Page 65 - Instrumentation Reference Book 3E
P. 65

50  Measurement of  viscosity

                                                      2.5  Measurement of the
                                                      extensiona  I viscosity
                                                      Many industrial processes, especially in the poly-
                                                      mer  industries,  involve  a  high  extension-flow
                                                      component  and  there  is  an  acknowledged  need
                                                      for extensional viscometers. The construction  of
                                             Diol     such devices is, however, fraught with difficulties.
                  -_-_-_     --Fluid  level-  - - -   For example, it is difficult to generate an exten-
                             r                        rate range. Indeed, many of the most popular and
                                                      sional deformation over a sufficient deformation-
                                                      sophisticated  devices for work  on polymer melts
                               Spindle
                                                      (such  as  those  constructed  at  B.A.S.F.  in  Ger-
                                                      many) cannot  reach  the steady state required  to
                                                      in  (2.4).  Therefore,  they  are,  as  yet,  of
                      ,AI                             determine  the  extensional  viscosity  qE defined
                                                      unproven utility. A full discussion of the subject
                                    Disc
             Figure 2.8  Schematic diagramof the Brookfield   of  extensional viscometry  within  the context  of
             viscometer.                              polymer-melt  rheology  is  provided  by  Dealy
                                                      (1982).
             was probably one of the first forms of viscometer   In the case of more mobile liquid systems, it is
             ever  used  and  today  there  are  more  than  50   difficult to generate flows which approximate to
             versions of the so-called flow cups.     steady uniaxial extension and the most  that can
               Often,  results  from  flow  cups  are  simply   reasonably be hoped for is that instruments will
             expressed as  “time in  seconds”  (e.g.,  “Redwood   provide  an  estimate  of  a  fluid’s  resistance  to
             seconds”) but for Newtonian liquids these can be   stretching flows (see,  for example, Chapter 1 of
             converted  to  kinematic  viscosity  v  through  an   Walters (1980)). With this important proviso, the
             (approximate) formula of the form         Ferguson  Spin-Line  Rheometer  is  a  commer-
                 v = At - B/t                  (2.17)   cially available instrument which can be used on
                                                      mobile  liquids  to  provide  extensional  viscosity
             where A and B are constants which depend on the   information.
             cup  geometry  (see,  for  example,  Walters  and
             Barnes (1980)).
               The  second  term  on  the  right-hand  side  of
             (2.17) is  essentially  a  kinetic-energy  correction.   2.6  Measurement of viscosity
             For Newtonian  liquids,  A  and  B  can  be  deter-   under extremes of temperature
             mined  by  carrying out standard experiments on   and pressure
             liquids of known kinematic viscosity.
               A major disadvantage of the standard Ford cup   Any  of  the  techniques  discussed  above  can
             so far as non-Newtonian liquids are concerned is   be  adapted  to  study  the  effect  of  temperature
             that only one time can be taken, i.e., the time taken   and pressure on viscosity, provided the apparatus
             for the cup to empty. Such a measurement leads to   can accommodate the extremes prevailing.
             a  single  (averaged)  viscosity  for  a  complicated   It  is  important  to  emphasize  that  viscosity
             deformation regime and this is difficult to interpret   is  very  sensitive  to  temperature.  For  example,
             consistently  for  rheologically  complex  fluids.   the  viscosity of water  changes  by  3 percent  per
             Indeed, liquids with different rheologies as regards   Kelvin.  It  is  therefore  essential  to  control  the
             shear viscosity, extensional viscosity, and elasticity   temperature and to measure it accurately.
             may  behave  in  an  identical  fashion  in  a  Ford-   Pressure is also an important variable in some
             cup  experiment  (Walters  and  Barnes,  1980)  so   studies.  In  the  case  of  lubricating  oils,  for
             that shop-floor instruments of this sort should be   example, high pressures are experienced during use
             used with extreme caution when dealing with non-   and it is necessary to know the pressure-depend-
             Newtonian  liquids.  The  same  applies  to  the   ence of viscosity for these fluids.
             “flow-around-obstacle” viscometers of  Figure 2.7.   At temperatures near absolute zero measurements
             Typical  examples of  this  type  of  viscometer  are   have  been  concerned with  the  viscosity  of  liquid
             the  Glen  Creston  falling-ball viscometer and  the   helium.  Recently,  special  techniques  have  been
             Hoeppler rolling-ball instrument (see, for example,   developed. Webeler  and  Allen  (1972) measured
             Van Wazer etal. (1963) and Cheng (1979). Rising-   the  attenuation of  torsional  vibrations  initiated
             bubble  techniques  may  also  be  included  in  this   by  a  cylindrical  quartz  crystal.  Vibrating-wire
             category.                                 viscometers  have  also  been  used.  The  resonant
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