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Multicomponent distillation packed towers

The concepts NTU and HTU are defined only for binary distillations and the transfer of a single substance in absorption or stripping. Since most processes of industrial interest involve multicomponents, the HETS of packed towers is the more useful concept, and may be evaluated readily from test data and tray calculations. [Pg.401]

Multicomponent distillation, 393 absorption factor method, 398 azeotropic, 420-426 bubblepoint (BP) method, 406-409 computer program references. 404 concentration profiles, 394 distribution of non-kevs. 395 Edmister method, 398,399 extractive, 412, 417-422 feed tray location, 397 free variables, number of 395 Lewis-Matheson method 404 MESH eauations. 405-407 molecular, 425-427 nomenclature, 405 number of theoretical trays, 397 packed towers, 433-439 petroleum, 411-415 reflux, minimum, 397 reflux, operating, 397 SC (simultaneous correction) method, 408-411... [Pg.752]

See other pages where Multicomponent distillation packed towers is mentioned: [Pg.497]    [Pg.501]    [Pg.564]    [Pg.507]    [Pg.511]    [Pg.469]    [Pg.564]    [Pg.5]   
See also in sourсe #XX -- [ Pg.433 , Pg.434 , Pg.435 , Pg.436 , Pg.437 , Pg.438 ]

See also in sourсe #XX -- [ Pg.457 , Pg.458 , Pg.459 ]

See also in sourсe #XX -- [ Pg.433 , Pg.434 , Pg.435 , Pg.436 , Pg.437 , Pg.438 ]

See also in sourсe #XX -- [ Pg.433 , Pg.434 , Pg.435 , Pg.436 , Pg.437 , Pg.438 ]

See also in sourсe #XX -- [ Pg.433 , Pg.434 , Pg.435 , Pg.436 , Pg.437 , Pg.438 ]



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