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Pressure melting, effect

One of the common problems associated with underwater pelletizers is the tendency of the die holes to freeze off. This results in nonuniform polymer melt flow, increased pressure drop, and irregular extrudate shape. A detailed engineering analysis of pelletizers is performed which accounts for the complex interaction between the fluid mechanics and heat transfer processes in a single die hole. The pelletizer model is solved numerically to obtain velocity, temperature, and pressure profiles. Effect of operating conditions, and polymer rheology on die performance is evaluated and discussed. [Pg.132]

Figure 10. Pelletizer pressure drop. Effect of polymer melt index (MI). Figure 10. Pelletizer pressure drop. Effect of polymer melt index (MI).
It is most important to know in this connection the compressibility of the substances concerned, at various temperatures, and in both the liquid and the crystalline state, with its dependent constants such as change of. melting-point with pressure, and effect of pressure upon solubility. Other important data are the existence of new pol3miorphic forms of substances the effect of pressure upon rigidity and its related elastic moduli the effect of pressure upon diathermancy, thermal conductivity, specific heat capacity, and magnetic susceptibility and the effect of pressure in modif dng equilibrium in homogeneous as well as heterogeneous systems. [Pg.8]

The melting point of liquids is raised by increasing the pressure this effect amounts to 15-20 °C per 100 MPa. Tables 2 and 3 summarize the freezing temperatures [3] and the viscosity of common solvents at high pressure, respectively [14]. [Pg.6]

Furthermore, it is not surprising that the thermal conductivity of melts increases with hydrostatic pressure. This effect is clearly shown in Fig. 2.3 [19]. As long as thermosets are unfilled, their thermal conductivity is very similar to amorphous thermoplastics. Anisotropy in thermoplastic polymers also plays a significant role in the thermal conductivity. Highly drawn semi-crystalline polymer samples can have a much higher thermal conductivity as a result of the orientation of the polymer chains in the direction of the draw. [Pg.39]

At atmospheric pressure, AS will decompose before it will melt. Upon decomposition it releases ammonia and leaves bisulfate behind. Above 300°C, decomposition gives N2, SO2, SOj and H2O in addition to ammonia. Its vapor pressure is effectively zero up to 80°C. [Pg.298]

Parabola at center 13.87 mm to 13.97 mm. Melt temp., hold pressure, hold time, and injection speed Same trends as above (for parabola at 10.16 mm.) with, in this case, hold time having the biggest effect, followed by injection speed and hold pressure melt temperature has the least effect. [Pg.206]

The data of [19650LS/MUL] and [1967BEN/HOF] show that ThN melts effectively congruently under 1-2 bar pressure of nitrogen at (3080 30) K. The above selections yield ... [Pg.309]

Maeda Y, Kanetsuna H (1975) Crystallization and melting of pdydhylene under high pressure. II. Effect of pressure on melting behavior of various types of crystals. J. Polymer Sd., Polymer Phys. Ed., 13 637... [Pg.110]

Isomer effects cannot be predicted. This means the same activity coefficients are obtained, for example, for o-/m-/p-xylene or phenanthrene/anthracene with the different solvents. But at least in the case of VLE or SLE calculation this is not a great problem, since the required standard fugacities, that is, vapor pressure, melting point, and heat of fusion are of much greater importance than small differences of the activity coefficients. Similar problems are also observed for other predictive models, for example, the quantum chemical approach. [Pg.309]

If the flight pitch is constant and the polymer melt viscosity can be described by Eq. 8.78, the maximum diehead pressure for effective devolatilization can be written as [2] ... [Pg.555]

In the i-Am,NI-H 0 system (figTd) clathrate formation is rapid and occurs at atmospheric pressure P S/, For this reaction dt/dP =4.5 C/kbar (l atm). At 0.26 kbar one more hydrate (h2) forms with a smaller hydrate number, which is shown hy the appearance of the melting effects of water eutectics in the samples in which the salt content slightly e x-ceeds that in the low pressure hydrate. We have managed to identify not only the incongruent melting lines of the hydrates, but also the monovariant equilibrium line The heat effect of this transition is... [Pg.207]

Process variables are dependent variables and the collective effect of the machine setting such as cavity and nozzle pressure, melt viscosity, and mold separation [65]. They are... [Pg.85]

Melting/Crystallization at High Pressures (Hydrostatic Effect)... [Pg.104]

Various parameters are evaluated which may affect ejection force during injection molding of syndiotactic polystyrene. Increase in mold temperature results in large decrease of ejection force. A predictive model was developed which allows evaluation of the combination of hold pressure, melt temperature, and mold temperature. To decrease ejection force by 72%, mold temperature has to be increased from 60 to 93°C. Also, increase of hold pressure contributes to a small decrease of ejection force. Figure 10.11 shows the effect of mold temperature and temperature of the part, immediately after ejection on the ejection force. [Pg.267]


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See also in sourсe #XX -- [ Pg.80 ]

See also in sourсe #XX -- [ Pg.64 ]




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