Article ID Journal Published Year Pages File Type
70860 Journal of Molecular Catalysis B: Enzymatic 2010 9 Pages PDF
Abstract

Free enzyme lipolase 100 T from Thermomyces lanuginosus has been investigated as a hydrolyzing catalyst in a spray extraction column. The aqueous buffer (pH 7.0) enzyme solution as continuous phase (batch-wise) and the oil as dispersed phase have been used. Various operating parameters which affect the drop size in a spray column, i.e. nozzle diameter, oil flow rate, etc. have been studied. Using the optimized flow rate and nozzle diameter, the effect of various other operating parameters such as concentration of enzyme, enzyme solution height (oil residence time) on the hydrolysis reaction has been evaluated. The highest conversion is obtained for the optimum flow rate of 3.8 ml/min and the nozzle diameter of 0.75 mm. The experimental result showed that the extent of hydrolysis of castor oil is 0.16% in a column reactor due to drop coalescing is almost equal to the hydrolysis due to drop residence time of 1 min in the column. It was also observed that the enzyme activity does not show any appreciable change up to a maximum of 44 passes in the spray column. The contributions of various hydrodynamic phenomena, such as drop formation, rise and coalesce of drops, to the overall hydrolysis rate have been estimated and discussed. Experimental data obtained for the spray column have been compared with that of an agitated batch reactor.

Graphical abstract. Optimized spray column operation is the key to enhanced enzymatic hydrolysis.Figure optionsDownload full-size imageDownload as PowerPoint slideResearch highlights▶ Optimum oil flow rate and nozzle diameter essential for enhancement in the hydrolysis yields. ▶ Coalescence of drops contributes significantly to oil hydrolysis in spray column. ▶ Enzyme deactivation can be avoided using low fluid shear in spray columns. ▶ Free enzyme gives marginally better efficacy as compared to conjugated enzyme.

Related Topics
Physical Sciences and Engineering Chemical Engineering Catalysis
Authors
, ,