Page 27 - Bird R.B. Transport phenomena
P. 27

12  Chapter  1  Viscosity  and  the Mechanisms  of  Momentum  Transport

                                                                              Fig.  1.1-1  The buildup to
                                                         ,  Q   Fluid initially  the steady, laminar  velocity
                                                                at rest       profile  for  a fluid  contained
                                                                              between two  plates. The
                                                                              flow is called 'laminar"  be-
                                                                              cause the adjacent layers  of
                                                                              fluid ("laminae") slide past
                                                                Lower plate
                                                                set in motion  one another  in an orderly
                                                                              fashion.



                                                           ..   Velocity buildup
                                         v x (y,  t)    c b m a 1 1  f  in unsteady  flow



                                                                Final velocity
                                                        Large t  distribution in
                                                                steady flow




                           has  been  attained,  a  constant  force  F  is  required  to  maintain  the  motion  of  the  lower
                           plate.  Common  sense suggests that this force may  be expressed as  follows:

                                                                   V
                                                                                                (1.1-1)
                           That  is,  the  force  should  be  proportional  to  the  area  and  to  the  velocity, and  inversely
                           proportional  to  the  distance between  the  plates.  The  constant  of  proportionality  д  is  a
                           property  of  the fluid, defined  to be  the viscosity.
                               We  now  switch  to  the  notation  that  will  be  used  throughout  the  book.  First  we  re-
                           place F/A  by  the  symbol  r ,  which  is  the  force  in  the  x  direction  on  a unit  area  perpen-
                                                  yx
                           dicular  to  the  у  direction.  It  is  understood  that  this  is  the  force  exerted  by  the  fluid  of
                           lesser  у  on  the  fluid  of  greater  y.  Furthermore,  we  replace  V/Y  by  -dv /dy.  Then,  in
                                                                                         x
                           terms  of  these symbols, Eq.  1.1-1  becomes
                                                                   dv
                                                                     x
                                                                                                (1.1-2) 1
                           This  equation,  which  states  that  the  shearing  force  per  unit  area  is  proportional  to  the
                           negative  of  the  velocity  gradient,  is  often  called  Newton's  law  of  viscosity}  Actually  we



                               1  Some authors write Eq. 1.1-2 in the form

                                                                   dv x
                                                                                                ( 1 Л  2 а )
                                                                                                   "
                                           2
                           in which т  [ = ] lty/ft , v  [ = ] ft/s, у [=] ft, and /JL [=] lb /ft  • s; the quantity £ f is the "gravitational
                                   ух
                                                                    m
                                             x
                           conversion factor" with the value of 32.174 poundals/lty. In this book we will always use Eq. 1.1-2 rather
                           thanEq.  l.l-2a.
                               2
                                Sir Isaac Newton (1643-1727), a professor at Cambridge University and later Master of the Mint,
                           was the founder  of classical mechanics and contributed to other fields  of physics as well. Actually Eq.
                           1.1-2 does not appear in Sir Isaac Newton's Philosophiae Naturalis Principia Mathematica, but the germ of
                           the idea is there. For illuminating comments, see D. J. Acheson, Elementary Fluid Dynamics, Oxford
                           University Press, 1990, §6.1.
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