Page 19 - Instrumentation Reference Book 3E
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4  Measurement of flow
           point  the motion  of  the  particles of  fluid is  not   of p1 kg and would require a force of 9.8.1 p1 N to
           all parallel to the tube walls but has a transverse   support it at a point where the gravitational con-
           velocity also. This form of flow pattern  is called   stant g is 9. 81 ds. Therefore if it is at a height of
           turbulent  flow. Summarizing, therefore,  for vel-   z  meters  above a reference plane  it would have
           ocities below the critical velocity, flow is said to be   9.81 plz joules of energy by virtue of its height.
           streamlined or laminar, and for velocities above
           the critical value flow is said to be turbulent-this
           situation is most common in practice.     1.2.1.4  Kinetic energy
             Reynolds formulated his data in a dimension-   A  fluid has this  energy by  virtue  of  its motion.
           less form                                 1 m3 of fluid of density p1 kg/m3 with a velocity
                                                    V1 ds would have a kinetic energy of (1)/(2)plV:
                                                    joules.

           where Re is the Reynolds number, D is the diameter   1.2.1.5  Pressure energy
           of the throat of  the installation, v  is velocity, p  is
           density of  fluid, and p  is absolute viscosity.  Flow   A fluid has this energy by virtue of its pressure.
           of  fluid in  pipes  is  expected  to be  laminar if  the   For example, a fluid having a volume qm3 and a
           Reynolds number is less than  2000  and turbulent   pressure of p1 Nlm2 would have a pressure energy
           if  it  is  greater than 4000.  Between these values is   of p1 v1 joules.
           the  critical zone.  If  systems  have  the  same Rey-
           nolds number  and  are  geometrically  similar they   1.2.1.6  Internal energy
           are said to have dynamic similarity.
                                                     The fluid will  also have  energy by  virtue  of  its
                                                     temperature  (i.e., heat  energy). If  there  is  resis-
           1.2.1.1  Flow profile                     tance to flow in the form of friction, other forms
           The velocity across the diameter of a pipe varies   of  internal  energy  will  be  converted  into  heat
           due  to many  influence quantities.  The  distribu-   energy.
           tion  is termed the velocity profile of  the system.
           For laminar  flow the profile is parabolic in  na-   1.2.1.7  Total energy
           ture.  The  velocity  at  the  center  of  the  pipe  is
           approximately  twice the mean velocity. For tur-   The  total  energy  E  of  a  fluid  is  given  by  the
           bulent flow, after a sufficient straight pipe run the   equation
           flow profile becomes fully developed.    total energy (E) =potential  energy
             The concept of “fully developed flow” is critical
           to  good  flow  measurement  system  design.  In  a    +kinetic energy
           fully developed flow, the velocity at the center of    +pressure energy
           the pipe is only about 1.2 times the mean velocity.    +internal energy
           This is the preferred flow measurement situation.
           It permits the most accurate, most repeatable, and   E=P.E.+K.E.+PR.E.+I.E.  (1.2)
           most linear measurement of flow.
                                                     1.2.2  Viscosity
           1.2.1.2  Energy of aJZuid in motion       Viscosity is the frictional resistance that exists in a
           Let’s look at the forms in which energy is repre-   flowing fluid. It will be discussed in more detail in
           sented  in  a  fluid  in  motion.  This  will  help  to   the  next  chapter.  Briefly,  the  particles  of  fluid
           understand  the  use  of  the  Reynolds  number  in   actually in contact with the walls of the channel
           universal  flow  formulas.  The  basic  types  of   are at rest, while those at the center of the channel
           energy associated with a moving fluid are:   move  at maximum velocity. Thus,  the layers of
                                                    fluid near  the center, which are moving at max-
           (a)  Potential energy or potential head.   imum velocity, will be slowed down by the slower
           (b)  Kinetic energy.                     moving layers, and the slower moving layers will
           (c)  Pressure energy.                    be speeded up by the faster moving layers.
           (d)  Heat energy.                          Dynamic  viscosity  of  a  fluid  is  expressed  in
                                                    units  of Ns/m2. Thus a fluid has a dynamic vis-
           1.2.1.3  Potential energy                cosity of  1 Nslm’  if  a force a  1 N  is required  to
                                                    move a plane of  1 m2 in area at a speed of  1 m/s
           The fluid has this energy by virtue of its position   parallel to a fixed plane, the moving plane being
           or height  above  some fixed level. For  example,   lm away  from  the  fixed  plane  and  the  space
           1 m3 of liquid of density p1 kg/m3 will have a mass   between  the planes  being completely filled with
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