Page 57 - Plastics News Issue September2025
P. 57

TECHNOLOGY NEWS








          Building a Screw-Cooling System





                                                                a gundrilled hole into the shank that extends to
                                                                the end of the feed channel. The inflowing wa-
                                                                ter enters a pipe at the rotary union. The pipe
                                                                extends to about 1 inch from the end of the gun-
                                                                drilled cooling hole. The water then flows back
                                                                toward the shank through the annular passage
                                                                between the pipe and the gundrilled hole. The
                                                                water then flows back out of the screw, through
                                                                the outer pipe. This outer pipe is attached by a
                                                                pipe thread to the screw shank and the rotary
                crews have been cored for cooling since
                the early 1960s. In many processes, how-        union. Water flows out through the rotary union.
          Sever, screw cooling is not utilized. Here’s
          an optimal design for a screw-cooling system.

          Poor solids conveying in smooth-bore, single-
          screw extruders can limit rates, cause flow surg-
          ing, and reduce the profitability of a line. Exam-
          ples of poor solids conveying were presented
          for a polystyrene (PS) resin and in the August
          2025 issue for a polycarbonate (PC) resin. In
          both cases, the screws became too hot in the          The typical bore sizes of cooling holes and the
          feed section, limiting the forwarding forces for      tap sizes for screws of different diameters are
          solids conveying. These processes were made           shown in Table 1. Screws with diameters less
          stable, and rates were increased with the use of      than 2 inches are very seldom bored for cool-
          screw cooling.                                        ing because it greatly weakens the screw’s tor-
                                                                sional strength unless its base material is made

          Screw cooling is one of the most misunderstood        of 17-4 PH stainless steel or other high modulus
          operations in the extrusion process. Screws have      steel. Screw cooling becomes very important for
          been cored for cooling since the early 1960s. In      screws that are 8 inches in diameter and greater.
          many processes, however, screw cooling is not
          utilized. This article describes the optimal design   When screw cooling is used to improve solids
          for screw-cooling systems.                            conveying, the screw is bored to a depth equal
                                                                to about the end of the feed section. In most
          Cooling the feed section of a screw is performed      cases, the depth will be the length of the drive
          by pumping water through a duo-flow rotary un-        shank plus five to six diameters of the screw. For
          ion into a passageway on the shank end of the         example,  on  a  4.5-inch  diameter  screw  with  a
          screw, as shown by Figure 1. The passageway is        drive shank length of 16 inches and six diameters

           September 2025                                                                    PLASTICS NEWS  57
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