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Effect of surfactants and biomass on the gas/liquid mass transfer in an aqueous‐silicone oil two‐phase partitioning bioreactor using Rhodococcus erythropolis T902.1 to remove VOCs from gaseous effluents
Author(s) -
Aldric JeanMarc,
Gillet Sébastien,
Delvigne Frank,
Blecker Christophe,
Lebeau Frédéric,
Wathelet JeanPaul,
Manigat Geralda,
Thonart Philippe
Publication year - 2009
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.2172
Subject(s) - mass transfer , chemistry , mass transfer coefficient , silicone oil , pulmonary surfactant , biomass (ecology) , bioreactor , chemical engineering , phase (matter) , bubble , aqueous two phase system , aqueous solution , chromatography , organic chemistry , biochemistry , oceanography , parallel computing , computer science , engineering , geology
BACKGROUND: The two‐phase partitioning bioreactor (TPPB) has become a new strategy for waste gas treatment. However, the impact of biomass and surfactants on gas/liquid (G/L) mass transfer needs to be better evaluated because the effects on the mass transfer coefficient K L and the interfacial area a , respectively, remains misunderstood. RESULTS: This study showed that, first, the surfactant extract produced by Rhodococcus erythropolis reduced the surface hydrophobicity of the biomass. Secondly, an optimal concentration appeared to exist for both components, respectively 0.5 g L −1 and 0.7 g L −1 for biomass (B) and surfactant extract (SE) when the global mass transfer coefficient ( K L a ) of oxygen was measured in a silicone oil/water TPPB. However, the combination of B and SE was found to induce a negative synergism. In particular, SE improved the interfacial area a by increasing the bubble diameter, while B reduced it as soon as a concentration of 1 g L −1 was exceeded. In contrast, the SE acted negatively on the K L , while B improved it overall. CONCLUSION: Better consideration is needed of the effect of biotic components in order to understand the phenomenon of G/L mass transfer in a TPPB. The behaviour of biomass growth and surfactants may strongly influence the mathematical models proposed in the literature. Copyright © 2009 Society of Chemical Industry