Journal
BIOCHEMICAL ENGINEERING JOURNAL
Volume 34, Issue 3, Pages 273-278Publisher
ELSEVIER SCIENCE SA
DOI: 10.1016/j.bej.2006.12.013
Keywords
biodiesel fuel; methanolysis; packed-bed reactor; whole-cell biocatalyst; filamentous fungi; Rhizopus oryzae; biomass support particles; immobilized cells
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A packed-bed reactor (PBR) system using fungus whole-cell biocatalyst was developed for biodiesel fuel production by plant oil methanolysis. Lipase-producing Rhizopus oryzae cells were immobilized within 6 mm x 6 mm x 3 mm cuboidal polyurethane foam biomass support particles (BSPs) during batch cultivation in a 20-1 air-lift bioreactor. Emulsification of the reaction mixture containing soybean oils and water improved the methanolysis reaction rate. Using a high flow rate for the reaction mixture in the PBR caused exfoliation of the immobilized cells from the BSPs, while the inefficient mixing of the reaction mixture at low flow rates allowed the BSPs to be covered with a hydrophilic layer of high methanol concentration, leading to a significant decrease in lipase activity. A high methyl ester content of over 90% was achieved at a flow rate of 251/h in the first cycle of repeated batch methanolysis and a high value of around 80% was maintained even after the tenth cycle. Comparison with methanolysis reaction in a shaken bottle suggested that the PBR enhances repeated batch methanolysis by protecting immobilized cells from physical damage and excess amounts of methanol. The process presented here is therefore considered to be promising for industrial biodiesel-fuel production. (c) 2007 Elsevier B.V. All rights reserved.
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