar, ultrasonic, guided-wave radar, capacitance, nuclear and level switches.
Pressure is measured everywhere — for its own sake (boiler drums, pipelines) and as the basis for flow (DP across an orifice) and level (hydrostatic head). The differential-pressure (DP) transmitter is probably the most common instrument in process plants.
Level measurement keeps tanks from overflowing or running dry. There are many technologies because liquids differ: foaming, sticky, corrosive, changing density, high pressure. Picking the wrong one is a classic cause of spills.
An analogy
Measuring level with pressure is like judging how deep a swimming pool is by how hard the water pushes on your ears at the bottom — the deeper (and denser) the water, the harder the push.
Pressure references
Gauge pressure is relative to atmosphere (tyre pressure), absolute is relative to vacuum (barometers, vapour-pressure work), differential is between two points (filters, orifices, level). Units: Pa, kPa, bar, psi, mmH₂O, mmHg — always state gauge (g) or absolute (a).
Pressure sensors
Mechanical elements turn pressure into motion, then electronics into a signal:
- Manometers (U-tube) — primary standard, ΔP = ρgh
- Bourdon tubes, bellows, diaphragms — local gauges
- Strain-gauge and piezo-resistive silicon — most electronic transmitters
- Capacitive — diaphragm between two plates, excellent for low DP
- Resonant (vibrating wire/silicon) — very stable, high accuracy
- Piezoelectric — dynamic only (combustion, blast)
Installing DP transmitters
Impulse lines connect process taps to the transmitter: slope them so gases vent (liquid service, transmitter below) or liquids drain (gas service, transmitter above). A 3- or 5-valve manifold allows zeroing and isolation. Remote diaphragm seals with capillaries avoid plugging and freezing but add temperature effects and slower response. Plugged or leaking impulse lines are the most common DP failure.
Level technologies
Select by fluid and vessel:
- Hydrostatic / DP / bubbler — simple, density-dependent
- Displacer (buoyancy) and float — mechanical, interface measurement
- Ultrasonic — non-contact, affected by foam, vapour, temperature
- Radar (80 GHz FMCW) — non-contact, unaffected by vapour/pressure
- Guided-wave radar (TDR) — probe into the liquid, interfaces, foam
- Capacitance, conductivity, vibrating fork — often as switches
- Nuclear (gamma) — through the vessel wall for extreme services
- Load cells — weigh the whole vessel
Wet legs, interfaces and density compensation
In closed pressurised vessels a DP transmitter's low side connects to the vapour space. If vapour condenses, a wet (filled) reference leg is used; its head makes the DP negative when the tank is full → zero elevation (negative LRV). Two-DP or DP + GWR combinations measure interface level and density. Boiler drum level requires density compensation because steam/water density changes with pressure — a famous cause of boiler accidents.
Formulas
- Absolute vs gauge:
P_abs = P_gauge + P_atm (≈ 101.325 kPa) - Hydrostatic pressure:
P = ρ·g·h - DP level span:
Span = ρ·g·(h_max − h_min) - Zero suppression (transmitter below tap):
LRV = +ρ·g·d - Zero elevation (wet reference leg):
LRV = −ρ_fill·g·H_leg (+ ...) - Radar/ultrasonic level:
distance = v·t/2; level = H_tank − distance - Units:
1 bar = 100 kPa = 14.504 psi; 10 m H₂O ≈ 98.07 kPa
Worked example: Absolute pressure
Given: Gauge reads 250 kPa(g), barometer 100 kPa
Find: Absolute pressure.
- 250 + 100
Answer: 350 kPa(a)
Worked example: DP level range
Given: Oil SG 0.85, 0–4 m, transmitter 0.5 m below tap
Find: Calibrated range.
- Span = 850 × 9.807 × 4 = 33.34 kPa
- LRV = 850 × 9.807 × 0.5 = 4.17 kPa
Answer: 4.17 to 37.51 kPa
Worked example: Radar level
Given: Tank 10 m, echo time 40 ns
Find: Level.
- distance = 3e8 × 40e-9 / 2 = 6 m
- 10 − 6
Answer: 4 m
Ranging a DP level transmitter
g = 9.80665
rho = 850.0 # oil, SG 0.85
h_max = 4.0 # m of level to measure
d_below = 0.5 # transmitter mounted 0.5 m below the lower tap
span = rho * g * h_max / 1000 # kPa
lrv = rho * g * d_below / 1000 # zero suppression
urv = lrv + span
print(f"span {span:.2f} kPa, LRV {lrv:.2f} kPa, URV {urv:.2f} kPa")
for h in (0, 1, 2, 4):
dp = lrv + rho * g * h / 1000
mA = 4 + 16 * (dp - lrv) / span
print(f"level {h} m -> dP {dp:6.2f} kPa -> {mA:5.2f} mA")
# span 33.34 kPa, LRV 4.17 kPa, URV 37.51 kPa
# level 0 m -> dP 4.17 kPa -> 4.00 mA
# level 1 m -> dP 12.50 kPa -> 8.00 mA
# level 2 m -> dP 20.84 kPa -> 12.00 mA
# level 4 m -> dP 37.51 kPa -> 20.00 mABecause the transmitter sits below the tap, liquid in the impulse line adds 4.17 kPa even when the tank is 'empty'. Ranging the transmitter 4.17–37.51 kPa (zero suppression) makes 4 mA = 0 m. If density changes, the level reading changes — DP level really measures mass/head, not height.
Common mistakes
- Wrong: Mixing gauge and absolute units. — Right: Always write kPa(g) or kPa(a).
- Wrong: Gas trapped in liquid impulse lines. — Right: Slope lines and vent high points.
- Wrong: Ultrasonic on foamy or vapour-laden tanks. — Right: Use radar or GWR.
- Wrong: Ignoring density change in DP level. — Right: Compensate or choose a density-independent method.
Applications
- Boilers: Drum level with density compensation and 2oo3 voting.
- Tank farms: Radar gauges for inventory and overfill protection.
- Pipelines: Pressure profiles for leak detection.
- Filters: DP indicates clogging.
Key takeaways
- State gauge/absolute/differential.
- DP level: ΔP = ρgh (density matters).
- Suppression when transmitter below tap; elevation with wet legs.
- Pick level technology by fluid behaviour.
Going further
- Multivariable transmitters: DP + static pressure + temperature for compensated flow.
- SIL-rated level: Overfill protection per API 2350 and IEC 61511.
- 80 GHz radar: Narrow beam for small tanks with internals.