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                         The flow velocity v, which is calculated using Eq. (19.68), is the average velocity along the transmission
                       path between the two transducers, and so the flowmeter’s calibration will be very dependent on the flow
                       velocity profile. The problem of flow regime dependency can be significantly reduced by using a config-
                       uration of several parallel ultrasonic beams and averaging the measured mean velocity along each beam
                       to calculate the overall fluid velocity. This is analogous to numerical integration, and a wide range of
                       multibeam configurations have been proposed, each with their own advantages.
                         Single path ultrasonic transit-time flowmeters have a typical accuracy of ±2% of reading over a range
                       of at least 100:1. Although this type of flowmeter can be used with liquids or gases, clamp-on designs
                       can only be used with liquids. Multibeam flowmeters have an improved accuracy, but are more expensive.
                       However, they are finding increased use in high value applications like the custody transfer of natural
                       gas. Unlike most other flowmeters, the cost of transit-time flowmeters does not increase significantly
                       with pipe diameter. Transit-time flowmeters are intended for use with clean fluids, although most can
                       still operate if there are a small amount of impurities present in the flow.

                       The Coriolis Flowmeter
                       The Coriolis flowmeter can be used to measure the mass flowrate of a fluid directly. As the name suggests,
                       the principle of operation makes use of the Coriolis effect discovered by Gustave Coriolis in 1835. The
                       fluid being metered passes through a vibrating tube, and as a result of the Coriolis force acting on it, the
                       fluid will accelerate as it moves towards the point of maximum vibration and decelerate as it moves away.
                       This will result in flexure of the tube, the amount of flexure being directly proportional to the mass
                       flowrate of the fluid.
                         The first commercial Coriolis flowmeter used a U-shaped tube, but now many different configurations
                       exist, including dual loops and straight through designs. Each design has its own advantages, with factors
                       such as accuracy, repeatability, and pressure drop varying from design to design.
                         Whichever design is used, the Coriolis flowmeter is a high accuracy instrument, which may be used
                       to meter gas or liquid with an accuracy of typically ±0.25% of reading. Measurement range varies with
                       design, but 100:1 is possible for U-tube designs and 50:1 for straight tube designs. Since the flowmeter
                       measures mass directly, changes in density, viscosity, pressure, and temperature do not effect the calibra-
                       tion of the flowmeter. The flowmeter is also not affected by changes in flow velocity profile or other flow
                       disturbances such as swirl. The flowmeter does not obstruct the flow at all, and can be used to meter
                       flow in both directions. However, the pressure drop across U-tube designs can be a limitation with viscous
                       fluids.
                         The major disadvantage of the Coriolis flowmeter is its cost, which is high in comparison to most
                       other flowmeters. This cost may be justified in applications where the product cost is high, or where
                       mass flowrate of the fluid is required. The cost and weight of the Coriolis flowmeter increase significantly
                       with increasing pipe diameter, and as a result are usually limited to pipe diameters with diameters less
                       than 100 mm.
                         Unlike most of the flowmeters discussed so far, the Coriolis flowmeter can meter some difficult two-
                       phase flows. For example, reliable measurements of the mass flowrate of liquid/gas mixtures are possible
                       if the gas component is small and well distributed, and therefore the mixture is acting like a pseudo-
                       homogeneous fluid. The percentage of gas that can be tolerated by the flowmeter will depend on the
                       viscosity of the liquid component. The less viscous the liquid the more likely the gas is to separate out
                       and cause problems. Liquid/solids flows (slurries) may also be metered, although the user has to com-
                       promise between avoiding particle dropout and avoiding excessive fluid velocities which would result in
                       accelerated wear of the flow tube.

                       Two-Phase Flow
                       There is a growing demand in areas such as the petroleum and food industries to be able to measure
                       two-phase flows such as liquid with entrained gas, or liquid with solids. Yet the measurement of such
                       flows nearly always presents difficulties to the process engineer.


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