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Single-screw extruders mixing

Mixing in single screw extruders. Mixing caused by the cross-channel flow component can be further enhanced by introducing pins in the flow channel. These pins can either sit on the screw as shown in Fig. 3.29 [9] or on the barrel as shown in Fig. 3.30 [15]. [Pg.133]

B. 10 Scaleup of a Single-Screw Extruder Mixing Method. As discussed in Sections 6.4 and 8.5.1, mixing is taken to be a function of strain, which in the metering section of a single-screw extruder is L/H. (This follows from y = yt = (%DbN/H)(L/%DbN).)... [Pg.270]

FIG. 18-48 Mixing enhancers for single-screw extruders a) Maddock (straight), (h) Maddock (tapered), (c) pineapple, (d) gear, (e) pin,... [Pg.1649]

In preliminary tests, melt mixed blends of PP and LCP were processed at six different temperatures (Tcyi 230, 240, 250, 260, 270, and 280°C) with a Brabender Plasti-Corder PLE 651 laboratory single-screw extruder. The measured melt temperatures were about 10°C higher than the cylinder temperatures (Tcyi). The objective was to study the influence of temperature on the size and shape of the dispersed LCP phase. Two different polypropylenes were used to ascertain the effect of the viscosity of the matrix on the final morphology. Different draw ratios were obtained by varying the speed of the take-up machine. [Pg.625]

Figure 2 Optical micrographs of melt mixed PP-LCP blends single-screw extruded at melt temperatures of (a) 250°C, and (b) 260°C. Figure 2 Optical micrographs of melt mixed PP-LCP blends single-screw extruded at melt temperatures of (a) 250°C, and (b) 260°C.
Illustration Optimum strain per period in shear flows with periodic reorientation. Many practical mixing flows (e.g., single screw extruder with mixing... [Pg.120]

Erwin, L Theory of mixing sections in single screw extruders. Polym. Eng. Sci. 18, 7, 572-576 (1978). [Pg.200]

What is the primary mechanism by which a mixing element in a single screw extruder creates mixing ... [Pg.241]

The fundamental processes and mechanisms that control single-screw extrusion are presented in Chapters 5 through 8. These processes include solids conveying, melting, polymer fluid flow, and mixing. The analyses presented in these chapters focus on easily utilized functions needed to assess the operation of the single-screw extruder. The derivation of these relationships will be presented in detail in the appendices for those who desire to explore the theory of extrusion in more detail. [Pg.5]

Spalding, M.A. and Flyun, K. S., Troubleshooting Mixing Probiems in Single-Screw Extruders, SPEANTEC Tech. Papers, 49, 229 (2003)... [Pg.246]

Common Mixing Operations for Single-Screw Extruders... [Pg.330]

Figure 8.6 Average stretching (5,) for operational modes of a conventional extrusion and the chaotic mixing. The j/-axis is logarithmic. The top wall moving curve corresponds to a conventional single-screw extruder with a rotating screw. The results are shown for an /r/FF aspect ratio of one and a period of 4 s... Figure 8.6 Average stretching (5,) for operational modes of a conventional extrusion and the chaotic mixing. The j/-axis is logarithmic. The top wall moving curve corresponds to a conventional single-screw extruder with a rotating screw. The results are shown for an /r/FF aspect ratio of one and a period of 4 s...
Erwin, L. and Mokhtarian, F., Analysis of Mixing in Modified Single-Screw Extruders, Polym. Eng. Set, 23, 49 (1983)... [Pg.383]


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