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Continuous extrusion process

This is produced by a continuous extrusion process, which gives the product a smooth-surface skin and enhances the mechanical properties. [Pg.122]

The success of any continuous extrusion process depends not only upon uniform quality and conditioning of the raw materials but also upon the speed and continuity of the feed of additives or regrind along with virgin plastic upstream of the extruders hopper. Variations in the bulk density of materials can exist in the hopper, requiring controllers such as weight feeders, etc. [Pg.476]

Injection molding is a common process that we use to convert polymer granules to solid objects. Unlike the products made by continuous extrusion processes, discussed in Chapter 11, products made by injection molding are discrete objects, produced in individual mold cavities. We encounter injection molded products of all sorts in our daily lives, ranging from combs, bottle caps, and ballpoint pens to car steering wheels, camera bodies, and the keys on our computers. [Pg.243]

Profiles, was recently opened to make plastic lumber profiles using a proprietary, continuous-extrusion process developed in-house. [Pg.45]

A continuous extrusion process that introduces molecular orientation to an unplasticised PVC pipe is described. Pipe design is discussed and it is shown how the relevant property improvements are utilised. Materials costs are reduced while short and long term performance is enhanced offering an outstanding opportunity for PVC pressure piping. [Pg.118]

Two notable methods to produce microcellular foams include gas supersaturation in combination with an extrusion process developed by MIT/Trexel [84-86] and the continuous extrusion process by Dow [87,88]. Super-insulating materials are made by the encapsulation of a filler material inside a barrier film, aluminum foil, or metallized film. These materials exhibit 5-7 times the R-value of typical nonvacuum insulating materials depending on vacuum level and barrier and filler type. Uses for these VIPs (vacuum insulation panels) include refrigeration and controlled-temperature shipping containers. [Pg.219]

During a continuous extrusion process, the feed stock is required to have good flow properties inside the hopper. For the material to demonstrate good flow, the angle between the side wall of the feeding hopper... [Pg.2004]

Reactive extrusion is well surveyed by a recent text (Xanthos, 1992), and has been referred to as the deliberate performance of chemical reactions during continuous extrusion of polymers and/or polymerizable monomers (Xanthos, 1992). This usually represents chemical reactions conducted during a continuous extrusion process at relatively short residence times. Examples of types of reactions and example polymer systems used in reactive-extrusion processes are given in Table 2.1. [Pg.178]

Like the extrusion of metals, the extrusion of plastics involves the continuous forming of a shape by forcing softened plastic material through a die orifice that has approximately the geometric profile of the cross-section of the work. The extruded form is subsequently hardened by cooling. With the continuous extrusion process, such products as rods, tubes, and shapes of uniform cross-section can be economically produced. Extrusion to obtain a sleeve of the correct proportion almost always precedes the basic process of blow molding. [Pg.1324]

A continuous extrusion process, as well as molding techniques, can be used as the thermoforming method. A more rapid rate of cure is then necessary to ensure the cure of the rubber before the cellular structure collapses. The stock is ordinarily extruded at a temperature high enough to produce some curing and expansion and then oven-heated to complete the expansion and cure. [Pg.1036]

TABLE 17.5 Effect of CO2 Content on the Physical Characteristics of Neat PLA and PLA/Talc Foamed in a Continuous Extrusion Process [73, 74]... [Pg.283]

While these previous studies offered valuable insights, demonstrating the continuous extrusion process of PLA foamed with supercritical CO2, the morphology achieved in foamed PLA failed to satisfy the definition of microcellular foam due to lower cell population density (less than 10 cells/ cm ) with cells being larger than 60 m in average size. Distinctions between these features and microcellular foam... [Pg.284]

Matuana and Diaz [79] examined the effect of processing temperature on the pressure drop rate, cell population density, and average cell size to understand the nucleation mechanisms in PLA foamed in a continuous extrusion process (Figure 17.7 and Table 17.7). [Pg.285]

The compression properties of amorphous PLA foamed in a continuous extrusion process using CO2 as a blowing agent are summarized in Table 17.12. Correlations were found by plotting the compressive modulus E) and stress at yield (tr) as a function of CO2 content. The decreased modulus and strength with the CO2 content is due to the high level of plasticization induced by the residual CO2 for specimens foamed at higher CO2 content [73, 74]. [Pg.288]

Recent developments as automotive fuel tanks and 55-gal drums have been produced using multilayer materials for barrier purposes and to use up the regrind. Thus, more use of the continuous extrusion process without the accumulator due to use of multilayer materials. [Pg.269]

Wire and cable insulation has a significant volume of rubber consumption. Rubber compounds based on such elastomers as CPE, EPDM, silicone, and thermoplastic elastomers are used for this purpose. In a continuous extrusion process, these compounds are applied to the wire as insulation. [Pg.596]

Abstract. Crystalline and amorphous interfaces were formed and modified in multiphase composite and pharmaceutical systems. Nanosize drug of antacid effect was prepared in continuous extrusion process. The structural features were analyzed using (micro-) thermal analytical and (micro-) Raman spectrometric methods combined with chemometric evaluation. [Pg.211]

A continuous extrusion process was also used to produce foamed sheets. The extrusion line is composed by a lab-scale twin-screw extruder (Haake CTWIOO), a hot heat exchanger, and a capillary system acting as nucleation nozzle. The latter device allowed for a good control of the pressure profile in the extrusion line. Detailed monitoring of the process parameters was obtained by means of four pressure transducers and five melt thermocouples. [Pg.279]

With the latter type of process it is possible to prepare foams under free expansion conditions, which is not possible to obtain in continuous extrusion processes. During the free expansion, the material does not experience extensional and/or shear stresses, and the analysis of cell nucleation and growth is more rigorous. The system is constituted by a cylinder, where the temperature is kept constant by means of an oil bath and/or an electrical resistance. Gas, under different pressure conditions is inserted in the chamber and, after complete solubilisation in the polymeric melt, the pressure is released at controlled drop rate. There are several parameters that influence the entire process, the most important ones are a) the saturation pressure, that determines the amount of gas dissolved in the polymer and hence the final density b) the foaming temperature, that affects the final density and the structure of the foam c) the pressure drop rate, that affects the nucleation rate and determines the cell density. [Pg.284]

Plastics sheet is manufactured by the main processes of press moulding, casting or by extrusion. In general, the very thick gauges of sheet continue to be press moulded, but by far the greatest proportion is produced by the continuous extrusion process (Fig. 1), and by this means sheet thicknesses ranging from 0.010 to 0.5 in (0.25 to 12.5 mm) can be economically produced, and thicknesses up to 0.75 in (22.8 mm) are also possible by extrusion. [Pg.81]


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See also in sourсe #XX -- [ Pg.79 , Pg.81 , Pg.82 ]




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