Page 28 - Bird R.B. Transport phenomena
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§1.1  Newton's Law  of Viscosity  (Molecular Transport of Momentum)  13

                  should  not refer  to Eq.  1.1-2  as  a  "law/'  since Newton suggested  it as  an empiricism —
                                                                                          3
                  the  simplest  proposal  that could  be  made  for  relating  the stress  and  the velocity  gradi-
                  ent.  However,  it  has  been  found  that the  resistance  to  flow  of  all  gases  and  all  liquids
                  with  molecular weight  of  less than about  5000  is described  by  Eq. 1.1-2, and  such  fluids
                  are  referred  to as  Newtonian  fluids.  Polymeric liquids,  suspensions,  pastes,  slurries,  and
                  other complex  fluids  are not described  by  Eq.  1.1-2  and are referred  to as non-Newtonian
                  fluids.  Polymeric liquids  are discussed  in Chapter 8.
                     Equation  1.1-2  may  be  interpreted  in  another fashion.  In the  neighborhood  of  the
                  moving  solid  surface  at у  = 0 the  fluid  acquires  a certain amount of  x-momentum. This
                  fluid,  in  turn, imparts momentum to the adjacent  layer  of  liquid, causing  it to remain in
                  motion  in the x direction. Hence x-momentum is being  transmitted through the  fluid  in
                  the  positive  у  direction. Therefore  r  may  also be interpreted as  the flux  of x-momentum
                                                yx
                  in the positive у direction, where the term "flux"  means "flow  per unit area." This interpre-
                  tation  is  consistent with  the molecular  picture  of  momentum transport and  the kinetic
                  theories  of  gases  and  liquids.  It also  is  in harmony with  the analogous  treatment  given
                  later for heat and mass transport.
                     The  idea in the preceding paragraph may be paraphrased by saying  that momentum
                  goes  "downhill"  from  a region  of high velocity  to a region  of  low  velocity—just  as a  sled
                  goes  downhill  from  a  region  of  high  elevation  to a  region  of  low  elevation, or  the  way
                  heat flows  from  a region  of  high temperature to a region  of  low  temperature. The veloc-
                  ity gradient can therefore be thought of as a "driving  force"  for momentum transport.
                     In  what  follows  we  shall  sometimes  refer  to Newton's  law  in  Eq.  1.1-2  in  terms  of
                  forces  (which emphasizes  the mechanical nature of  the subject)  and sometimes  in terms
                  of momentum transport (which emphasizes the analogies with heat and mass transport).
                  This dual viewpoint  should prove helpful  in physical interpretations.
                     Often  fluid  dynamicists  use  the symbol  v to represent  the viscosity  divided  by  the
                  density  (mass per unit volume)  of the fluid, thus:
                                                    v  = p/p                           (1.1-3)
                  This quantity is called the kinematic viscosity.
                     Next we  make a few  comments about the units  of  the quantities we  have  defined.  If
                  we  use  the symbol  [=] to mean "has units  of,"  then in the SI system  r XJX  [=] N/m  2  = Pa,
                  v  [ = ] m/s, and у [=] m, so that
                   x
                                                                l
                                   д  =  —тЛ —г^  [ = ] Pa)[(m/s)(m )]  l  =  Ра •  s   (1.1-4)
                                                    (
                                          \dy)
                  since the units on both sides  of  Eq.  1.1-2  must agree. We  summarize the above  and  also
                  give the units  for  the c.g.s. system  and the British  system  in Table  1.1-1. The conversion
                  tables in Appendix  F will prove to be very  useful  for  solving  numerical problems  involv-
                  ing diverse  systems  of units.
                     The  viscosities  of  fluids  vary  over  many orders  of  magnitude, with  the viscosity  of
                                        5
                  air  at 20°C being  1.8  X  10~  Pa • s and that of glycerol  being about 1 Pa •  s, with  some  sili-
                                                                                         4
                  cone oils being even more viscous.  In Tables  1.1-2,1.1-3, and  1.1-4  experimental data  are
                     3
                       A relation of the form  of Eq. 1.1-2 does come out of the simple kinetic theory of gases (Eq.  1.4-7).
                  However, a rigorous  theory for gases sketched in Appendix  D makes it clear that Eq. 1.1-2 arises as the
                  first  term in an expansion, and that additional (higher-order) terms are to be expected. Also, even an
                  elementary kinetic theory of liquids  predicts non-Newtonian behavior  (Eq.  1.5-6).
                     4
                       A comprehensive presentation of experimental techniques for measuring transport properties can be
                  found in W. A. Wakeham, A. Nagashima, and J. V. Sengers, Measurement of the Transport Properties of Fluids,
                  CRC  Press, Boca Raton, Fla. (1991). Sources for experimental data are: Landolt-Bornstein, Zahlemverte und
                  Funktionen, Vol. II, 5, Springer  (1968-1969); International Critical Tables, McGraw-Hill, New York (1926);
                  Y. S. Touloukian, P. E. Liley, and S. С Saxena, Thermophysical Properties of Matter, Plenum Press, New York
                  (1970); and also numerous handbooks of chemistry, physics, fluid dynamics, and heat transfer.
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