eFunda: Introduction to Coriolis Flowmeters
engineering fundamentals Coriolis Flowmeter
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Overview

Coriolis flowmeters are relatively new compared to other flowmeters. They were not seen in industrial applications until 1980's. Coriolis meters are available in a number of different designs. A popular configuration consists of one or two U-shaped, horseshoe-shaped, or tennis-racket-shaped (generalized U-shaped) flow tube with inlet on one side and outlet on the other enclosed in a sensor housing connected to an electronics unit.

The flow is guided into the U-shaped tube. When an osillating excitation force is applied to the tube causing it to vibrate, the fluid flowing through the tube will induce a rotation or twist to the tube because of the Coriolis acceleration acting in opposite directions on either side of the applied force. For example, when the tube is moving upward during the first half of a cycle, the fluid flowing into the meter resists being forced up by pushing down on the tube. On the opposite side, the liquid flowing out of the meter resists having its vertical motion decreased by pushing up on the tube. This action causes the tube to twist. When the tube is moving downward during the second half of the vibration cycle, it twists in the opposite direction. This twist results in a phase difference (time lag) between the inlet side and the outlet side and this phase difference is directly affected by the mass passing through the tube.

A more rescent single straight tube design is available to measure some dirty and/or abrasive liquids that may clog the older U-shaped design.

An advantage of Coriolis flowmeters is that it measures the mass flow rate directly which eliminates the need to compensate for changing temperature, viscosity, and pressure conditions. Please also note that the vibration of Coriolis flowmeters has very samll amplitude, usually less than 2.5 mm (0.1 in), and the frequency is near the natural frequency of the device, usually around 80 Hz. Finally, the vibration is commonly introduced by electric coils and measured by megnetic sensors.

Further Information

Suppose that the fluid is flowing into the U-shaped tube at velocity V and the tube is vibrating at angular velocity . Consider a small section of the fluid that is on the inlet side away from the point of flexture at distance r.


    Please note that the amplitudes of the vibration and twist are extremely small compared to the size of the U-shaped tube. The above graphics are highly exaggerated for illustration purposes.

The Coriolis force on the small fluid section m is

During the down cycle, the tube applys an upward resisting force to the fluid or the fluid pushes the tube down. On the outlet side, the Coriolis force has the opposite direction.

To simply the problem, we assume that the tube has a perfect U shape with a cross section area of A. The length and width are l, d, respectively. The opposite directions of Coriolis forces on inlet and outlet sides result in a twisting moment Tc

A K factor can be introduced to compensate for the more generalized U-shape.

where Qm = AV is the mass flow rate.

The governing equation of twisting is

where Iu is the inertia of the U-shaped tube, Cu is the damping coefficient, Ku is the stiffness, is the twist angle, and t is time.

Recall that the Coriolis flowmeters are vibrating the U-shaped tube to generate the rotation, the real angular velocity is function of vibrating frequency :

Assuming that the damping term Cu is negligible, the equation of twisting becomes

The particular solution (steady-state solution) of the twist angle is

Furthermore, the velocity of the turning corners of the U-shaped tube are  and the displacement difference between these two corners is d/2. Therefore, the time lag between these two corners is

By measuring the time lag , the mass flow rate can be obtained

In vibration analysis, it is custom to use the natural frequency as a basis and normalize frequency terms against it. The natural frequency of the U-shaped tube system is (note that Iu includes the mass of the fluid in the tube)

The mass flow rate then becomes

Common Specifications

Common specifications for commercially available Coriolis flowmeters are listed below:

  Fluid Phase:

Score Phase Condition
 Liquid  Clean 
  Direct Mass 
  Dirty 
  Non-Newtonian 
  Viscous 
 Slurry  Abrasive 
 Gas  Clean 
  Dirty 
 Liquid  Corrosive  
 Slurry  Fibrous 
: Recommended
: Limited applicability

  Line Size: 6 ~ 200 mm (0.25 ~ 8 inch)
  Turndown Ratio: 100 : 1

Pros and Cons

  • Pros:
  - Higher accuracy than most flowmeters
  - Can be used in a wide range of liquid flow conditions
  - Capable of measuring hot (e.g., molten sulphur, liquid toffee) and cold (e.g., cryogenic helium, liquid nitrogen) fluid flow
  - Low pressure drop
  - Suitable for bi-directional flow
  • Cons:
  - High initial set up cost
  - Clogging may occur and difficult to clean
  - Larger in over-all size compared to other flowmeters
  - Limited line size availability

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