Page 87 - Engineering Plastics Handbook
P. 87

Processing  61

                ρ ref  = reference density
               T test  = test temperature, K
               ρ test  = test density


        Shear Rate

        Shear rate is the rate at which a layer of melt slides over the layer below.
        It is observed as velocity. Shear rate applies to nonnewtonian (shear-
        dependent) macromolecular polymeric melts and solutions. Newtonian
        fluids, typically small molecules such as H O and oil, have constant vis-
                                               2
        cosities and are not shear rate–dependent.
          Zero shear rate viscosity (the steady-state viscosity at zero shear rate)
        is influenced by the type of polymer, MW, MWD, and additives. To calcu-
        late the increase of zero shear rate viscosity with increasing MW [3], use
                                    η = KMa
                                      0
        where η = zero shear rate viscosity, s  −1
                0
               K = empirical constant
               M = molecular weight of macropolymer
                a = 3.4 at M > critical molecular weight M c
                 = 1 at M < critical molecular weight M c
          Shear rate viscosity (shear strain or stress) behavior is fundamental
        to controlling melt flow rheology. At low strain rate viscosity, the zero
        strain rate viscosity is directly related to extensional (stretching) strain
        viscosity by [3]
                                        = 3η
                                     η E    0
                                              −1
        where η = extensional strain viscosity, s
                E
               η = zero shear rate viscosity, s −1
                0
          The effects of shear on viscosity are plotted in three phases (y axis =
        log viscosity, x axis = log shear rate): I, a newtonian plateau which is the
        initial phase where the viscosity shows no change with increased shear
        rate; II, the power law region which shows a rapid drop in viscosity as shear
        rate increases; and III, the newtonian plateau which is the final phase
        where the viscosity again shows no change with increased shear rate [3].
        Newtonian law works with low shear rate, and the power law works with
        high shear rate.
          At low shear rates, polymeric liquid properties are characterized by two
                                                      and recoverable shear
        constitutive parameters: zero shear rate viscosity η 0
                     e
        compliance J 0 , which indicates fluid elasticity. At higher shear strain
        rates, rheological behavior is measured with a viscometer. Extensional
        strain viscosity, associated with extensional flow, occurs with film extrusion,
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