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               636                                                                                  Polymer Processing


                 The production of manmade fibers usually includes the
               following processes:

               1.  Preparation of polymer (polymerization, chemical
                  modification, etc.)
               2.  Preparation of the spinning fluid (polymer melt or
                  solution)
               3.  Spinning (extrusion, solidification, and deformation
                  of the spinning line or filament)
               4.  Drawing (due to a higher linear speed at the take-up
                  roll relative to that at the die; drawing is used to
                  increase the degree of molecular orientation and
                  improve the tensile strength, modulus of elasticity
                  and elongation of the fibers)
               5.  Heat treatment
               6.  Textile processing (twisting, oiling, dyeing, etc.).

                 The spinning process can be achieved mainly by three
               procedures: melt spinning, solution dry-spinning, and so-
               lution wet-spinning. Of these three procedures, melt spin-
                                                                 FIGURE 30  Schematic of the melt-spinning process for a single
               ning  is  the  simplest  and  the  most  economical  one.  Its  filament. [From Baird, D. G., and Collias, D. I. (1998). “Polymer
               simplicity stems from the fact that it involves only heat  Processing: Principles and Design,” Wiley, New York.]
               transfer and extensional deformation, whereas the other
               methods in addition to the above processes involve also
               mass transfer and diffusion. The melt spinning procedure  Some spinnerets can have as many as 10,000 holes (rayon
               can be applied to polymers that are thermally stable at the  spinning from a 15-cm platinum disk spinneret). Extru-
               extrusion temperature and that exhibit relatively high flu-  sion through the spinneret (or die), subsequent die swell
               idity at that temperature. Typical examples of melt-spun  (due to the relaxation of the elastic stresses of the poly-
               polymers are polyamides, polyesters, polystyrene, poly-  mer), cooling of the filament by cooling air (or water
               olefins, and inorganic glasses.                    vapor) flowing perpendicularly to the filament axis, so-
                 In the solution dry-spinning procedure the polymer is  lidification of the polymer, and its cold drawing in the
               dissolved in a volatile solvent and the solution is extruded.  region from the solidification point to the take-up roll are
               Then the spinning line meets a stream of hot air and the sol-  shown in this figure. Part of the time the holes in the
               vent is evaporated. The recovery of the solvent increases  spinneret are circular in shape, but mostly they are ir-
               the cost of the whole process. Typical examples of dry-  regular in shape. Typical shapes include trilobal, square,
               spun polymers are cellulose acetate, acrylonitrile, vinyl  and cross. Note that dry- and wet-spinning from circu-
               chloride,  and  acetate.  Lately,  extended-chain  PE  fibers  lar spinneret holes usually results in irregularly shaped
               (ECPE,  Spectra  fibers)  are  made  by  solution  spinning  fibers.
               in a typical melt-spinning apparatus. The solution wet-  In terms of the number of the filaments per spin-
               spinning procedure is applied to polymers that meet nei-  neret plate, as well as the spinning speed, melt spinning
               ther criteria of  the  previous  two  methods  (i.e.,  thermal  is divided into various groups. Monofilaments are pro-
               stability and solubility in a volatile solvent). It involves  duced by one-hole spinneret plates, while most of the
               the extrusion of a polymer solution into a liquid bath of  time numerous filaments are extruded through the spin-
               coagulating agents, which drive the solvent out of the fil-  neret(multifilamentyarns).Verylow-speedspinning,with
               ament. Four other spinning procedures (phase separation  speeds ranging from 30 to 100 m/min, usually occurs
               spinning, emulsion spinning, gel spinning, and reaction  for thick monofilaments spun through liquid baths. Low-
               spinning) are not addressed here.                 speed spinning is usually carried out at speeds in the range
                 A schematic (not in scale) of the typical melt-spinning  of100to750m/min,wherethe filamenttensionisconstant
               procedure  is  shown  in  Fig.  30.  Polymer  is  pumped  by  along the entire length. To enhance the degree of orienta-
               means of an extruder through a screen pack, in which the  tion and crystallinity and, hence, physical properties, the
               polymer is filtered through layers of screens and sand.  yarns are subsequently drawn and annealed and, there-
               Then  it  is  divided  into  many  small  streams  by  means  fore, the melt-spinning process is considered to be a two-
               of  a  plate  containing  many  small  holes,  the  spinneret.  step process (first step: spinning; second step: drawing;
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