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Column liquid redistribute

The variations in the column flow profiles are caused by the liquid side draws. The liquid flow at the top of the column is the reflux rate. Each liquid draw removes a portion of the column liquid flow. With a reduced liquid flow, the vapor flow also decreases since the LIV ratio remains unchanged, assuming other factors are constant. The column flow profiles can be manipulated by redistributing the condenser duty among side coolers along the column. [Pg.311]

As vapor moves up the column and the liquid moves down, there is a continuous redistribution of the two components between the liquid and vapor phases to establish equilibrium at each position (that is, each temperature) in the column. This redistribution must take place quickly if the equilibrium is to be established at every position. There... [Pg.303]

Liquid redistributors are used wherever an intermediate liquid feed is introduced into a packed column, and between packed sections, wherever liquid redistribution is required. [Pg.71]

For fast reactions, change in the flow regime has dramatic effects on performance. Prevent foaming. Liquid distributor design is very important. Carefully plan the liquid redistribution along the walls for columns < 2-3 m diameter. For these small columns place redistributors at distances = 8-10 times the column diameter. The critical surface tension of the solid packing should be greater than the surface tension of the liquid to ensure that the liquid film remains intact in a packed contactor. [Pg.243]

A basic requirement for the proper functioning of a packed column is that its diameter should be at least ten times the nominal size of the packing (see Table 5.6) to ensure adequate distribution of the gas and, particularly, the liquid. Redistribution sections, in which the liquid down-flow is collected and redistributed over entire tower cross sections, are often inserted to ensure good performance. On the other hand, the tower cannot be too large for structural and economic reasons. A normal diameter range is 0.5 to 5 m, but diameters as high as 14 m have been reported. [Pg.221]

Packed columns must be provided with good initial distribution of liquid across the column cross section and redistribution of liquid at various height intei vals that decrease with increasing column diameter. A wide variety of distributors and redistributors are available. Packed columns should be considered when ... [Pg.1346]

Internal uniform distribution Properly designed devices to distribute and redistribute liquid entering the column is critical to obtain best performance of these types of packings. [Pg.342]

Redistributors are used to collect liquid that has migrated to the column walls and redistribute it evenly over the packing. They will also even out any maldistribution that has occurred within the packing. [Pg.612]

The height of the column for a packed column needs to allow for liquid distribution and redistribution. As the feed enters the column, the liquid above the feed needs to be collected, combined with the feed liquid and distributed across the packing below the feed using troughs,... [Pg.172]

The assembly shown in Fig. 2.104 illustrates a set-up for simple fractionation using a Vigreux column which has moderate fractionating efficiency and is probably one of the most widely used columns. The column consists of a glass tube with a series of indentations such that alternate sets of indentations point downwards at an angle of 45° in order to promote the redistribution of liquid from the walls to the centre of the column. The mixture to be fractionated is placed in a flask of convenient size (it should be one-third to one-half full), a few fragments of porous porcelain added and a water condenser attached to the side-arm. The distillate is collected in small flasks or in test tubes. The bulb of the thermometer... [Pg.173]

Liquid redistributors are installed at frequent intervals in a packed column to remix the liquid, thus counteracting the propagation of maldistribution effects and the natural tendency of liquid to migrate toward the wall. A common design practice is to redistribute the liquid every 20 ft (6-7 m). [Pg.25]

In large-diameter towers and long beds, a redistributor may help correct a maldistributed composition profile. For instance, remixing stage 4 liquid of the two columns in Example 9.1 would have alleviated the pinch. Good redistribution prectices are discussed elsewhere... [Pg.541]

Since liquid maldistribution may become a problem unless the flow is periodically redistributed in a tall column, the total packing height must be broken up into a number of individual beds ... [Pg.371]

Liquid Distribution Good initial distribution is not as essential in a sieve tray extractor as it is in a packed extractor, since the trays provide redistribution. While the same distributors used in packed columns are... [Pg.1760]


See other pages where Column liquid redistribute is mentioned: [Pg.614]    [Pg.469]    [Pg.769]    [Pg.198]    [Pg.641]    [Pg.1385]    [Pg.1044]    [Pg.173]    [Pg.87]    [Pg.683]    [Pg.1044]    [Pg.9]    [Pg.489]    [Pg.46]    [Pg.386]    [Pg.538]    [Pg.268]    [Pg.67]    [Pg.1208]    [Pg.413]    [Pg.1749]    [Pg.2136]   
See also in sourсe #XX -- [ Pg.2 , Pg.523 , Pg.524 ]




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