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Standard mold unit

The present edition is not only updated, but modernized and renewed. This is also indicated by the fact that only six of the old authors are still involved, and there are new chapters such as micro injection molds, molds for the rubber industry, or rapid prototyping, while others are no longer applicable. Otherwise, as it was already stated in the preface of the 4th German edition, it still applies that this compilation does not intend to serve as a textbook for the detailed design of an injection mold or to replace the catalogue of a manufacturer of standard mold units, and it is also not the long version of a lecture manuscript either. Rather, the brief description of the basic facts and the latest state of the art for the individual mold types and their manufacture allow a direct comparison in a compact form. [Pg.8]

Figure 1.81 shows a standard mold unit, which is another type of compression mold. Both mold halves are permanently clamped in the press. The cavities for the base mold are carried out in the form of inserts. [Pg.86]

The guide systems for the plates and maybe for the mold inserts should be determined. Standard guide elements from manufacturers of standard mold units are preferred for reasons of costs. In addition to avoiding a static over-determination in the centering system of the plates and cavities, it is important to ensure a smooth operation at temperatures around 200 °C. If a guide cone is used in cavity-self-centering, special attention should be paid to manufacturability (only as accurate as necessary). [Pg.282]

For demolding undercuts and internal threads, collapsible cores (Figure 2.38) are used. Two technical solutions are available as a standard mold unit ... [Pg.368]

Figure 1 Surface profile of standard molding with low profile additives (units pinch/inch). Figure 1 Surface profile of standard molding with low profile additives (units pinch/inch).
The direct manufacture of prototype molds using the rapid prototyping process offers significant advantages (see also Section 4.7). By LaserCUSING and adapted processes, molds without restriction for prototype and small-series production can be used. Also, highly filled thermoplastics of up to 70% GF can still be manufactured to several thousand injection molded parts on standard injection molding units. [Pg.318]

Hydrocyclones are available in numerous sizes and types ranging from pencil-sized 10-mm diameters of plastic to the 1.2-m (48-in) diameter of rubber-protected mild or stainless steel. Porcelain units 25 to 100 mm (1 to 4 in) in diameter are becoming popular, and in the 150-mm (6-in) size the starch industry has standardized on special molded nylon types. Small units for fine-size separations are usually manifolded in multiple units in parallel with up to 480 ten-mm... [Pg.1776]

Compression molded (150°C for 3 minutes press chilled with cold water immediately thereafter) samples of poly(trans-l,4-hexadiene) (14) and poly(5-methyl-l,4-hexadiene) were examined with a General Electric (XRD-3) X-ray unit. Transmission Laue X-ray photographs were taken using nickel filtered copper X-radiation. Samples were stretched to four times of their original lengths to obtain oriented fibers. The fiber patterns were obtained in a flat plate film holder with the specimen to film distance standardized at 5 centimeters. X-ray diffraction patterns were similarly obtained for the hydrogenated sample of poly(5-methyl-l,4-hexadiene). [Pg.174]

The Fresnel lens concentrator, shown in Figure 1.36 top right, uses refraction rather than reflection to collect the solar energy. These units are molded out of inexpensive plastic and provide higher efficiency than the standard PV collectors. Point-focusing Fresnel lenses are also available. In Figure 1.36 bottom left, parabolic dish collectors are shown. Both the Fresnel lenses and these collectors can be rotated around two axes to continuously track the Sun. [Pg.91]

Two-component injection machines, using separate injection units for each of the two components perform the standard sandwich molding process. This process is characterized by a sequential injection of the two components using the same gating system. After filling the mold partially with the skin material with one injection unit the core component will be injected by the second injection unit. In order to avoid flow marks on the part surface a simultaneous phase is inserted between the injection of skin and core components. The final packing phase may be performed either with the core or the skin component. [Pg.220]

In 1992, a new sandwich injection molding concept, called monosandwich, was developed by Jaroschek and Thoma (Ferromatic Milacron). In contrast to the standard sandwich molding process, this technology uses only one injection unit for both skin and core components with an extruder. [Pg.220]

The cycle starts with the plastification of the core component in the injection unit. Then the extruder moves to the bottom position, the injection unit moves forward to the extruder nozzle to link the nozzles of the extruder and the injection unit. The extruder starts plastification of the skin component and extrudes the melted skin component into the screw antechamber of the injection unit. Thus the skin and core components are located one after the other in the screw antechamber. After the extruder moved back to the top position, the injection unit moves forward to the mold followed by a conventional filling phase. Due to the fountain flow effect the first injected material forms the skin layer followed by the second component forming the core. Compared to the standard sandwich process the injection phase of the monosandwich process is less complicated as it is identical to the conventional injection molding process. [Pg.220]

AG (now Datacolor International) software. Finally, the Colour Measurement Committee (CMC) of the Society of Dyers and Colourists in the United Kingdom made some compromises and published a formula based on the J P Coates work but incorporating the CIELAB coordinates [53], This was made a British standard (BS 6923) and soon was adopted by textile associations around the world. The usefulness of such an equation has been demonstrated many times in the textile industry and in some papers from manufacturers of textured, molded polypropylene as well. [Pg.37]

Table 8.9. Classification of materials on the basis ofIp2 corrected by the functional unit found by an LCA and standardized with a criterion of transparency and compatibility with the process of blow molding... Table 8.9. Classification of materials on the basis ofIp2 corrected by the functional unit found by an LCA and standardized with a criterion of transparency and compatibility with the process of blow molding...

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See also in sourсe #XX -- [ Pg.343 ]




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