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Bubble size distribution and interfacial areas of electrolyte solutions in bubble columns

✍ Scribed by Rüdiger Burckhart; Wolf-Dieter Deckwer

Publisher
Elsevier Science
Year
1975
Tongue
English
Weight
354 KB
Volume
30
Category
Article
ISSN
0009-2509

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✦ Synopsis

where values of R and U must be obtained from Fig. 2, or N,, v,V vertical gas velocity and its dimensionless form can be calculated during the integration of Eq. ( 8) A large range of W width of a square or rectangular column N was covered from 20 to 60 and all points lie between the two x,X horizontal distance and its dimensionless form curves shown on Fig. 4. for small values of D/H < 10, p gas density 351 H N NW P P'7 p* r,R u,u D2 N,, = 0.042 7i 0 NOTATION height of the gas entry position resistance of the packing in velocity heads resistance due to au entrance effect pressure atmospheric pressure pressure in the tower above the packing radius and a dimensionless radius horizontal gas velocity and its dimensionless form

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