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Sieve trays with downcomers calculations

Example 18.6. A sieve-plate column operating at atmospheric pressure is to produce nearly pure methanol from an aqueous feed containing 40 mole percent methanol. The distillate product rate is 5800 kg/h. (a) For a reflux ratio of 3.5 and a plate spacing of 18 in., calculate the allowable vapor velocity and the column diameter. b) Calculate the pressure drop per plate if each sieve tray is in, thick with j-in, holes on a -in. triangular spacing and a weir height of 2 in. (c) What is the froth height in the downcomer ... [Pg.566]

A sieve-tray column with 15 plates is used to prepare 99 percent methanol from a feed containing 40 percent methanol and 60 percent water (mole percent). The plates have 8 percent open area, in. holes, and 2-in. weirs with segmental downcomers, (a) If the column is operated at atmospheric pressure, estimate the flooding limit based on conditions at the top of the column. What is the F factor and the pressure drop per plate at this limit (Z>) For the flow rate calculated in part (a) determine the F factor and the pressure drop per plate near the bottom of the column. Which section of the column will flood first as the vapor rate is increased ... [Pg.587]

A mixture of three components (60% benzene, 30% toluene and 10% ethylbenzene) is separated in a DWG with sieve plates and lateral downcomers. The vapor pressures Ry of components were calculated on the basis of Antoine equation, and the trays efficiency was set at value 1 (equilibrium trays). [Pg.315]


See other pages where Sieve trays with downcomers calculations is mentioned: [Pg.498]    [Pg.508]    [Pg.380]    [Pg.721]   
See also in sourсe #XX -- [ Pg.195 , Pg.199 ]

See also in sourсe #XX -- [ Pg.195 , Pg.199 ]




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