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The Single Screw Extruder

The following table compares the single screw extruder with the main types of twin screw extruders. [Pg.264]

Figure 4 Optical micrographs from the skin region of the single-screw extruded strands processed at cylinder temperatures of (a) ISO C, (b) 200°C, (c) 230°C, (d) 250°C, and (e) 280°C. Figure 4 Optical micrographs from the skin region of the single-screw extruded strands processed at cylinder temperatures of (a) ISO C, (b) 200°C, (c) 230°C, (d) 250°C, and (e) 280°C.
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]

Here, is the lateral stress ratio, and oy are the stresses in the x and y directions, and ff, in the case of the single-screw extruder, is assumed to be the local downstream pressure P. Lateral stress ratios were discussed in Section 4.2. [Pg.140]

All of the data in Fig 7.5 were analyzed using linear regression. The summation of the helix and core-regressed flow rates are plotted in Fig. 7.5 as the red dotted line. The experimental superposition for the flows induced by the screw elements essentially overlaid the regression line for the screw configuration rate. Thus, it was concluded that the helix is the pump in the single-screw extruder, and core rotation reduces the flow by dragging the fluid back toward the extruder inlet. [Pg.251]

The single screw extruder was fitted with a standard equipment (see Table XII) the operating conditions and the results obtained are presented in Table XIII. [Pg.286]

Single screw extruder. Let us take the case of a single screw extruder section that works well when dispersing a liquid additive within a polymer matrix. The single screw extruder was already discussed in the previous section. However, the effect of surface tension, which is important in dispersive mixing, was not included in that analysis. Hence, if we also add surface tension as a relevant physical quantity, it would add one more column on the dimensional matrix. To find the additional dimensionless group associated with surface tension, as, and size of the dispersed phase, R, two new columns to the matrix in eqn. (4.32) must be added resulting in ... [Pg.195]

Besides the single-screw extruder, also twin-screw extruders are being used. Two... [Pg.217]

The best place to start is with a brief account of the origin of all multiple screws, namely the single screw extruder. Its inventor, Archimedes [1] (approximately 2250 years ago), used it to transport water overcoming differences in elevation. The same principle is still used today in Egypt, Holland, and in many water purification plants. [Pg.9]

TPs are characterized by low thermal conductivity, high specific heat, and high melt viscosity. Preparation of a uniform homogeneous melt and its delivery at adequate pressure and a constant rate could pose considerable problems if not properly processed (Chapter 3). The principal extruder variants are the single-screw and the twin-screw types. Of these, the single-screw extruder is by far the most versatile and popular in use. [Pg.230]

In the past twin and other multi-screw extruders were developed to correct the problems that existed with the single-screw extruder. Later the single-screw designs with material developments practically eliminated all their original problems. [Pg.236]

The conveyance and flow processes of multi-screw extruders are very different from those in the single-screw extruder. The main characteristic of multi-screw extruders include ... [Pg.236]

The single-screw extruders are being used for the preparation of blends that either do not require... [Pg.640]

Extruders can have different designs and modes of operation, e.g., single or multi-screw, continuous or discontinuous. The basic operation of the most widely used extruder for forming thermoplastics into finished products, the single screw extruder, will be reviewed in the next section. This provides the concepts that can be extended to other, more complex machines, viz. the multiscrew and specialty extruders discussed briefly in... [Pg.686]


See other pages where The Single Screw Extruder is mentioned: [Pg.57]    [Pg.326]    [Pg.7]    [Pg.247]    [Pg.254]    [Pg.325]    [Pg.379]    [Pg.383]    [Pg.604]    [Pg.604]    [Pg.606]    [Pg.785]    [Pg.95]    [Pg.113]    [Pg.247]    [Pg.2]    [Pg.235]    [Pg.242]    [Pg.247]    [Pg.247]    [Pg.249]    [Pg.251]    [Pg.253]    [Pg.255]    [Pg.257]    [Pg.447]    [Pg.607]    [Pg.978]    [Pg.396]    [Pg.230]    [Pg.237]    [Pg.200]    [Pg.605]    [Pg.687]    [Pg.689]    [Pg.697]   


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