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Disk processor

Example 6.5 The Synthesis of the Disk Processor In this example, we once again take building block 1 and pair it with the flat face of a rotating disk to obtain a disk processor, as shown in Fig. E6.5a. As was the case in the roll pump, the inlet and outlet ports are cut into the... [Pg.244]

Fig. 6.32 Shape-correction factors for parallel-shaped chambers. [Reproduced by permission from Y. Edelist and Z. Tadmor, Velocity Profiles in a Co-rotating Disk Processor Polym. Process Eng., 1,1 (1983).]... Fig. 6.32 Shape-correction factors for parallel-shaped chambers. [Reproduced by permission from Y. Edelist and Z. Tadmor, Velocity Profiles in a Co-rotating Disk Processor Polym. Process Eng., 1,1 (1983).]...
P. S. Mehta, L. N. Valsamis, and Z. Tadmor, Foam Devolatilization in Multi-Channel Corotating Disk Processors, Polym. Process Eng, 2, 103-128 (1984). [Pg.315]

In screw extruders, as we have seen, the processing takes place in the helical channel formed between the screw and the barrel. In a co-rotating disk processor (CDP), on the other hand, processing takes place in flat doughnut-shaped processing chambers formed by two neighboring disk surfaces, the inner surface of the barrel, the shaft to which the disks are attached, and the channel block attached to the barrel, with very small clearance to the disk surfaces. It thus blocks the channel and separates inlet from outlet, as shown in Fig. 9.44. Processing chambers can be connected in series, parallel, or any other... [Pg.507]

Fig. 9.49 The evolution of the interfacial area of a viscous Thiokol rubber in a 26.6-cm parallel-disk mixing chamber with a. — 0.5, with the number of turns. The rubber filled up half the chamber with one-quarter cream color (at the channel block at the left side) and one-quarter black. The numbers on the figure indicate the number of turns from 1/4 to 10. [Reprinted by permission from B. David and Z. Tadmor, Laminar Mixing in Co-rotating Disk Processors, Int. Polym. Process., 3, 38-47 (1988).]... Fig. 9.49 The evolution of the interfacial area of a viscous Thiokol rubber in a 26.6-cm parallel-disk mixing chamber with a. — 0.5, with the number of turns. The rubber filled up half the chamber with one-quarter cream color (at the channel block at the left side) and one-quarter black. The numbers on the figure indicate the number of turns from 1/4 to 10. [Reprinted by permission from B. David and Z. Tadmor, Laminar Mixing in Co-rotating Disk Processors, Int. Polym. Process., 3, 38-47 (1988).]...
Fig. 9.51 Separation efficiency in consecutive chambers of 450°F PS melt fed at 42 lb/h into 0.54-in-wide chambers at 50-torr absolute pressure, with disks rotating at 30 rpm. [Reprinted by permission from P. S. Mehta, L. N. Valsamis, and Z. Tadmor, Foam Devolatihzation in a Multichannel Corotating Disk Processor, Polymer Process Eng., 2, 103-128 (1984).]... Fig. 9.51 Separation efficiency in consecutive chambers of 450°F PS melt fed at 42 lb/h into 0.54-in-wide chambers at 50-torr absolute pressure, with disks rotating at 30 rpm. [Reprinted by permission from P. S. Mehta, L. N. Valsamis, and Z. Tadmor, Foam Devolatihzation in a Multichannel Corotating Disk Processor, Polymer Process Eng., 2, 103-128 (1984).]...
Fj Drag-flow shape factor for co-rotating disk processor (Example 6.12)... [Pg.919]

Oil and grease vacuum manifold, extraction disk processors... [Pg.334]


See other pages where Disk processor is mentioned: [Pg.3]    [Pg.5]    [Pg.236]    [Pg.246]    [Pg.278]    [Pg.447]    [Pg.447]    [Pg.519]    [Pg.519]    [Pg.521]    [Pg.522]    [Pg.5]    [Pg.7]   


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