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Melt channels

Figure 11.3 Cross-section through a melt channel in the melting zone of an extruder... Figure 11.3 Cross-section through a melt channel in the melting zone of an extruder...
Figure 11.6 illustrates the general configuration of a film blowing operation. Molten polymer from the extruder is pumped into an annular die, where it is distributed around a tubular melt channel before emerging vertically as a relatively thick-walled molten tube. The top of... [Pg.220]

Ironmaking processes, 14 498-521 blast furnace, 14 498-509 direct reduction, 14 509-520 direct smelting, 14 520-521 Iron-manganese-silicon steels, 22 712 Iron melting channel melting furnaces, 12 316... [Pg.492]

Figure 6.1 Schematic for a barrier melting section (courtesy of Jeff A. Myers of Robert Barr, Inc.). The barrier flight is undercut from the main flight to allow molten resin to transfer from the solids channel to the melt channel... Figure 6.1 Schematic for a barrier melting section (courtesy of Jeff A. Myers of Robert Barr, Inc.). The barrier flight is undercut from the main flight to allow molten resin to transfer from the solids channel to the melt channel...
Figure 6.23 Schematic for the position of the barrier flight via the width of the solids channel [W,) and the depths of the solids and melt channels a) a barrier section design with a continuously decreasing /V b) constant-width solids channel, and c) a hybrid design. The designs all utilize a constant lead length for the primary flight... Figure 6.23 Schematic for the position of the barrier flight via the width of the solids channel [W,) and the depths of the solids and melt channels a) a barrier section design with a continuously decreasing /V b) constant-width solids channel, and c) a hybrid design. The designs all utilize a constant lead length for the primary flight...
Figure 6.26 Comparison of melting dynamics for a conventional melting channel and a transverse barrier melting channel for an LDPE resin at identical rates and screw speeds. The conventional channel is in red while the barrier melting section is in black... Figure 6.26 Comparison of melting dynamics for a conventional melting channel and a transverse barrier melting channel for an LDPE resin at identical rates and screw speeds. The conventional channel is in red while the barrier melting section is in black...
The restriction was mitigated by modifying the screw as outlined in the case study in Section 11.10.1. That is, the depth of the melt channel of the barrier section was increased to that of the solids channel at the entrance, and it was tapered into the depth of the melt channel over 2 diameters. The barrier flight was removed for the first 2 diameters and blended in with the melt channel, the shallower of the two channels in this region. The barrier flight for the next diameter was blended into the original undercut. With this modification the restriction still existed but it was spread over a three-diameter length of the screw instead of over half of a diameter. [Pg.512]

Figure8.20 The screw zone comprises a conveying element-spacer disc-mixing element-spacer disc and kneading element at a pressure difference of 0 bar and melt flow of 0.11 kg/s. The top figure shows the pressure on the screw surface, while the bottom figure shows the axial velocity in the melt channel at half the channel height... Figure8.20 The screw zone comprises a conveying element-spacer disc-mixing element-spacer disc and kneading element at a pressure difference of 0 bar and melt flow of 0.11 kg/s. The top figure shows the pressure on the screw surface, while the bottom figure shows the axial velocity in the melt channel at half the channel height...
The usual die used is a crosshead with a 90° angle between the wire line and the extruder body axis (Chapter 17). With this setup, the entire length of the extruder projects sideways from the coating lines. To help melt flow from developing dead spots in the melt channels, 30° or 45° crossheads can be used. They provide a more streamlined interior and the extruder location is better adapted to some plant layouts. They are sometimes preferred when processing PVC because of the streamlining and better control of the melts heat profile. Most dies are subjected to very high internal pressures since the uncommon pressure in the extruder barrel of over 5,000 psi (35 MPa) is required. [Pg.262]

Each melt basically has its own plus and minus capabilities for operating in the die melt channels following its non-Newtonian behaviors (Chapter 1). The extruders (and other equipment) have their limitations, such as heat transfers through metal parts and metal parts that are subjected to wear. Therefore, what tends to exist is an empirical science that continues to work efficiently. The limitations have always existed. But with time as material and equipment developments occur, designing dies, as well as operating equipment, continues to improve by increasing product performances and output rates.449-455... [Pg.534]

Fig. 8 Coextmsion feed block manifold and sheet die (A) (1) sheet die with flow restriction (2) adapter plate (3) feed block asembly (4) core material layer inlet (5) upper material layer inlet (6) lower material layer inlet and coextrusion multimanifold sheet die (B) (1) lower melt channel (2) upper melt channel (3) lower choker bar (4) lower choker bar adjustment bolt (5) upper choker bar (6) upper choker bar adjustment bolt (7) flex lip. Fig. 8 Coextmsion feed block manifold and sheet die (A) (1) sheet die with flow restriction (2) adapter plate (3) feed block asembly (4) core material layer inlet (5) upper material layer inlet (6) lower material layer inlet and coextrusion multimanifold sheet die (B) (1) lower melt channel (2) upper melt channel (3) lower choker bar (4) lower choker bar adjustment bolt (5) upper choker bar (6) upper choker bar adjustment bolt (7) flex lip.
Each melt channel has its own choker bar for flow control. [Pg.642]


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See also in sourсe #XX -- [ Pg.367 ]




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