Industry News
Home / News / Industry News / What is the problem with the Coriolis flow meter?
Get in Touch

If you need any help, please feel free to contact us

What is the problem with the Coriolis flow meter?


In the field of industrial process control and fluid dynamics, accurate flow measurement is essential for maintaining product quality, ensuring process safety, and optimizing operational efficiency. Among the various technologies available, the Coriolis Mass Flowmeter has earned a reputation as one of the most advanced and accurate instruments for measuring fluid flow. By measuring mass flow directly rather than relying on volume, which fluctuates with temperature and pressure changes, this device provides exceptional precision under controlled conditions.

However, despite its widespread adoption in industries such as oil and gas, chemical processing, and food production, this technology is not without its challenges. In real world industrial environments, engineers and operators frequently encounter specific operational limitations and technical problems that can degrade the performance of these instruments.

Understanding these limitations is critical for proper instrument selection, system design, installation planning, and long term maintenance. This detailed guide explores the fundamental issues associated with the Coriolis Mass Flowmeter, analyzing the mechanical, environmental, and fluid properties that can compromise its accuracy and reliability.

Fundamental Principles of Coriolis Mass Flow Measurement

To analyze the problems that can occur within a Coriolis Mass Flowmeter, it is first necessary to understand the physics of its operation and the delicate balance required to maintain its high level of precision.

How the Coriolis Force is Utilized

The operation of a Coriolis Mass Flowmeter relies on the principles of rotational mechanics and vibration. The instrument contains one or two measuring tubes that are artificially vibrated at their natural resonant frequency by an electromagnetic drive coil. When a fluid, whether liquid or gas, flows through these vibrating tubes, it is forced to accelerate as it moves toward the point of maximum vibration and decelerate as it moves away from it. This acceleration and deceleration generate a Coriolis force that acts on the tube walls.

Because the fluid is flowing in and out of the tube simultaneously, the Coriolis force acts in opposite directions on the inlet and outlet sides of the loop. This opposing force causes the vibrating tubes to twist slightly. Highly sensitive electromagnetic sensors, known as pickoffs, are positioned at the inlet and outlet sections to detect the physical movement of the tubes.

The phase shift, or time difference, between the signals received by these two sensors is directly proportional to the mass flow rate passing through the meter. Because the time differences being measured are incredibly minute, often in the range of nanoseconds, any external disruption to this delicate vibration can lead to significant measurement errors.

The Importance of Zero Stability and Calibration

The accuracy of a Coriolis Mass Flowmeter depends heavily on a parameter known as zero stability. Zero stability represents the maximum error that can occur when there is absolutely no fluid flowing through the meter. Ideally, when the flow rate is zero, the phase shift between the two pickoff sensors should be exactly zero. However, physical factors such as manufacturing tolerances, temperature gradients across the meter body, and mounting stresses can introduce a small residual phase shift.

Manufacturers calibrate each meter to compensate for this offset, establishing a baseline zero point. However, if the physical state of the meter changes after installation, the zero point can drift. This zero drift is particularly problematic at the lower end of the meter's operating range, where the actual phase shift caused by fluid flow is very small. If the zero point drifts even slightly, the percentage error of the flow reading at low flow rates can become exceptionally high, rendering the measurements unreliable.

Primary Operational Challenges and Limitations

The most common problems encountered with a Coriolis Mass Flowmeter in industrial applications are related to the physical characteristics of the process fluid and the surrounding environment.

Sensitivity to External Vibration and Structural Noise

The most significant and persistent problem with the Coriolis Mass Flowmeter is its vulnerability to external mechanical vibration and acoustic noise. Because the meter relies on the precise excitation and measurement of a specific resonant frequency, any external vibration that matches or lies close to this operating frequency will interfere with the pickoff sensors.

In industrial plants, vibrations are constantly generated by nearby machinery, including positive displacement pumps, rotary compressors, control valves, and heavy blending equipment.

If these external vibrations travel through the piping system and reach the flowmeter, they can disrupt the clean harmonic oscillation of the measuring tubes. The transmitter, which processes the signals from the pickoff sensors, struggles to distinguish between the phase shift caused by the Coriolis force and the phase shift induced by external noise.

This interference can manifest as highly erratic flow readings, sudden spikes in measurement data, or a complete failure of the meter to lock onto its resonant frequency, resulting in system shutdown. To prevent this, engineers must implement costly isolation strategies, such as anchoring the piping securely on both sides of the meter and using flexible pipe connectors.

Entrained Gas and Two Phase Flow Disruption

Another major limitation of standard Coriolis Mass Flowmeters is their performance when measuring liquids that contain entrained gases, a condition commonly referred to as two phase flow. In many industrial processes, liquids naturally contain small air bubbles, dissolved gases, or gas pockets caused by splashing, chemical reactions, or changes in pressure.

When a homogeneous liquid flows through the vibrating tubes of the meter, the liquid moves in perfect unison with the tube walls. However, when gas bubbles are introduced, the difference in density between the liquid and the gas causes them to move at different velocities, a physical phenomenon known as decoupling.

The gas bubbles cushion the movement of the liquid, absorbing the vibrational energy of the tube. This absorption dampens the oscillation, requiring the meter's drive coil to consume significantly more electrical current to maintain the required vibration amplitude.

If the gas volume fraction becomes too high, the drive current will reach its maximum limit, a condition known as drive gain saturation. When this occurs, the meter can no longer maintain stable tube vibration, leading to a complete loss of measurement or massive measurement errors that can easily exceed twenty percent of the actual flow rate.

+-------------------------------------------------------------+
|               LIQUID AND GAS DECOUPLING EFFECT              |
+-------------------------------------------------------------+
|                                                             |
|     Vibrating Tube Wall                                     |
|     ===================================================     |
|              ▲                ▲                 ▲           |
|              |                |                 |           |
|         [  Liquid  ]     [Gas Bubble]      [  Liquid  ]     |
|              |                |                 |           |
|              ▼                |                 ▼           |
|                         [Moves Faster]                      |
|                                                             |
|     ===================================================     |
+-------------------------------------------------------------+

Fluid Viscosity and Pressure Drop Penalties

While Coriolis Mass Flowmeters are capable of measuring highly viscous fluids such as molasses, crude oil, and heavy polymers, doing so introduces a severe operational penalty in the form of a high pressure drop. To measure flow with high accuracy, many Coriolis meters utilize a bent tube design, splitting the fluid flow into two narrow, curved tubes. This geometry creates a tortuous path for the fluid, which naturally increases resistance to flow.

When highly viscous fluids are forced through these narrow, curved channels, the friction between the fluid molecules and the tube walls increases exponentially. This high friction results in a significant drop in pressure across the meter.

To maintain the desired flow rate, the process pumps must work much harder, consuming more energy and increasing wear on pump seals and impellers. If the pressure drop is too severe, it can cause the pressure of volatile liquids to fall below their vapor pressure, leading to cavitation or flashing within the meter, which not only ruins measurement accuracy but can also physically erode the interior surfaces of the measuring tubes.

Comparison of Industrial Flowmeter Technologies under Challenging Conditions

The following table provides a comparative analysis of how different common industrial flowmeters perform when subjected to various environmental and fluid challenges, highlighting why Coriolis technology is selected despite its specific limitations.

Flowmeter Technology

Sensitivity to External Vibration

Impact of Two-Phase Flow (Entrained Gas)

Pressure Drop Penalty

Relative Capital and Installation Cost

Coriolis Mass Flowmeter

Exceptionally high; requires structural isolation

Severe; causes decoupling and drive gain saturation

High; particularly in bent-tube designs with viscous fluids

Very high; requires premium materials and transmitters

Electromagnetic Flowmeter

Low; unaffected by pipe vibrations

Moderate; bubbles cause noise but do not stop operation

Negligible; features a completely unobstructed bore

Moderate; cost increases with larger pipe diameters

Ultrasonic Flowmeter

Low; but acoustic noise can interfere with signals

High; bubbles scatter ultrasonic transit signals

Negligible; non-intrusive clamp-on options available

High; especially for high-accuracy multi-path meters

Vortex Shedding Flowmeter

High; pipe vibration can mimic vortex signals

High; changes fluid density and disrupts vortex formation

Low to moderate; requires a bluff body in the flow stream

Low to moderate; economical for steam and gas utility lines

Structural and Installation Induced Vulnerabilities

The physical design and installation requirements of Coriolis Mass Flowmeters introduce several potential failure points that operators must manage carefully.

Piping Stress and Alignment Issues

Coriolis Mass Flowmeters are incredibly sensitive to any external mechanical forces applied to the meter body. When a meter is bolted into a piping system, it should ideally experience zero mechanical tension or compression. However, in real world installations, piping segments are frequently misaligned, unevenly supported, or subject to thermal expansion and contraction.

If the adjacent pipes are forced into alignment with the meter flanges, they transfer significant torsional, tensile, or compressive stresses directly onto the sensor housing. These external forces alter the mechanical resonance frequency of the internal measuring tubes, much like tuning a guitar string changes its pitch.

This frequency shift directly interferes with the zero stability calibration, leading to constant measurement drift. Furthermore, high piping stress can cause mechanical fatigue at the weld joints where the measuring tubes meet the manifold, eventually leading to structural cracking, fluid leaks, and catastrophic instrument failure.

High Initial Capital Cost and Physical Footprint

From an economic and space planning perspective, Coriolis Mass Flowmeters present a significant challenge. The raw materials and manufacturing precision required to build these instruments, such as utilizing corrosion resistant alloys like Hastelloy or titanium for the measuring tubes, make them far more expensive than other flowmeter technologies of equivalent pipe size. For large diameter pipelines, the cost of a single Coriolis meter can be prohibitive.

Additionally, the physical size and weight of these meters, particularly those with curved tubes, are substantial. A large Coriolis meter can weigh hundreds of kilograms, requiring dedicated structural steel supports to prevent the weight of the instrument from sagging the pipeline.

The large physical footprint also makes retrofitting these meters into existing, compact piping arrangements extremely difficult, as they require long, straight runs of pipe and ample clearance space for the large, bulky sensor housing.

Diagnostics, Troubleshooting, and Mitigation Strategies

Despite these challenges, the unique capability of the Coriolis Mass Flowmeter to provide direct mass flow measurement means that manufacturers and operators have invested heavily in developing effective troubleshooting and mitigation techniques.

Implementing Advanced Digital Signal Processing

To combat the issues of external vibration and two phase flow, modern Coriolis transmitters are equipped with highly sophisticated digital signal processing electronics. These advanced transmitters utilize high speed microprocessors to analyze the raw signals from the pickoff sensors in real time.

By applying digital filtering algorithms, such as Fourier transform analysis, the transmitter can isolate the specific frequency of the measuring tubes from the random background noise of the industrial plant.

Furthermore, some advanced transmitters can dynamically adjust the drive power supplied to the coil within microseconds, allowing the meter to maintain stable tube oscillation even during brief periods of high gas entrainment. This active drive management significantly reduces the frequency of meter dropouts and improves measurement consistency in challenging chemical processes.

Proper Installation and Mechanical Isolation Techniques

Many of the problems associated with piping stress and vibration can be entirely avoided by adhering to strict installation guidelines. When installing a Coriolis Mass Flowmeter, the piping on both sides of the instrument must be rigidly anchored to solid structural supports, such as concrete floors or heavy steel beams. This anchoring ensures that any vibration traveling down the pipeline is diverted to the ground before it can reach the sensitive sensor housing.

Additionally, the meter must be installed in the correct physical orientation based on the characteristics of the process fluid. For liquid applications, the measuring tubes should point downward, a configuration that allows any trapped gas bubbles to rise and escape the meter rather than accumulating in the tubes.

For gas applications, the tubes should point upward, allowing any condensed liquid droplets to drain naturally out of the meter under the force of gravity.

For slurry applications, mounting the meter vertically with the fluid flowing upward is highly recommended, as this prevents heavy solid particles from settling out of the fluid and accumulating in the bottom of the measuring tubes, which would cause severe imbalance and measurement errors.

Managing Aerated Liquids with System Backpressure

When dealing with entrained gas in liquid lines, operators can often mitigate the decoupling effect by manipulating the process pressure. By installing a control valve downstream of the Coriolis Mass Flowmeter, operators can intentionally increase the backpressure within the meter body.

Increasing the fluid pressure causes the entrained gas bubbles to compress in size, following the laws of thermodynamics.

As the bubbles shrink, their volume fraction decreases, and they become more tightly coupled with the surrounding liquid. This reduction in bubble volume minimizes the damping effect on the measuring tubes, allowing the meter to maintain stable oscillation and restore its high level of measurement accuracy without requiring physical modifications to the process fluid.