Basic options for level measurement are;
1. hydrostatic (pressure at the bottom of the liquid column)
This will be sensitive to headspace pressure and density of the liquid. Headspace pressure can be accounted for by measuring it and using the differential pressure to imply the liquid level, taking into account the density. If density varies then a third pressure sensor a known height above the bottom sensor is needed. The fluid density can be derived from this pressure differential.
2. Float and position measurement (I think this is a displacer type you refer to?)
A physical float and LVDT will provide a reliable level independent of vessel pressure. This system will be sensitive to density variations due to the float floating higher or lower.
3. Ultrasonic or Radar (distance measurement based on time of flight for a sound or radio wave)
Time of flight for reflected waves is independent of vessel pressure and fluid density. Ultrasonic (sound) can be affected by headspace density and other sources of reflections in the tank eg agitator blades and baffles. For a vacuum vessel application where variable vapour levels exist there may be an un reliable measurement. Radar is immune to headspace density variations, but more sensitive to tank internal reflections. This has been solved by the use of a guide (aerial) to reduce the false echoes.
4. Discrete level switches.
Simple robust switch at the level the process needs to be controlled to. If the control requirement is on at level 1 and off at level 2 then 2 switches can be used to reliably solve the problem.
The answer depends upon process requirements – accuracy, switching range, fulid and process conditions etc.
Mark Hutton