The need to synthesize various enantiomers for preparative purposes poses a significant challenge for modern chem. engineering.The ability to rapidly prototype microfluidic devices, in which reaction-transport processes are significantly intensified, offers a potential solution to this problem.Our study aims to develop a functional modular microfluidic system capable of continuously producing an industrially significant enantiomer (R)-(+)-1-phenylethanol (R-PE) from racemic 1-phenylethyl acetate (PEAc).The system consists of a packed-bed reactor (PBR) with an immobilized lipase, which synthesizes R-PE, and a slug flow extractor (SFE), where the unreacted substrate is removed from the reaction solution using hexane.From the exptl. data, we determined the values of kinetic parameters for enzymic hydrolysis and found that R-PE competitively inhibits the reaction.In SFE, we examined the yields of 1-phenylethanol, and the separation efficiency for PEAc, and determined the values of the volumetric mass transfer coefficientThe obtained knowledge enabled us to operate the PBR and SFE in a series, with a total residence time of 260 s.The overall yield of R-PE in the modular system reached nearly 90 % under the chosen conditions.The reaction time of the enzymic process was shortened by up to 100 times compared to traditional batch reactors.The detailed knowledge about the kinetics of the enzymic reaction and the extraction process allowed for the harmonization of residence times in both devices, suggesting a pathway for quick production of optically active compounds with high yield.