Mass transfer estimation for bubble column scale up

2019 ◽  
Vol 205 ◽  
pp. 350-357 ◽  
Author(s):  
S.S. Deshpande ◽  
K. Kar ◽  
J. Pressler ◽  
I. Tebeka ◽  
B. Martins ◽  
...  
Keyword(s):  
1983 ◽  
Vol 48 (3) ◽  
pp. 703-710
Author(s):  
Milan Rylek ◽  
Karel Svoboda ◽  
Jindřich Zahradník

Absorption rates of CO2 into aqueous solutions of sodium hydroxide were measured in shallow-bed bubble columns with sieve trays as gas distributors. Experiments were carried out in two cylindrical columns (ID 0.15 and 0.30 m) and in a rectangular unit with square cross-section 1 m2. Liquid side mass transfer coefficients (kL) and specific interfacial area (a) were evaluated from experimental data of absorption rates. The effect of bubble-bed dimensions on mass transfer characteristics is discussed and recommendations for scale-up of bubble column reactors are presented.


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