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Random packings metal

Table 5 Packing factors random packing, metal... Table 5 Packing factors random packing, metal...
Fig. 21. Random packing elements for distillation columns (a), Raschig ring (metal) (b). Bed saddle (ceramic) (c), Intalox saddle (ceramic) (d), PaH ring... Fig. 21. Random packing elements for distillation columns (a), Raschig ring (metal) (b). Bed saddle (ceramic) (c), Intalox saddle (ceramic) (d), PaH ring...
Corrosivity. Corrosivity is an important factor in the economics of distillation. Corrosion rates increase rapidly with temperature, and in distillation the separation is made at boiling temperatures. The boiling temperatures may require distillation equipment of expensive materials of constmction however, some of these corrosion-resistant materials are difficult to fabricate. For some materials, eg, ceramics (qv), random packings may be specified, and this has been a classical appHcation of packings for highly corrosive services. On the other hand, the extensive surface areas of metal packings may make these more susceptible to corrosion than plates. Again, cost may be the final arbiter (see Corrosion and corrosion control). [Pg.175]

Figure 9-6K. Nutter Ring (metal random packing). Used by permission of Nutter Engineering, Harsco Corp., Bull. NR-2. Figure 9-6K. Nutter Ring (metal random packing). Used by permission of Nutter Engineering, Harsco Corp., Bull. NR-2.
Figure 9-6N(a). Koch Metal HcKp " random packing. Used by permission of Koch Engineering Co., Inc., Bull. KRP-2. [Pg.240]

Figure 9-21G. Generalized pressure drop correlation for non-foaming systems for IMTP metal random packing. Parameter of curves is pressure drop in inches of water/foot packed height. Numbers in parentheses are mm of water/meter of packed height. Used by permission of Norton Chemical Process Products Corp., Bull-IHP-1, 12/91 (1987). Figure 9-21G. Generalized pressure drop correlation for non-foaming systems for IMTP metal random packing. Parameter of curves is pressure drop in inches of water/foot packed height. Numbers in parentheses are mm of water/meter of packed height. Used by permission of Norton Chemical Process Products Corp., Bull-IHP-1, 12/91 (1987).
Sintered metal fibers with filaments of uniform size (2-40 (tm), made of SS, Inconel, or Fecralloy , are fabricated in the form of panels. Gauzes based on thicker wires (100-250 tm) are made from SS, nickel, or copper. They have a low surface area of about 10 m g. Several procedures are used to increase the surface area, for example, leaching procedures, analogous to the production of Ra-Nickel, and electrophoretic deposition of particles or colloid suspensions. The porosity of structures formed from metal fibers range from 70 to 90%. The heat transfer coefficients are high, up to 2 times larger than for random packed beds [67]. [Pg.201]

Structured packings are produced by a number of manufacturers. The basic construction and performance of the various proprietary types available are similar. They are available in metal, plastics and stoneware. The advantage of structured packings over random packing is their low HETP (typically less than 0.5 m) and low pressure drop (around 100 Pa/m). They are being increasingly used in the following applications ... [Pg.592]

Fib er-Bed Scrubbers Fibrous-bed structures are sometimes used as gas-liquid contactors, with cocurrent flow of the gas and liquid streams. In such contactors, both scrubbing (particle deposition on droplets) and filtration (particle deposition on fibers) may take place. If only mists are to be collected, small fibers may be used, but if solid particles are present, the use of fiber beds is limited by the tendency of the beds to plug. For dust-collection service, the fiber bed must be composed of coarse fibers and have a high void fraction, so as to minimize the tendency to plug. The fiber bed may be made from metal or plastic fibers in the form of knitted structures, multiple layers of screens, or random-packed fibers. However, the bed must have sufficient dimensional stability so that it will not be compacted during operation. [Pg.43]

Pressure drop has been reported for a number of rotor internals, including corrugated structured packing (28), foam metal (26,40,42), rectangular and elliptical cylinder plastic grains randomly packed (41), wire screen (43), and glass beads (17). In spite of the variation in porosity from 0.38 to 0.95 and in volumetric surface area from 500 to 4000 m2/m3, all of these studies showed similarities of increased pressure drop as rotor speed increased and gas rates increased. [Pg.55]

As an alternative to trays, especially at low volumetric liquid-to-vapor ratios, packing can be used to promote vapor-liquid contact. One approach is to dump specially shaped pieces of metal, glass, or ceramic material into the column, wherein they are supported on a grid. An example of dumped or random packing is shown in Fig. 7. [Pg.226]

Figure B.1 First-generation random packings, (a) Raschig ring, metal (6) Lessing ring, metal (c) Berl saddle, ceramic. Figure B.1 First-generation random packings, (a) Raschig ring, metal (6) Lessing ring, metal (c) Berl saddle, ceramic.
Figure 8.2 (Continued) Second-generetion random packings, (cl Super Intalox seddie, plastic (d) Pall ring, metal, (Courtesy of Norton Company.)... Figure 8.2 (Continued) Second-generetion random packings, (cl Super Intalox seddie, plastic (d) Pall ring, metal, (Courtesy of Norton Company.)...
Figure (Continued Third-generation metal random packings, (e) HcKp (f) FLEXIMAX (Parti e and f courtesy of Koch Engineering Company, lnc. ... Figure (Continued Third-generation metal random packings, (e) HcKp (f) FLEXIMAX (Parti e and f courtesy of Koch Engineering Company, lnc. ...

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See also in sourсe #XX -- [ Pg.237 , Pg.238 , Pg.239 , Pg.240 ]

See also in sourсe #XX -- [ Pg.237 , Pg.238 , Pg.239 , Pg.240 ]




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