Page 165 - Mechanical Engineer's Data Handbook
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154                                                 MECHANICAL ENGINEER’S DATA  HANDBOOK


             Channels

             Symbols used :
             m = hydraulic mean radius = A/P
              i=slope of  channel                        Values of K
             C = constant = 87/[ 1 + (K/&)]
             A=flow  area                                Surface                        K
             P = wetted perimeter
             Mean velocity V= ~Jmr                       Clean smooth wood, brick, stone   0.16
                                                                                        0.28
                                                         Dirty wood, brick, stone
                                                         Natural earth                  1.30
             Flow rate Q= VA

             Maximum discharge for given excavation

             Channel             Condition           Arrangement
             Rectangular         d=b/2
             Trapezoidal         Sides tangential to
                                   semicircle
















                                                         Let  :
             4.3.3   Venturi, orifice and pipe nozzle
                                                         D = pipe diameter
                                                          d = throat diameter
             These are used for measuring the flow of  liquids and
                                                          p = fluid density
             gases.  In  all  three  the  restriction  of  flow  creates  a   p,  =density  of  manometer fluid
             pressure  difference  which  is  measured  to  give  an   p1 =upstream  pressure
             indication of the flow rate. The flow is always propor-   p = throat pressure
             tional to the square root of  the pressure difference so   C,  = coefficient of  discharge
             that these two factors are non-linearly related. The   h = manometer reading
             venturi gives the least overall pressure loss (this is often
             important), but is much more expensive to make than   Flow rate Q = C,E  4 /?
             the  orifice which  has  a much  greater  loss.  A good
             compromise is the pipe nozzle. The pressure difference
             may be measured by means of a manometer (as shown)
             or any other differential pressure device.
               The formula for flow rate is the same for each type.
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