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characteristic  property  to  the  final  film,  such  as
                               stiffness,  heat-sealability,  impermeability  or
                        1
                               resistance  to  some  environment,  all  of  which
                               properties  would  be  impossible  to  attain  with  any
                        2      single material. This technology is used on any of the
            3
                               processes as blown film, overjacketing, tubing and
                               sheets extrusions.

                               CAST  FILM  EXTRUSION:  The  cast  film  process
                               differs from the blown film process through the fast
      quench and virtual unidirectional orientation capabilities. These characteristics allow
      a cast film line to operate at higher production rates while producing amazing optics.
      Polymer melt is extruded through a flat die. Immediately after exiting the die, the
      molten curtain is passed onto rotating water cooled chill roll or into water quench tank
      to “freeze” the film. The speed of the roller controls the draw ratio and final film
      thickness which then is passed downstream where the edges are trimmed, corona
      treatment is applied (if a fabrication process such as printing or coating is required)
      and the film is wound into rolls. Cast film is usually made in a thickness range of 20 to
      200 microns, and is used in applications with good optical properties such as gloss,
      transparency,  surface  smoothness,  good  tear  resistance  with  toughness  and
      flexibility.
      DRY SPINNING: is used to form polymeric fibers from solution. The polymer is
      dissolved in a volatile solvent and the solution is pumped through a spinneret (die)
      with numerous holes (one to thousands). As the fibers exit the spinneret, air is used
      to evaporate the solvent so that the fibers solidify and can be collected on a take-up
      wheel. Stretching of the fibers provides for orientation of the polymer chains along
      the fiber axis. Cellulose acetate (acetone solvent) is an example of a polymer which
      is  dry  spun  commercially  in  large  volumes.  Due  to  safety  and  environmental
      concerns associated with solvent handling this technique is used only for polymers
      which cannot be Melt spun. (Fig.A)

                                                              rotating
                                                              mandrel
                                                                   head

                                                                     resin
                                                                     bath

                                                                     guides
           A                     B                    C     fiber tows

      MELT SPINNING: is the preferred method of manufacture for polymeric fibers. The
      polymer is melted and pumped through a spinneret (die) with numerous holes (one
      to thousands). The molten fibers are cooled, solidified, and collected on a take-up
      wheel.  Stretching  of  the  fibers  in  both  the  molten  and  solid  states  provides  for
      orientation of the polymer chains along the fiber axis. Polymers such as PET and
      nylon 6,6 are melt spun in high volumes. (Fig.B)

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