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                                          Velocity profile in  Velocity profile in
                                           turbulent flow
                                                           laminar flow


                                                                  Distorted velocity profile
                                                                     after pipe bend


                       FIGURE 19.52 Flow velocity profiles in laminar and turbulent flow.

                       Reynolds number can be calculated using


                                                          Re =  rvD                             (19.65)
                                                               ----------
                                                                h
                                                 v
                       where ρ is the density of the fluid,   is the mean velocity of the fluid, D is the pipe diameter, and η is the
                       dynamic viscosity of the fluid. If Re is less than 2000, viscous forces in the flow dominate and the flow
                       will be laminar. If Re is greater than 4000, inertia forces in the flow dominate and the flow will be turbulent.
                       If Re is between 2000 and 4000 the flow is transitional and either mode can be present. The Reynolds
                       number is mainly calculated using properties of the fluid and does not take into account factors such as
                       pipe roughness, bends, and valves, which also affect the flow characteristic. However, the Reynolds number
                       is a good guide to the type of flow which might be expected in most situations.
                         The fluid velocity across a pipe’s cross section is not constant and depends on the type of flow present
                       (Fig. 19.52). In laminar flow, the velocity at the center of the pipe is twice the average velocity across the
                       pipe cross-section and the flow profile is unaffected by the roughness of the pipe wall. In turbulent flow,
                       pipe wall effects are less and the flow’s velocity profile is flatter, with the velocity at the center being about
                       1.2 times the mean velocity. The exact flow profile in a turbulent flow depends on pipe wall roughness
                       and Reynolds number. In industrial applications laminar flows are rarely encountered unless very viscous
                       fluids are being metered. The pipe Reynolds number should always be calculated since some flowmeters
                       are not suitable for use in both laminar and turbulent flow conditions.
                         A flow’s velocity profile will only be symmetrical at the end of a very long pipe. Bends and obstructions
                       such as valves will cause the profile to become distorted or asymmetric. Since the calibration of many
                       flowmeters is sensitive to the velocity profile of the flow passing through the meter then in order to have
                       confidence in the performance of a  flowmeter, the velocity profile of the  flow passing through the
                       flowmeter should be stable and known.

                       Flowmeter Classification

                       Although there at least 80 different types of flowmeter commercially available, they may be all classified
                       into nine main groups. Table 19.3 gives examples of the main types of flowmeter in each group.
                         Traditional flow measurement technologies are represented by the differential pressure, variable area,
                       positive displacement, and turbine categories. Newer techniques are represented by the electromagnetic,
                       ultrasonic, oscillatory, and mass categories. Although differential pressure flowmeters are still the most
                       commonly used method of  flow measurement, especially in the process industrial sector, in general
                       traditional methods are being increasingly replaced by newer techniques. These techniques are now often
                       preferred because in most cases they do not obstruct the flow, and yet match many of the traditional
                       flowmeters in terms of accuracy and reliability.


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