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Saddle packing dehydration

Figure 6.4 Standard ceramic saddle packing for Fig. 6.3 s dehydration packed bed tower (Koch-Knight, 2012). Saddles used in acid plants are typically 0.05-0.08 m, maximum dimension. Acid descends around and through the saddles while H20(g) laden gas ascends, creating turbulence and a large acid-gas interface. Figure 6.4 Standard ceramic saddle packing for Fig. 6.3 s dehydration packed bed tower (Koch-Knight, 2012). Saddles used in acid plants are typically 0.05-0.08 m, maximum dimension. Acid descends around and through the saddles while H20(g) laden gas ascends, creating turbulence and a large acid-gas interface.
These conditions are obtained by carrying out the process with counter-current flow in a ceramic saddle -packed bed (Figs. 6.4 and 6.6). Warm conditions, 50-70 °C, atop the dehydration tower also help. [Pg.65]

The tendency in ceramic packing is towards high surface area, low gas flow resistance perforated saddles. These saddles give rapid dehydration with low resistance to gas flow. [Pg.69]

See other pages where Saddle packing dehydration is mentioned: [Pg.62]    [Pg.62]    [Pg.62]    [Pg.976]    [Pg.62]   
See also in sourсe #XX -- [ Pg.59 ]



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