Mathematical modeling of gas–liquid mass transfer rate in bubble columns operated in the heterogeneous regime

2005 ◽  
Vol 60 (22) ◽  
pp. 5937-5944 ◽  
Author(s):  
Benoıˆt Haut ◽  
Thierry Cartage
RSC Advances ◽  
2016 ◽  
Vol 6 (111) ◽  
pp. 109978-109982 ◽  
Author(s):  
Young-Kee Kim ◽  
Sung-Yeob Lee ◽  
Byung-Keun Oh

In an enzyme process using a gas substrate, the enhanced gas liquid mass transfer rate of the gas substrate by methyl-functionalized mesoporous nanoparticles could improve the productivity.


2017 ◽  
Vol 57 (11) ◽  
pp. 1902-1910 ◽  
Author(s):  
Takahiro Okuno ◽  
Md. Azhar Uddin ◽  
Yoshiei Kato ◽  
Sang Beom Lee ◽  
Yong Hwan Kim

2007 ◽  
Vol 13 (3) ◽  
pp. 167-168 ◽  
Author(s):  
Aleksandar Dudukovic ◽  
Rada Pjanovic

The scope of this paper is to explain effect of eddy viscosity and turbulent Schmidt number on mass transfer rate. New, theoretically based correlation for gas-liquid mass transfer coefficients are proposed.


AIChE Journal ◽  
2009 ◽  
pp. NA-NA ◽  
Author(s):  
Vinit P. Chilekar ◽  
John van der Schaaf ◽  
Ben F. M. Kuster ◽  
Johan T. Tinge ◽  
Jaap C. Schouten

2012 ◽  
Vol 66 (9) ◽  
pp. 1914-1922 ◽  
Author(s):  
Takuro Kobayashi ◽  
Kai-Qin Xu ◽  
Yu-You Li ◽  
Yuhei Inamori

Biological desulfurization using a bubble column reactor was investigated in a continuous biogas treatment. Rapid biogas circulation between the digester and the bubble column for biological desulfurization was used to stimulate the gas–liquid mass transfer of H2S. A positive correlation between the biogas circulation rate and H2S removal rate was observed. Moreover, the increase in the circulation rate stimulated the O2 mass transfer, eventually translating into an increase in sulfate production from the oxidation of H2S. Throughout the continuous experiment, the reactor retained sufficient levels of sulfide-oxidizing bacteria. A comparison of the results of the continuous biogas treatment and batch tests suggests that the gas–liquid mass transfer rate of H2S was the rate-limiting step in the biological desulfurization in the reactor, indicating that the mass transfer efficiency of H2S needs to be improved to enhance the desulfurization performance.


1984 ◽  
Vol 17 (5) ◽  
pp. 547-549 ◽  
Author(s):  
KOZO KOIDE ◽  
KAZUYOSHI HORIBE ◽  
HISATSUGU KITAGUCHI ◽  
NORIAKI SUZUKI

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