Page 521 - Carrahers_Polymer_Chemistry,_Eighth_Edition
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484                                                    Carraher’s Polymer Chemistry



                    The viscous component is dominant in liquids, hence their flow properties may be described by
                 Newton’s law (Equation 14.3) where η is the viscosity, which states that the applied stress s is pro-
                 portional to the rate of strain dγ /dt, but is independent of the strain γ   or applied velocity gradient.
                                                          dγ
                                                      S  = η                                (14.3)
                                                           dt
                    Both Hooke’s and Newton’s laws are valid for small changes in strain or rate of strain, and
                 both are useful in studying the effect of stress on viscoelastic materials. The initial elongation of a
                 stressed polymer below T  is reversible elongation due to a stretching of covalent bonds and distor-
                                      g
                 tion of the bond angles. Some of the very early stages of elongation by disentanglement of chains
                 may also be reversible. However, the rate of flow, which is related to slower disentanglement and

                 slippage of polymer chains past one another, is irreversible and increases (and η decreases) as the
                 temperature increases in accordance with the following form of the Arrhenius equation (Equation
                 14.4) in which E is the activation energy for viscous fl ow.
                                                     η = Ae E/RT                            (14.4)

                    It is convenient to use a simple weightless Hookean, or ideal, elastic spring with a modulus G and
                 a simple Newtonian (fl uid) dashpot or shock absorber having a liquid with a viscosity of η as models
                 to demonstrate the deformation of an elastic solid and an ideal liquid, respectively. The stress–strain
                 curves for these models are shown in Figure 14.1.

                    In general terms, the Hookean spring represents bond flexing and slight separation of the atoms
                 while the Newtonian dashpot represents chain and local segmental movement. It is customary to
                 attempt to relate stress–strain behavior to combinations of dashpots and springs as indicators of the
                 relative importance of bond flexing and segmental movement.

                    Again, in general terms, below their T  polymers can be modeled as having a behavior where
                                                   g
                 the spring portion is more important. Above their T  where segmental mobility occurs, the dashpot
                                                           g
                 portion is more important.
                    The relative importance of these two modeling parts, the spring and the dashpot, is also depen-
                 dent on the rate at which an experiment is carried out. Rapid interaction, such as striking with a

                 hammer, with a polymer is more apt to result in a behavior where bond flexibility is more important,
                 while slow interactions are more apt to allow for segmental mobility to occur.
                    Since polymers are viscoelastic solids, combinations of these models are used to demonstrate the defor-
                 mation resulting from the application of stress to an isotropic solid polymer. Maxwell joined the two
                 models in series to explain the mechanical properties of pitch and tar (Figure 14.2a). He assumed that the
                             (a)                             (b)





                              Stress                           Stress








                                        Strain                           Strain

                 FIGURE 14.1  Stress–strain plots for a Hookean spring (a) where  E is the slope (Equation 14.1), and a
                 Newtonian dashpot (b) where s is a constant (Equation 14.3).







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