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Screw-channel depth

Thus traditional analysis predicts that when only the z-direction velocity is converted to the laboratory frame, the laboratory flow solution is toward the inlet of the extruder. Thus to be absolutely correct, the Literature Theory line of Fig. 7.13 should be below the x axis and predict a negative flow for all screw channel depths. [Pg.270]

Solubility Mixing time (min) Screw channel depth... [Pg.338]

Screw Channel Depth Very Shallow shallow long ... [Pg.44]

By choosing characteristic variables for temperatures, velocities and lengths we can reduce the dimensionality even further. The temperature is scaled based on the maximum gradient, the length with the gap thickness and screw channel depth and the velocity with the barrel x-velocity,... [Pg.223]

Devolatilizing Screw Extruder A 150-mm-diameter, square-pitched, single-flighted screw extruder, with screw channel depth of 25 mm and 20-mm flight width is used to devolatilize a 1000-kg/h stream with 0.78-g/cm3 density at 200° C and 125 torr. (a) At what frequency of screw rotation will the channel be 30% or less full (b) With water injection, if density is halved by formation of 1-mm bubbles, how much surface area (per meter length) is created (c) How does... [Pg.445]

Shear in the channel of the screw is equal to KDN/6Qh (where D = average barrel inside diameter, N = screw RPM, and h = average screw channel depth). This formula does not include the melt slippage between the barrel wall and screw surfaces, but the shear rate obtained is still useful for purposes of comparison. A l in. screw with a 0.140 in. channel rotating at 100 RPM results in a shear rate of 93.5 reciprocal seconds (rsec). This value is approximately the desired value in most extrusion processes, with 100 rsec generally the target. [Pg.9]

Decreasing-lead screw n. A screw in which the helix angle decreases steadily over the length of the screw. Channel depth is usually constant. [Pg.386]

An extruder (0.05-m-diam screw channel depth of 0.01 m) has a helix angle of 26°. If all surfaces have the same coefficient of friction, what is the Q/N value for the extruder s solids-conveying section ... [Pg.306]

However, for all four screw temperatures the predicted melting rate in the numerical simulation is still significantly higher than the experimental data in Fig. 2. For simulation results as well as for the experimental data in Fig. 2, the sohd fi action presented in Fig. 7 was measured as a ratio of the sohd bed width to the width of the serew ehannel. The sohd fi action thus obtained was further normalized by multiplying it with the ratio of the current screw ehannel depth to the screw channel depth at the entrance of the compression section. [Pg.736]

In a particular extruder screw the channel depth is 2.4 mm, the screw diameter is 50 mm, the screw speed is 100 rev/min, the flight angle is 17° 42 and the pressure varies linearly over the screw length of 1000 mm from zero at entry to 20 MN/m at the die entry. Estimate... [Pg.340]

An extruder is coupled to a die, the output of which is given by (KP/ij) where P is the pressure drop across the die, i] is the visco.sity of the plastic and is a constant. What are the optimum values of screw helix angle and channel depth to give maximum output from the extruder. [Pg.340]

Why does the channel depth of the screw generally decrease as you move from the feed zone to the metering zone of an extruder ... [Pg.227]

In the simplest and most often used form, the screw has a free channel cross-section that diminishes at a steady rate from the feed to the delivery end. The ratio of the channel depths from feed to die region along the screw is usually referred to as the compression ratio, since it gives a crude indication of the relative conveying capacities at feed and discharge. [Pg.182]

Apart from improving the mixing effect in the deeper part of the screw the restriction that occurs towards the delivery end also helps to make sure that the screw runs full. If a screw does not have a diminishing channel depth along its length then it is difficult to feed rubber at a rate that will keep up with its unrestricted conveying capacity. The screw then runs partially filled after the feed opening and only becomes completely filled at a point that allows sufficient pressure to be developed to overcome the restriction at the die. [Pg.183]

Cij Deformation rate / Fraction of screw channel filled with liquid F[> Ihag flow shape factor H, h Channel depth in screw extruder... [Pg.102]


See other pages where Screw-channel depth is mentioned: [Pg.299]    [Pg.582]    [Pg.586]    [Pg.486]    [Pg.306]    [Pg.307]    [Pg.2]    [Pg.89]    [Pg.180]    [Pg.70]    [Pg.194]    [Pg.299]    [Pg.582]    [Pg.586]    [Pg.486]    [Pg.306]    [Pg.307]    [Pg.2]    [Pg.89]    [Pg.180]    [Pg.70]    [Pg.194]    [Pg.441]    [Pg.137]    [Pg.273]    [Pg.1647]    [Pg.1648]    [Pg.1651]    [Pg.246]    [Pg.340]    [Pg.328]    [Pg.215]    [Pg.216]    [Pg.4]    [Pg.8]    [Pg.9]    [Pg.9]    [Pg.16]    [Pg.17]    [Pg.19]    [Pg.111]    [Pg.134]    [Pg.146]    [Pg.159]    [Pg.160]   
See also in sourсe #XX -- [ Pg.486 ]




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