The hydrostatic pressure is the pressure inside a liquid and always acts vertically towards all limiting walls of the container. As the level in such a vessel rises, so does the pressure. A sensor (transmitter) at the bottom of the vessel, can measure, display and output this pressure variations to the PLC. Since the pressure acts on all sides, the sensor diaphragm can be mounted at the bottom of the vessel or laterally at the bottom edge of the vessel, depending on which installation situation is more suitable.
To transmit the measurement results to the PLC, pressure transmitters use a piezoelectric signal converter internally, which converts the mechanical process pressure from the pressure diaphragm into a proportional voltage signal. This is then converted into a 4…20 mA standard signal or other protocol according to the customer’s adjustment.
Modern measuring systems, such as the L3, already offer the possibility of converting the measured pressure values in the sensor electronics and thus directly outputting volume or mass. For this purpose, further parameters must be determined, such as the container shape, the medium, and the process temperature (for the calculation of the respective specific density). In the case of the L3, the integrated temperature compensation provides a higher accuracy over the entire process temperature range than conventional hydrostatic level transmitters. This enables the display of the sensor in liters, kg, or other volume units with a very high measuring accuracy, even with dynamic temperature curves.
In an open system (vessel with atmospheric pressure), a pressure sensor at the bottom of the vessel is sufficient since the external pressure conditions do not change.
A closed system (pressure vessel), on the other hand, can be subjected to varying pressures, which affects the pressure at the bottom of the vessel. To measure the level in such a system, two sensors are required which separately determine the process pressure at the bottom and the head pressure at the top. The differential pressure can then be calculated from this in the PLC or an evaluation unit, and thus the correct fill level displayed.