Page 29 - Plastics News June 2021
P. 29

FeAtures




                                                                required to reduce the change in direction of the fibers
                                                                as they pass over the moving barrier flight in relation to
                                                                the barrel. In general, the screw should be designed so
                                                                that such high-shear mixers are not required to complete
                                                                melting, which may mean a sacrifice in output rate.

                                                                Screw designs that do well processing amorphous polymers
                                                                with  glass  fiber  are  often  ineffective  with  crystalline
                                                                polymers.

                                                                A better choice of mixer types is the kind that divides the
                                                                melt, minimizing fiber breakage and offering improved
          or barrier flights, but also subjects the polymer to more   wetting-out of the fibers. These mixers are sometimes
          repetitive shearing. For those running glass- or other   referred to as Saxton mixers, and consist of multiple flights
          fiber-filled compounds on a daily basis, determination of   with interrupting cuts (Fig. 2). This design eliminates much
          the best L/D can be critical. Selecting the ideal L/D can   of the high compressive forces present in shear mixers.
          be done by stopping the screw, pushing it out filled, and
          having the glass length at various L/Ds measured after   A mixer type that I have had success with for low-shear
          burning off the polymer.                              mixing  and  good  fiber  wetting  is  the  simple  grooved-
                                                                root design (Fig. 3). It can be designed to provide any
          Crystalline polymers require even more care in order to   level of shear and mixing, thereby avoiding the severe
          prevent fiber breakage than amorphous polymers, because   reorientations that can break fibers. Additionally, designs
          they do not soften until reaching their melting point. This   like this apply multiple low-shear cross-directional forces
          makes channel plugging more difficult to eliminate. That   that can help to unbundle fibers as well as reduce the
          should be considered along with the compression rate   formation of agglomerates.
          and feed length. Screw designs that do well processing
          amorphous polymers with glass fiber are often ineffective   FIG 3 A simple grooved-root mixer design offers low-shear
          with crystalline polymers.                            mixing  and  good  fiber  wetting.  It  can  be  designed  to
                                                                provide any level of shear and mixing, thereby avoiding
          Mixer Choice is Crucial
                                                                the severe reorientations that can break fibers.
          Mixers require special consideration as well. High-shear
          mixers like the traditional Maddock design can be used,   Regardless of the single-screw design, there is always some
          but they need to be placed well down the screw where   reduction in fiber length during the transition from solid
          there is an expectation of complete or nearly complete   to melt in the screw. However, with care in the design and
          melting, which reduces their basic purpose of melting.   operating conditions, suitable product physical property
          Even then, a greater clearance over the barrier flight is   improvements can be obtained.

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