What this category covers
Level is the measurement of a boundary rather than of a quantity: the surface between a liquid and the vapour above it, between two immiscible liquids, or between a solid and the air in a silo. Almost every difficulty in the category comes from the state of that boundary. Foam, vapour, condensation, agitation, build-up and a moving surface all change how the instrument sees it.
The practical split is between continuous measurement, which reports a value through the whole range, and point level, which reports only whether the product has reached a position. Many installations need both: a continuous transmitter for inventory and a point switch for a high-level interlock that does not depend on the transmitter being correct.
Instrument choice follows the medium and the tank rather than the accuracy requirement. A clean water tank in an open sump and a pressurised reactor with a condensing vapour are the same measurement in principle and entirely different problems in practice.
Product types in level measurement
| Product type | How it works | Usually specified for |
| Radar level transmitter | Time of flight of a microwave pulse reflected from the surface | Tanks and silos with vapour, foam or a varying dielectric; non-contact models tolerate agitated and hygienic processes |
| Guided wave radar | The same principle along a probe, which concentrates the return echo | Low-dielectric media, narrow vessels and stilling wells where a free-space beam would be disturbed |
| Ultrasonic level transmitter | Time of flight of an acoustic pulse through the vapour space | Water, wastewater and simple liquid storage where the vapour space is clean and the temperature is stable |
| Hydrostatic level transmitter | The pressure exerted by the column of liquid above the sensor | Vented tanks of known density, and wells and sumps where a simple submersible device is preferred |
| Differential pressure level | Difference between the wet leg and the measured leg of a closed tank | Pressurised and closed vessels where the top pressure must be cancelled out |
| Capacitive level sensor | Change in capacitance between a probe and the vessel wall | Short-range and point duties on clean liquids and powders |
| Float and displacer | Buoyancy acting on a float or a displaced volume | Interface measurement and simple, very reliable high-level duties |
| Vibrating fork and tuning fork switch | A change in resonant frequency when the fork is covered | Point level on liquids and powders, including high and low alarms on sticky or foaming media |
| Rotary paddle and capacitance point switch | A paddle stalls, or capacitance changes, when the product reaches it | Bulk solids, bin high-level and plug detection where a mechanical answer is acceptable |
Level gauges, sight glasses and magnetic float indicators give a direct visual reading and are listed under this category alongside the transmitters.
How to choose a level instrument
There is rarely a single correct instrument for a duty, but there is always a
shortlist that can be justified and a set of answers that eliminates the rest. These
are the questions that decide it.
- Continuous or point measurement, or both. Interlocks and alarms are frequently better served by an independent switch than by a transmitter.
- The state of the surface: foam, turbulence, a boiling liquid and a moving powder surface each eliminate technologies before accuracy is discussed.
- The vapour space above the product: condensation, dust, steam and corrosive gases affect optics and acoustics differently, and a purged installation may be required.
- Dielectric constant and density. Radar depends on the first, hydrostatic on the second, and a process that changes either one changes the reading.
- Tank geometry: nozzles, agitators, heating coils, ladders and internal structure all sit in the measurement path and have to be described.
- Pressure and temperature in the vessel, which set the flange rating and the electronics arrangement.
- Hygienic and clean-in-place requirements, which restrict the wetted materials and the crevice tolerance.
- Area classification, which determines the protection concept for the transmitter and the cabling.
- Build-up and coating behaviour: sticky, crystallising or bridging products need a technology that does not depend on a clean emitting surface.
- Mounting access, because a non-contact instrument still has to be installed, aimed and maintained at the top of the vessel.
Working through the selection in order
- Decide whether a continuous value or a point signal is required, and whether an independent switch is needed alongside a transmitter.
- Characterise the surface: still or agitated, clean or foaming, liquid or solid, single phase or with an interface.
- Characterise the vapour space: pressure, temperature, condensation, dust and corrosivity.
- Choose the technology that survives that environment, then check the dielectric constant or the density it depends on.
- Walk the measurement path from the nozzle to the bottom of the tank and list what the beam or the probe will meet.
- Set the range, the accuracy and the required resolution at the low end, where a level reading is often most critical.
- Apply the flange, the wetted materials and the area classification.
- Decide the output, whether a local display is needed, and whether a stilling well or bypass chamber should be part of the order.
Comparing the technologies
| Technology | Best suited to | Limits | Typical medium |
| Radar, non-contact | Vapour, foam, pressure and temperature; hygienic vessels | A very low dielectric constant can weaken the echo; condensation on the antenna distorts it | Chemicals, hydrocarbons, water, food products |
| Guided wave radar | Low-dielectric media and cramped vessels | The probe can be coated or bridged by build-up; not suited to heavy solids | Solvents, light oils, clean liquids |
| Ultrasonic | Simple liquids in open or vented tanks | Temperature stratification, vapour, foam and condensation all affect the speed of sound or the echo | Water, wastewater, non-hazardous storage |
| Hydrostatic | Clean liquids of known and stable density | Density changes shift the reading with no change in level; blocked impulse lines are a common failure | Water, fuels, dilute solutions |
| Differential pressure | Closed and pressurised vessels | Both legs must be rated for the vessel pressure; a wet leg must never run dry | Process vessels, boilers, columns |
| Point switches | Alarms, interlocks and pump protection | They report a position, not a value, and cannot be used for inventory | Liquids, slurries and bulk solids depending on the type |
Parameters to confirm before ordering
What is left after the technology is chosen is a list of values that only the
installation can supply. These are the ones that change the model, the price or the
lead time:
- Tank or vessel: dimensions, shape, and whether it is open, vented or closed.
- Medium and its nature: clean, viscous, sticky, foaming, granular or a two-phase interface.
- The vapour-space conditions: pressure, temperature, condensation, dust and any corrosive component.
- Dielectric constant for radar duties, or density for hydrostatic duties, where they are known.
- Internal obstructions along the measurement path: agitators, coils, ladders, baffles and nozzles.
- Continuous or point measurement, and whether an independent high-level switch is required.
- Process connection: flange or thread standard, size and rating, and the nozzle orientation.
- Wetted-material and hygienic requirements.
- Output: 4-20 mA, HART, Modbus, switch contact or local indication only.
- Area classification and the protection concept required.
Figures are quoted, not assumed
Specifications vary by model and application, so no performance figure is stated on
this page. Where a parameter has not been documented for a particular model, the
product page says so rather than filling the gap with a plausible number. Send the
values above and we will return the ones the selected model actually holds.
Where these instruments are used