Page 27 - Plastics News May 2021
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FeAtures



          Getting The Profile Die Design Just Right

                                                                                                   Jim Frankland

          That ‘Sliding’ effect has a considerable influence on the die design and it’s important to understand this when
          troubleshooting die performance


             alculating polymer flow is fairly straightforward when
         Cdesigning a die for a simple round profile, but as the
         shapes get more complicated these calculations can get
         extremely challenging. Here’s what you need to consider.
         Die forming typically occurs immediately after polymer
         melt  has  exited  an  extruder. The  most  basic  process
         involves guiding the stream of molten polymer under
         pressure through a die, which three distinct regions:
         manifold, approach, and lip. The 'manifold' serves to
         channel the polymer melt from its initial extrusion point
         to a near-net-shape of the final product. The 'approach'
         region further guides the melt into the final shape, and
         begins to correct for any non-uniform flow. Finally, the   additional surface area in the corners causes a reduction
         'lip' forms the melt into the final desired cross section and   in flow. This tends to round the corners. The shear stress
         compensates  for  any  remaining  flow  asymmetry. After   in the polymer shape is always zero in its exact center
         exiting the lip of the die, the polymer melt will undergo   of flow, which may or may not be the center of the part
         die swell before curing. Die swell is an expansion of the   (except in the simplest shapes). The maximum shear
         melt as the pressure is released, and is dependent on   stress occurs at the die wall, and shear stress increases
         polymer chemistry and die design. After curing, the solid,   proportionally with the distance from the center point of
         continuous part is drawn onto a take-up roller or cut into   flow. That variation in shear stress alone develops a slight
         transportable lengths, depending on the type of part. A   difference in viscosity due to the changing shear. The
         lot of experienced extrusion operators—especially those   more complex the profile,  the more complex the effects.
         with limited background in polymer rheology—tend to    Thus, as the die becomes more complicated, the variations
         think the material “slides” through the die to form its final   in flow become more complex and the die internals often
         shape. In fact, the polymer should adhere firmly to the die   do not look that much like the final part. Note the rounded
         walls, as slips result in melt fracture. That effect has a   corners in the relatively simple square profile in Fig. 1. For
         considerable influence on the die design and it’s important   that profile, the die had to be designed with additional
         to understand this when troubleshooting die performance.   space for polymer to flow into all the corners as the part
         Once the polymer exits the extruder and enters the die it   moves through the die.
         sticks quite firmly to the die walls and is sheared in the   Each surface of the die also needs to be uniformly heated
         die openings as pressure from the screw or melt pump   so that the viscosity along the walls provides for the same
         forces it through the die. Calculating polymer flow is not   pressure drop to match the other legs, so that the profile
         all that difficult when designing a die for a simple round   stays “square” exiting the die. Any unbalanced heating
         profile, but as the shapes get more complicated these   of the die can distort the shape by varying the viscosity
         calculations can get extremely challenging. Just moving   near the die wall. This occurs even in simple dies such
         to a simple rectangle makes things more complex.
                                                                as one in Fig. 1, but it becomes much more pronounced
         A circular profile tends to just get a little smaller than   in more complex profile dies where the shape is more
         the die cross-section (neglecting polymer swell) because   irregular (see Fig. 2).
         of the polymer adhering to the wall—but the shape does   The sections labeled 1 to 4 show how the shape of the
         not change. On the other hand, with a simple rectangular   die channel would change from extruder exit on the left
         profile the square corners will not fill out because the




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