The Use of Fixed Bed Meander Microreactor in Enzymatic Glycerolysis Study

Authors

  • M. Drhová Institute of Chemical Process Fundamentals, Academy of Sciences of the Czech Republic, Prague
  • S. Šabata Institute of Chemical Process Fundamentals, Academy of Sciences of the Czech Republic, Prague
  • J. Sýkora Institute of Chemical Process Fundamentals, Academy of Sciences of the Czech Republic, Prague
  • J. Hetflejš Institute of Chemical Process Fundamentals, Academy of Sciences of the Czech Republic, Prague
  • J. Křišťál Institute of Chemical Process Fundamentals, Academy of Sciences of the Czech Republic, Prague
  • G. Kuncová Institute of Chemical Process Fundamentals, Academy of Sciences of the Czech Republic, Prague

Keywords:

enzymatic glycerolysis, flow meander and column reactor, stirred batch reactor, Novozyme 435, transesterification, soybean oil

Abstract

Transesterification of soybean oil (O) with glycerol (G), catalysed by Novozym 435, was studied in tert-butyl alcohol as solvent. The effects of reaction tempe­rature (40–50 °C), solvent concentration (20–35 vol.%), G/O molar ratio (1:1 – 2:1), and  residence time (min) on the oil phase composition (tri- (TAG), di- (DG) and monoacylglycerol) were evaluated. DAG formation was preferred at lower temperatures, lower G/S mole ratios, and at higher solvent concentrations. The data for G/S = 2:1 agreed well with those obtained in a continous fixed-bed column reactor. Glycerolyses of olive, sunflower, rapeseed, and linseed oils are also reported. Higher reaction rates of continous processes compared with batch glycero­lysis were observed.

Published

2014-11-15

How to Cite

Drhová, M., Šabata, S., Sýkora, J., Hetflejš, J., Křišťál, J., & Kuncová, G. (2014). The Use of Fixed Bed Meander Microreactor in Enzymatic Glycerolysis Study. Chemické Listy, 108(11), 1058–1066. Retrieved from http://ww.w.chemicke-listy.cz/ojs3/index.php/chemicke-listy/article/view/438

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Section

Articles