A membrane bioreactor was developed to perform an extractive bioconversion aimed at the production of isovaleraldehyde by isoamyl alcohol oxidation with whole cells of Gluconobacter oxydans. A liquid/liquid extractive system using isooctane as extractant and assisted by a hollow-fiber hydrophobic membrane was chosen to recover the product. The aqueous bioconversion phase and the organic phase were maintained apart with the aid of the membrane. The extraction of alcohol and aldehyde was evaluated by performing equilibrium and mass transfer kinetic studies. The bioprocess was then performed in a continuous mode with addition of the substrate to the aqueous phase. Fresh solvent was added to the organic phase and exhausted solvent was removed at the same flow rate. The extractive system enabled a fast and selective in situ removal of the aldehyde from the water to the organic phase. High conversions (72–90%) and overall productivity (2.0–3.0 g l−1 h−1) were obtained in continuous experiments performed with different rates of alcohol addition (1.5–3.5 g l−1 h−1). Cell deactivation was observed after 10–12 h of operation.

Continuous production of isovaleraldehyde through extractive bioconversion in a hollow-fiber membrane bioreactor / F. Molinari, F. Aragozzini, J.M.S. Cabral, D.M.F. Prazeres. - In: ENZYME AND MICROBIAL TECHNOLOGY. - ISSN 0141-0229. - 20:8(1997), pp. 604-611.

Continuous production of isovaleraldehyde through extractive bioconversion in a hollow-fiber membrane bioreactor

F. Molinari
Primo
;
1997

Abstract

A membrane bioreactor was developed to perform an extractive bioconversion aimed at the production of isovaleraldehyde by isoamyl alcohol oxidation with whole cells of Gluconobacter oxydans. A liquid/liquid extractive system using isooctane as extractant and assisted by a hollow-fiber hydrophobic membrane was chosen to recover the product. The aqueous bioconversion phase and the organic phase were maintained apart with the aid of the membrane. The extraction of alcohol and aldehyde was evaluated by performing equilibrium and mass transfer kinetic studies. The bioprocess was then performed in a continuous mode with addition of the substrate to the aqueous phase. Fresh solvent was added to the organic phase and exhausted solvent was removed at the same flow rate. The extractive system enabled a fast and selective in situ removal of the aldehyde from the water to the organic phase. High conversions (72–90%) and overall productivity (2.0–3.0 g l−1 h−1) were obtained in continuous experiments performed with different rates of alcohol addition (1.5–3.5 g l−1 h−1). Cell deactivation was observed after 10–12 h of operation.
Extractive bioconversion; Hollow fiber; Isovaleraldehyde; Membrane reactor; Microbial oxidation
Settore CHIM/11 - Chimica e Biotecnologia delle Fermentazioni
Settore CHIM/04 - Chimica Industriale
Settore AGR/16 - Microbiologia Agraria
Settore CHIM/10 - Chimica degli Alimenti
Settore AGR/15 - Scienze e Tecnologie Alimentari
1997
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/2434/166841
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