Page 615 - Carrahers_Polymer_Chemistry,_Eighth_Edition
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578                                                    Carraher’s Polymer Chemistry


                                                        Polymer solidifies as
                            (a)   Melt spinning
                                                             it cools
                                Melted polymer



                                                     Spinneret
                                                                     Hot gas to remove solvent
                            (b)   Solvent spinning
                                Dissolved polymer


                            (c)   Wet spinning
                                                               Hot gas
                                          Dissolved polymer
                                                    Spinneret
                                                             Nonsolvent bath






                 FIGURE 18.3  Fiber production using the three major spinning techniques.



                 TABLE 18.4
                 (Preferred) Spinning Processes
                                                          Wet Spinning
                 Melt Spinning        Dry Spinning        Coagulation         Regeneration
                 Nylon                Acetate             Acrylic             Viscose
                 Polyester            Triacetate          Aramid              Cupro
                 Polyethylene         Acrylic             Elastane/Spandex
                 Polypropylene        Elastine/Spandex    Poly(vinyl chloride)
                 Poly(vinylene chloride)   Poly(vinyl chloride)
                                      Aramid
                                      Modacrylic
                                      Vinyal




                    For continuous filament formation, the number of holes is on the order of 10–100. The exit hole
                 is usually circular giving round fibers. Other shaped holes are also employed that produce fi bers

                 with varying shapes.
                    The extruded fiber is then often uniaxially stretched by take-up rollers rotating at different

                 speeds. The fiber stretching encourages the polymer chains to align on a molecular level producing

                 increased strength in the direction of the pull.
                    To produce the melted polymer, the polymer chips, rods, marbles, or sheets are heated forming
                 a melted pool of material. To minimize oxidation, the melted polymer is blanketed by an inert gas
                 such as nitrogen or argon. The fl uidicity (inverse of viscosity) of the melt increases with increased
                 temperature as does the cost to provide the necessary energy and tendency for unwanted reactions
                 to occur. Thus, the polymer melt is generally assisted to and through the spinneret by means of an
                 extruder that may also be used to supply some or all of the heating.







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