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Flat films

Flat films processed through slit dies are cooled principally by using chilled rolls. Many different resins are used, with thicknesses ranging from 15 to 200 fim (Figs. 3-26 and 3-27). Alternatively, certain plastics go directly into a water tank, but that creates many technical difficulties in production. Thus, the chill roll process is preferred and film up to 3 m in width will have output rates of at least 120 m/min. [Pg.144]

In this process, the melt film contacts (as quickly as possible, vertically or at an angle) the first water-cooled highly polished (to 1 ptm) chrome-plated roll. An air knife can be used its placement parallel to the die makes it possible to press the film smoothly onto the first cooling roll by means of a cold air stream. Lubricant plate-out on the cooling rolls is avoided by operation with contact rolls. At haul-off rates of up to 60 m/min, reel change is carried out by hand. At higher rates, automatic changeover equipment is required. [Pg.144]

Sheet is usually defined as being thicker than film, or thicker than 1 to 4 mm ( 0.003-0.010 in). Sheet thickness can be at least 2 mm (0.5 in.), and widths can be up to 30 m (10 ft). Basically, hot melt from a slit die is directed to a combination of an air knife with two cooling rolls, or, a more popular choice, to a three-cooling-roll stand (Fig. 3-28), which cools, calibrates, and produces a smooth sheet. To aid the chill rolls, end sections of the die are operated at a higher heat than the center (Fig. 3-12c). Cooling rolls require this type of heat control from their ends to the center. [Pg.147]

The operation (as well as design) of a slit die, particularly for wide sheets, requires extensive experience. Its rather high melt pressure can deform the die. [Pg.147]


Flash spinning Flat-bed screen printing Flat film Flat glass... [Pg.405]

Fig. 3. Two-dimensional schematic illustrating the distribution of Hquid between the Plateau borders and the films separating three adjacent gas bubbles. The radius of curvature r of the interface at the Plateau border depends on the Hquid content and the competition between surface tension and interfacial forces, (a) Flat films and highly curved borders occur for dry foams with strong interfacial forces, (b) Nearly spherical bubbles occur for wet foams where... Fig. 3. Two-dimensional schematic illustrating the distribution of Hquid between the Plateau borders and the films separating three adjacent gas bubbles. The radius of curvature r of the interface at the Plateau border depends on the Hquid content and the competition between surface tension and interfacial forces, (a) Flat films and highly curved borders occur for dry foams with strong interfacial forces, (b) Nearly spherical bubbles occur for wet foams where...
Extmsion of polyethylene and some polypropylenes is usually through a circular die into a tubular form, which is cut and collapsed into flat film. Extmsion through a linear slot onto chilled rollers is called casting and is often used for polypropylene, polyester, and other resins. Cast, as well as some blown, films may be further heated and stretched in the machine or in transverse directions to orient the polymer within the film and improve physical properties such as tensile strength, stiffness, and low temperature resistance. [Pg.453]

Figure 10.13. Methods of producing polyethylene film (a) tubular process using air cooling (b) flat film process using water bath cooling (c) flat film process using chill... Figure 10.13. Methods of producing polyethylene film (a) tubular process using air cooling (b) flat film process using water bath cooling (c) flat film process using chill...
Figure II.II. Two-stage orientation—flat films (After Gray reproduced with permission of The... Figure II.II. Two-stage orientation—flat films (After Gray reproduced with permission of The...
A plastic film, 0.1 mm thick, is required to have its orientation in the transverse direction twice that in the machine direction. If the film blowing die has an outer diameter of 100 mm and an inner diameter of 98 mm estimate the blow-up ratio which will be required and the lay flat film width. Neglect extrusion induced effects and assume there is no draw-down. [Pg.341]

The pumping pressure required on the melts entering the different designed die heads differs to meet their melt flow patterns within the die cavities. The pressure usually varies as follows (1) blown and lay-flat films at 13.8-41.3 MPa (2000-6000 psi) (2) cast film, sheet, and pipe at 3.5-27.6 MPa (500-4000 psi) (3) wire coating at 10.3-55.1 MPa (1500-8000 psi), and (4) monofilament at 6.9-20.7 MPa (1000-3000 psi). [Pg.463]

A fiber-diffraction pattern is recorded on a flat-film camera in which the fiber-to-photographic film distance is typically in the range of 3 to 4 cm. During exposure to X-rays, the specimen chamber is continuously flushed with a slow and steady stream of helium gas that has been bubbled through a saturated salt solution so that (a) the fiber is maintained at a constant desired r.h. and (b) fogging of the photographic film from air scattering is reduced. [Pg.314]

From the results of the urease activity test summarized in Figure 15, it is clear that the deposition procedure preserved to a certain extent the enzyme catalytic activity. Heating the sample before testing decreased the enzyme in the film by about 30% but did not eliminate it completely. The results of the activity test of two samples are summarized in Table 1 together with reference values for a spontaneous reaction without enzyme. It is necessary to underline that enzymatic activity on spherical supports was higher than the respective value in flat films, which could indicate that apparent catalytic efficiency was improved due to an increased area-to-volume ratio. [Pg.158]

Pseudo-partial wetting if 5 > 0 and P < 0. A macroscopic droplet with a finite contact angle can form on top of a flat film, while a microscopic droplet will spread to form a pancake or a diluted gas. [Pg.245]

X-ray diffraction pictures taken with a flat-film camera show that crosslinked SE-BR samples crystallize on stretching. Sharp reflections are observed at an extension ratio of 4 1 (Figure 4). With samples having different degrees of stereoregularity the order for increasing strain-induced crystallization is the same as the order for the rate of low temperature crystallization. [Pg.62]

V . The resulting fractal dimensions are listed with the dimension of the flat film surface in Table 2 (3rd column). [Pg.384]

The process is divided into five steps (see Fig. 9) Ecovio is first processed by the extruder to form a melt stream with constant melt temperature and output rate (Fig. 9, 1). In the forming section, the melt streams of several extruders can be merged into one using an adapter feed block or a multilayer die. These devices control the flow of each stream to obtain an even layer distribution (Fig. 9, 2) [30]. Then, the melt stream is transformed into a flat film in the film die. The thickness distribution is controlled automatically by means of expansion bolts. [Pg.119]

Lipkowski and coworkers [332] have applied several electrochemical techniques to study adsorption of A -dodecyl-A, N-dimethyl-3-ammonio-l-propanesulfonate, a model zwitterionic surfactant, on Au(lll) electrode. Adsorption of this compound proceeded via a few states. The first two states were observed at potentials close to the zero charge potential. At low bulk concentrations, a nearly flat film of the adsorbed molecules was formed, which was converted into a hemimicellar state at higher concentrations. The second state at negative potentials corresponded to... [Pg.876]

For wide angle scattering, flat film camera with appropriate film back and intensifying screen (Fig. 21.6)... [Pg.179]

Fig. 74. Arrangements for taking single-crystal rotation photographs (a) on flat films, (6) on cylindrical films. Fig. 74. Arrangements for taking single-crystal rotation photographs (a) on flat films, (6) on cylindrical films.
The length of c can be obtained very simply from this photograph by measuring the distance y of any layer line from the equator if the camera radius is r, then rjy is tan c is then given by wA/ccs , n being the number of the layer line selected (the equator having n = 0). For the potassium nitrate crystal, c is G-45 A. If a flat film is used instead of a cylindrical film, the layer lines are shown, not as straight lines... [Pg.149]


See other pages where Flat films is mentioned: [Pg.1380]    [Pg.388]    [Pg.427]    [Pg.155]    [Pg.155]    [Pg.145]    [Pg.376]    [Pg.377]    [Pg.419]    [Pg.441]    [Pg.669]    [Pg.235]    [Pg.236]    [Pg.461]    [Pg.625]    [Pg.483]    [Pg.88]    [Pg.364]    [Pg.314]    [Pg.259]    [Pg.264]    [Pg.222]    [Pg.65]    [Pg.79]    [Pg.234]    [Pg.447]    [Pg.161]    [Pg.156]    [Pg.185]    [Pg.183]    [Pg.117]    [Pg.113]   
See also in sourсe #XX -- [ Pg.4 , Pg.273 ]

See also in sourсe #XX -- [ Pg.14 ]




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Biaxial stretching of flat films

Duplex films, “flat

Extruder flat film

Extruder flat-film draw-ratio

Extruder flat-film orientation

Extruder flat-film tape

Extrusion flat-film

Extrusion of Flat Film, Sheet, and Tubing

Film canvas, flat

Film condensation vertical flat plate

Flat Film or Sheet Extrusion

Flat film camera

Flat film membranes

Flat film membranes reverse osmosis membrane

Flat plates film condensation

Flat-film production

Flat-panel displays, organic thin-film transistors

Flat-panel displays, organic thin-film transistors display technologies

Oxide films flat surfaces

Processing, thermoplastics flat film

Shrink flat film process

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