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Advantages of Packing vs. Trays

Since we do not rely on pumparounds to fractionate—but just to remove heat—good vapor-liquid distribution is not critical. A bed of 4 or 5 ft of structured packing is often, then, an excellent selection for the pumparound section of a tower. The capacity of such a bed potentially has a 30 to 40 percent advantage over trays. [Pg.136]

Finally, the pressure drop of the vapor flowing through a packed tower will be an order of magnitude less than through a frayed tower. For vacuum distillation service, this is often of critical importance. [Pg.136]

Water Hammer and Condensate Backup Steam-Side Reboiler Control [Pg.119]

A few of the nasty features of this sort of process equipment we discuss are [Pg.119]

When considering the steam side of steam heated reboilers, it is best to think about the reboiler as a steam condenser. The steam, at least for a conventional horizontal reboiler, is usually on the tube side of [Pg.119]


See other pages where Advantages of Packing vs. Trays is mentioned: [Pg.85]    [Pg.135]    [Pg.117]   


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