Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Packed towers flow arrangements

For finite flow rates of heavy liquid, hi will decrease, i.e., the interface will rise. This piping arrangement is not directly applicable to control of the extraction tower shown in Fig. 12.8, because of the variable pressure drop encountered in the packing and discharge line. [Pg.340]

See other pages where Packed towers flow arrangements is mentioned: [Pg.39]    [Pg.167]    [Pg.246]    [Pg.292]    [Pg.167]    [Pg.245]    [Pg.246]    [Pg.39]    [Pg.292]    [Pg.39]    [Pg.109]    [Pg.146]    [Pg.147]    [Pg.105]    [Pg.456]    [Pg.249]    [Pg.542]    [Pg.18]    [Pg.95]    [Pg.387]    [Pg.762]    [Pg.565]    [Pg.39]    [Pg.50]    [Pg.19]    [Pg.18]    [Pg.50]    [Pg.39]    [Pg.50]    [Pg.50]    [Pg.387]    [Pg.1255]    [Pg.65]    [Pg.18]    [Pg.750]    [Pg.762]    [Pg.299]    [Pg.294]    [Pg.592]    [Pg.155]    [Pg.543]    [Pg.299]   
See also in sourсe #XX -- [ Pg.3 ]



SEARCH



Flow Arrangement

Packed towers

Packed towers packing

Packing arrangements

Tower packings

© 2024 chempedia.info