Level Measurement ~ Learning Instrumentation And Control Engineering Learning Instrumentation And Control Engineering

How a Pneumatic Displacer level sensor is used to Control Liquid Level

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Although we have covered the principle of operation of the displacer level sensor before, here we attempt to introduce you how a pneumatic displacer level sensor is applied in liquid level control in a process plant. The anatomy of a typical pneumatic displacer level sensor is exemplified by the fisher 25000 controller/displacer level sensor assembly:
Fisher 2500 Pneumatic Level Sensor. Photo Credit : Fisher

Principle of Operation of the Displacer Level Sensor/Controller 

Liquid Level Controller Using a Displacer Level Sensor

As shown above, changes in the level of liquid in the vessel whose level is being controlled exerts a buoyant force on a displacer which causes the rotation of a torque tube shaft. The rotation of the torque tube shaft is converted into a proportional pneumatic output signal by the pneumatic controller attached to the displacer level sensor. Typically, this pneumatic output is 3 – 15psig. The output signal from the controller drives a dump valve open to evacuate liquid from the vessel. When liquid level rises, the buoyant force on the displacer increases leading to increasing output from the controller if it is a direct acting controller. When the liquid level falls, the buoyant force on the displacer decreases resulting in decreasing output to the controller. If the controller is set at 25% of vessel level for example, then as soon as liquid in the vessel reaches 25%, the controller outputs a signal to completely open the dump control valve to release the liquid to a dump or safe area in the case of a hazardous liquid e.g hydrocarbon condensate.





Operating Principle of Float and Displacer Level Switches and Sensors

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Float level switches and sensors operates based on Archimedes principle. The apparent weight of a floating object is reduced by the weight of the liquid displaced. Archimedes’ principles states that the buoyant force acting on an object equals the weight of the fluid displaced. As the level changes around the float and displacer materials, the buoyant force varies in proportion and can be detected as an indication of level. Floats are commonly used for point level indication while displacers can be used for continuous as well as point level indication.

Design of Float and Displacer Level Switches
The buoyant force available to operate a float level switch is the difference between the weight of the displaced fluid (gross buoyancy) and the weight of the float.

Floats and displacers are available in spherical, cylindrical and a variety of other shapes. Standard float sizes are available from 1 to 5 inches in diameter. Custom float sizes, shapes, and materials can be ordered from most manufacturers. They can be made out of stainless steel, Teflon, Hastelloy, Monel, and various plastic materials.

Floats should always be lighter than the minimum expected specific gravity, SG, of the process fluid. For clean liquids a 0.1 SG difference is desirable, while for viscous or dirty applications a difference of at least 0.3 SG is recommended. This allowance provides additional force to overcome the resistance due to friction and material build-up. In dirty applications, floats should also be accessible for cleaning so as to increase the efficiency and effectiveness of the float mechanism.

Floats can be attached to mechanical arms or levers and can actuate




SelectIion Chart for Point Level Measurement Technologies

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Point level measurement is commonly done using the following technologies
(a) Capacitance sensors
(b) Nuclear sensors
(c) Vibrating fork sensors and
(d) Float switches
The above technologies are often best suited to certain process conditions or a combination of process conditions. To apply these technologies, some questions commonly asked include:
  1. Which level measurement technology best suits density changes in the process?

  2. Which technology will suffice for a changing dielectric strength of process fluid?

  3. Which technology can be best used where you have solids, dust, foam, slurries, emulsion, internal obstructions, vapors, viscous/sticky product?

  4. Which technology is best suited for high process temperature limits, high vessel pressure limits, low process temperature limits, low vessel pressure limits?

  5. Which level measurement technology can best resist noise (EMI, motors), product coating etc?

  6. Which technology is best suited a process where there is aeration, agitation, ambient temperature changes, or corrosion?

The above questions are




How a Vibrating Fork Level Switch Works

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Vibration fork switches are only suitable for point level measurement. They consist of an oscillating or tuning fork, which resonate in air with a known natural frequency. The resonance frequency will be reduced when the fork is brought into contact with a medium. The diagram below shows tuning fork type level switches used for point level measurement:




Operating principle of Nuclear Level Sensors

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Nuclear based level measurement sensors can be used for point as well as continuous level measurement applications.  The concept of nuclear level sensors is based on the fact that certain types of nuclear radiation easily penetrate the walls of industrial vessels, but is attenuated by traveling through the bulk of material stored within those vessels. By placing a radioactive source on one side of the vessel and measuring the radiation making it through to the other side of the vessel, an approximate indication of level within that vessel may be obtained. Other types of nuclear radiation are scattered by process material in vessels, which means the level of process material may be sensed by sending radiation into the vessel through one wall and measuring back scattered radiation returning through the same wall.

In a typical industrial nuclear level measurement sensor shown below




Operating Principle of Guided Wave Radar Level Measurement Probes

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As already discussed in operating principle of non-contact radar level sensors/gauges, radar level measurement can be done using: guided and unguarded radar waves. We have already covered unguided or non-contacting radar level measurement. Here the focus is on the operating principle of guided wave radar level measurement applications.

Guided wave radar (GWR) is also called time domain reflectometry (TDR) or micro-impulse radar (MIR). In guided wave radar installations, the guided wave radar sensor/gauge is mounted on the top of a tank or chamber, and the probe usually extends to the full depth of the vessel where level measurement is required. A typical guided wave radar installation in a vessel is shown below:





Bubbler Tube System for Level Measurement – Operating Principle.

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Bubbler tubes provide a simple and inexpensive but less accurate (±1-2%) level measurement system for corrosive or slurry-type applications or in open or vented containers, especially those in harsh environments such as cooling tower sumps, swimming pools, reservoirs, vented fuel tanks, drain sumps, air washers, etc

In the bubble tube system, liquid level is determined by measuring the pressure required to force a gas into a liquid at a point beneath the surface as shown below:




Ultrasonic Level Sensors - Operating Principle

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Ultrasonic level sensors measure level by measuring the distance from the transmitter (usually located at the top of a vessel) to the surface of a process material located further below inside the vessel or tank. The time for a sound wave to travel back and forth the process material surface is used to calculate this distance, and is interpreted by the transmitter electronics as process level.

The transmitter electronics module contains all the power, computation, and signal processing circuits and an ultrasonic transducer. The transducer consists of one or more piezoelectric crystals for the transmission and reception of the sound waves. When electrical energy is applied to the piezoelectric crystals, they move to produce a sound signal. When the sound signal is reflected back, the movement of the reflected sound wave generates an electrical signal; this is detected as the return pulse. The transit time, which is measured as the time between the transmitted and return signals, is then used to infer the level of a vessel. The basic design of an Ultrasonic level instrument is shown below:




Operating Principle of Non-Contacting Radar Level Sensors/Gauges (Unguided Wave)

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Radar level instruments measure the distance from the transmitter/sensor (located at some high point) to the surface of a process material located further below in much the same way as ultrasonic level sensors, by measuring the time-of-flight of a traveling wave and then determine the level of the process material. They are regarded as continuous level measurement devices because they continue to measure level even as the level of the liquid in the vessel changes
The fundamental difference between a radar level instrument and an ultrasonic level instrument is the type of wave used. Radar level instruments use radio waves instead of sound waves used in ultrasonic instruments. Radio waves are electromagnetic in nature (comprised of alternating electric and magnetic fields), with very high frequency in the microwave frequency range – GHz.

There are two basic types of level radar instruments: guided-wave radar and non-contact wave radar. Guided-wave radar instruments use wave guide “probes” to guide the radio waves into the process liquid while non-contact radar instruments send radio waves out through open space to reflect off the process material. Note that guided-wave radar instruments are used in applications where the dielectric of the process liquid is quite low. All radar level instruments use an antenna to broadcast or send radio signals to the process liquid whose level is to be determined. The diagram below illustrates these two approaches:




Operating Principle of Displacer Level Sensors

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Displacer level sensors use Archimedes’ Principle to detect liquid level by continuously measuring the weight of a displacer rod immersed in the process liquid. The displacer is cylindrical in shape with a constant cross-sectional area and made long or short as required. Standard heights range from 14 inches to 120 inches. As liquid level increases, the displacer rod experiences a greater buoyant force, making it appear lighter to the sensing instrument, which interprets the loss of weight as an increase in level and transmits a proportional output signal. As liquid level decreases, the buoyant force on the displacer rod decreases with a corresponding weight increase which is interpreted as decreasing level by the level sensor which then give a corresponding signal output.
Shown below is a typical displacer level sensor installation:

Although the basic theory of operation has been outlined above, in a practical displacer level sensor, the construction is engineered to achieve the desired measurement objective with sophisticated electronic circuitry. In these types of displacer level sensors, the displacer is attached to a spring which restricts its movement for each increment of buoyancy (i.e. level change). A transmitter incorporating a Linear Variable Differential Transformer (LVDT) is used to track the rise and fall of the displacer rod as liquid level changes. Sophisticated electronics is then used to process the voltage signal from the LDVT into a 4-20mA output signal.

Archimedes’ Principle Applied to the Displacer
According to Archimedes’ Principle, the buoyant force on an immersed object is always equal to the weight of the fluid volume displaced by the object.
Suppose in a displacer level sensor, we have a cylindrical displacer rod with density, ρ, radius, r, length, L, and process fluid of density, У. In this installation, the length of the displacer rod is proportional to the liquid level being measured:

Volume of displacer rod, $V = πr^2L$

Note that as shown in the diagram for the displacer level sensor installation above, when the vessel is full, the displacer rod is completely immersed in the process fluid hence the volume of process fluid displaced is $V = πr^2L$. When the level of the vessel is empty or minimum, volume of process fluid displaced is V = 0

Hence:
When vessel is full, buoyant force on displacer rod is given by:
Buoyant Force                =  weight of process fluid displaced

                                       =  $πr^2L Уg$                (g = acceleration due to gravity)
Real weight of displacer   = $πr^2L ρ g$
Net weight of displacer sensed by the LVDT, transmitter and associated electronics when vessel is full is:
$ =   πr^2L ρ g - πr^2L Уg = πr^2Lg(ρ – У) = Vg(ρ – У)$
As can be seen above, the net weight sensed by the LVDT is proportional to the difference in density of the displacer rod (ρ) and that of the process fluid (У)
Therefore, the displacer rod must have a higher specific gravity than that of the liquid level being measured and have to be calibrated for the specific gravity of the liquid. Typical specific gravity range for liquids where the displacer level sensor is applied is in the range of 0.25 to 1.5. Another point worth mentioning is that the range of the displacer level instrument is dependent only upon the length (L) of the displacer rod specified for the given application.

When vessel is empty or level is minimum,
Buoyant force on displacer = 0
Hence, weight sensed by the LVDT is $= πr^2L ρ g$
The LVDT registers a voltage signal at minimum vessel level and outputs a corresponding signal. The displacer length is determined by the operating range (span) specified, the specific gravity, pressure, and temperature of the process fluid. The diameter and weight are factory calculated to ensure correct operation and providing accurate 4-20mA output.

Areas of Application
The displacer level sensor is used in level measurement applications such as knock- out pots, condensate drums, separators, flash vessels, storage vessels and receiver tanks.




Operating Principle of Capacitance Level Sensors

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Capacitance level instruments operate on the basic principle of the variation of the electrical capacity or capacitance of a capacitor formed by the sensor, vessel wall and dielectric material. A capacitor is made up of two conductive plates which are separated from each other by a dielectric. The storage capability of a capacitor defined by the capacitance, C, is directly dependent on the plate areas (A), their distance apart (d) and the dielectric constant of the material between the plates:

C = ЄA/d






Zero Elevation Calibration in Level Measurement

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Wet Leg Condition
Condensation of the gas above the process liquid slowly causes the low side of the transmitter piping to fill with liquid. The pipe is therefore purposely filled with a convenient reference fluid to eliminate this potential error. This is called a wet leg condition.

In a wet leg application, the low pressure side of the level transmitter will always experience a higher pressure than the high pressure side. This type of installation requires that the height of the wet leg will always be equal to or greater than the maximum height of the liquid column (H) inside the tank.
Consider the scenario below:




Zero Suppression Calibration in Level Measurement

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In some cases of level measurement in open tanks, the level transmitter has to be installed some distance below the base of the tank as shown below:
Zero Suppression in Open Tank Level Measurement Installation





Closed Tank Level Measurement with a DP Transmitter

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As shown below, in a close tank level measurement installation, if a gas phase exists on top of the liquid, the gas pressure must be compensated for.
Closed Tank Level Measurement Installation





Introduction to Level Measurement with Differential Pressure Transmitters

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Most level measurement done is achieved through inference. Inferential level measurement techniques obtain a level indication by monitoring the pressure exerted by the column of liquid.
The pressure exerted at the base of a column of liquid is given by:

Pressure = Height of column of liquid * Density of Liquid * Acceleration due to gravity

               Pressure  =  H*D*g
In terms of weight density(N/m3), S, we can organize the above formula to read:

               Pressure = H*S

Because the specific gravity of a liquid can be expressed as the ratio of the weight of the volume of a liquid to that of an equivalent volume of water, in level measurement applications, we can define level as:
Level = Height * Specific gravity of liquid = H * S.G
Where H = Height of liquid to be measured
S.G = Specific gravity of the liquid





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