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Lewis-Matheson method multicomponent distillation

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]

The general methods of design for multicomponent distillation apply. Since in most cases all the components of the feed streams are found in the bottoms, the method of Lewis and Matheson can be used, starting at the bottom and computing to the top. There will be an optimum solvent-circulation rate small solvent rates require many trays, but the column diameters are small large ratios require fewer trays but larger column diameters and greater solvent-circulation costs. [Pg.459]

See other pages where Lewis-Matheson method multicomponent distillation is mentioned: [Pg.206]   
See also in sourсe #XX -- [ Pg.404 ]

See also in sourсe #XX -- [ Pg.429 ]

See also in sourсe #XX -- [ Pg.404 ]

See also in sourсe #XX -- [ Pg.404 ]

See also in sourсe #XX -- [ Pg.404 ]



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