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Downcomer, distillation liquid height

With relatively high outlet weir height hw, the clear liquid height h increases and vapor and liquid contact time increases. This improves distillation efficiency. However, a too high outlet weir height could affect the downcomer backup and tray capacity. [Pg.244]

Depending on the tray geometry (diameter, weir height, downcomer design, etc.) in trayed columns or on the type of packing in packed columns, a certain amount of liquid is retained within the column as liquid holdup. An additional amount of liquid holdup is associated with the condenser assembly. The remaining space within the distillation system contains the vapor holdup. In continuous columns, holdup is usually not a factor since it does not affect the separation as long as the column operates at steady state. [Pg.574]

The most common applications of this technique in distillation and absorption columns is for liquid level and liquid level interface detection, especially when normal level-measuring techniques suffer from plugging. Neutron backscatter techniques have also been used for froth height measurements on trays and downcomers, and for measuring the top and bottom of packed beds. One case history has been described (71) where downcomer froth height measurements using the neutron backscatter technique led to a detection of downcomer deposits which caused premature flooding of the column. The author is familiar with one case where this technique successfully detected overflow of a packed tower distributor. [Pg.431]

Downcomer seal On a distillation tray, the height of liquid above the... [Pg.711]


See other pages where Downcomer, distillation liquid height is mentioned: [Pg.498]    [Pg.508]    [Pg.131]    [Pg.399]    [Pg.406]    [Pg.29]    [Pg.31]    [Pg.199]    [Pg.1582]    [Pg.1584]    [Pg.807]    [Pg.1578]    [Pg.1580]    [Pg.549]   
See also in sourсe #XX -- [ Pg.168 ]

See also in sourсe #XX -- [ Pg.168 ]




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