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Single screw extruders geometry

Klein, 1., The Melting Factor in Extruder Performance, SPEL, 28, 47 (1972) Altinkaynak, A., Three-Dimensional Finite Element Simulation of Polymer Melting and Flow in a Single-Screw Extruder Optimization of Screw Channel Geometry, Ph. D. Thesis, Michigan Technological University, Houghton, MI (2010)... [Pg.244]

Altinkaynak, A., Gupta, M., Spalding, M.A., and Crabtree, S. L., The Investigation of the Effect of the Screw Geometry on Melting in a Single-Screw Extruder, SPE ANTEC Tech. Papers, 56, 426 (2010)... [Pg.244]

Solid bed profile prediction for a plasticating single screw extruder. In this example we would like to use Tadmor s model to predict the solid bed profile of a low density polyethylene in a plasticating single screw extruder, based on experiments published by Tadmor and Klein [27], In their experiments they used the following screw geometry ... [Pg.327]

The purpose of this analysis is to design an industrial size version of the pilot process, which achieves the same dispersive mixing without overheating the polymer melt. In order to simplify the solution we lay the helical geometry flat, a common way of analyzing single screw extruders. [Pg.642]

Table 10.18 - Typical geometries of a single screw extruder (lengths expressed as L/D ratio)... Table 10.18 - Typical geometries of a single screw extruder (lengths expressed as L/D ratio)...
Any modification to the screw geometry always leads thereby to modification of the two parameters. Depending on the mass, product and the necessary pressure level, single-screw extruders work in the ceramics industry with screws which show an L/D ratio (screw length/screw diameter in the closed cylinder) of 2-20. Similarly extreme differences can be estab-... [Pg.199]

FIGURE 1 Schematic diagram of (a) the single-screw extruder for pulverization of rubbers and (b) geometry of the screw channel with variable depth. (From Bilgili et al. [57].)... [Pg.670]

In the solids-conveying and melting sections in single-screw extruders, the solid particulate assembly is normally treated as a solids plug . This assumption can be nsed to predict the pressurisation of polymer solids in the solids-conveying section of single-screw extruders with different screw geometries and material properties. [Pg.47]

Because of the more complex machine geometry, the cost per unit throughput of the diskpack is higher than for the conventional single screw extruder. Therefore, the diskpack does not compete directly with single screw extruders. [Pg.36]

In the extrusion of medical devices, molecular degradation is often a critical issue. This degradation of the MW can be strongly influenced by the geometry of the extruder screw. Unfortunately, little information on this problem is available in the open literature. Paakinaho et al. [127] published results of a study on the MW reduction along the length of a single screw extruder for three polylactic acid (PLA) resins see Fig. 8.111. [Pg.630]


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