Gas−Liquid Interfacial Area and Holdup in a Cocurrent Upflow Packed Bed Bubble Column Reactor at Elevated Pressures

1997 ◽  
Vol 36 (3) ◽  
pp. 622-631 ◽  
Author(s):  
E. J. Molga ◽  
K. R. Westerterp
1996 ◽  
Vol 35 (11) ◽  
pp. 3842-3847 ◽  
Author(s):  
D. Stegeman ◽  
P. A. Knop ◽  
A. J. G. Wijnands ◽  
K. R. Westerterp

2016 ◽  
Vol 299 ◽  
pp. 192-200 ◽  
Author(s):  
T. Geißler ◽  
A. Abánades ◽  
A. Heinzel ◽  
K. Mehravaran ◽  
G. Müller ◽  
...  

1999 ◽  
Vol 48 (1-4) ◽  
pp. 221-228 ◽  
Author(s):  
J.M. Winterbottom ◽  
Z. Khan ◽  
A.P. Boyes ◽  
S. Raymahasay

2017 ◽  
Vol 168 ◽  
pp. 403-413 ◽  
Author(s):  
Freddy Hernandez-Alvarado ◽  
Dinesh V. Kalaga ◽  
Damon Turney ◽  
Sanjoy Banerjee ◽  
Jyeshtharaj B. Joshi ◽  
...  

2013 ◽  
Vol 11 (1) ◽  
pp. 587-593 ◽  
Author(s):  
Antonio Blanco ◽  
Alicia García-Abuín ◽  
Diego Gómez-Díaz ◽  
Jose M. Navaza

Abstract This work analyses the influence of different experimental conditions over important hydrodynamic parameters of a bubble column reactor, such as bubble size distribution, gas hold-up and the gas–liquid interfacial area. The influence of gas flow-rate (18–40 L h–1) and reagent concentration (0–0.5 mol L–1) in the liquid phase upon these hydrodynamic parameters have been studied. The influence of experiment time must also be taken into account due to non-steady-state regime. Under these considerations, the chemical absorption rate changes throughout time, and it produces important changes upon the global absorption process, due to modifications in the gas–liquid interfacial area. The presence of a fast reaction in the liquid bulk has the highest influence upon interfacial area.


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