Development of a two separate phase submerged biocatalytic membrane reactor for the production of fatty acids and glycerol from residual vegetable oil streams

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• 作者：S. Chakraborty^a ; ^b ; ^{sudip@unical.it} ; ^{zsudip.c@gmail.com} ; E. Drioli^a ; ^b ; L. Giorno^a
• 关键词：Submerged biocatalytic membrane ; Waste biomass ; Immobilized enzyme ; Waste valorization ; Fried oil ; Valuable compounds production
• 刊名：Biomass and Bioenergy
• 出版年：2012
• 出版时间：November, 2012
• 年：2012
• 卷：46
• 期：Complete
• 页码：574-583
• 全文大小：1339 K

文摘

Enzymatic membrane bioreactors (MBR) have been studied for very different applications since many years. Submerged MBR has also been successfully used for treatment of wastewater. In the existing submerged configuration, the membrane works as the separation unit operation while the bioconversion is carried out by microorganisms suspended in the tank reactor. In the present work, a novel approach that combines the concept of biocatalytic membranes and submerged modules is proposed for the treatment of biomass. Lipase enzyme from Candida rugosa has been immobilized in polyethersulphone hollow fiber (PES HF) membrane in order to develop a two separate phase biocatalytic submerged membrane reactor in which the membrane works as both catalytic and separation unit. Furthermore, the submerged biocatalytic membrane reactor is intended for production of valuable components from waste biomass, and different physical, chemical and fluid dynamics has been optimized. Response surface methodology (RSM) has been used to model the operating parameters and Box-Behnken method has been applied to maximize the fatty acids production and optimization. At TMP 80?¡À?2?kPa, pH 7.40?¡À?0.1, temperature 35?¡À?0.5?¡ãC with an axial velocity of 0.07?¡À?0.01?ms^?1 and organic stirring 89.01?rad?s^?1 the system showed the global examined value within the experimental scope. The proof of principle using fried cooked oils has been performed in later period.