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Theoretical study on enzyme synthesis of cephalexin in a parallel-flow microreactor combined with electrically driven ATPS microextraction

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F20%3A43921137" target="_blank" >RIV/60461373:22340/20:43921137 - isvavai.cz</a>

  • Result on the web

    <a href="https://pubs.rsc.org/en/content/articlelanding/2020/RE/C9RE00482C#!divAbstract" target="_blank" >https://pubs.rsc.org/en/content/articlelanding/2020/RE/C9RE00482C#!divAbstract</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1039/c9re00482c" target="_blank" >10.1039/c9re00482c</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Theoretical study on enzyme synthesis of cephalexin in a parallel-flow microreactor combined with electrically driven ATPS microextraction

  • Original language description

    Cephalexin is an important beta-lactam antibiotic that is enzymatically synthetized from a nucleophile (7-aminodeacetoxycephalosporanic acid - 7-ADCA) and an acyl donor (phenylglycine methyl ester - PGME). The process is catalyzed by penicillin acylase. Cephalexin is thermodynamically unstable and is typically produced in a kinetic regime. Based on our previous experimental findings and additional batch experiments intended for the estimation of kinetic constants of cephalexin synthesis, we developed a mathematical model of a microfluidic device with two aqueous phases (ATPS) for the simultaneous cephalexin production and its separation from a reaction mixture. This device operates with free enzyme dissolved in one phase and the reactants introduced in the other phase. Because of small characteristic dimensions, the reactants are intensively transported through the interface to the enzyme phase where they are converted to cephalexin. The product then easily returns into the original phase due to a high value of the partition coefficient. The transport can be enhanced by an imposed electric field as the reaction compounds are charged. We studied the effects of four well-controllable parameters on the cephalexin yield: (i) the residence time of the phase introducing the reactants, (ii) the residence time of the phase containing the enzyme, (iii) the applied voltage difference across the interface, (iv) the characteristic dimension of microfluidic chambers. The mathematical model predicts that a cephalexin yield higher than 70% can be achieved in counter-current parallel flow arrangement, which is a result comparable with those obtained in batch experiments. The applied electric field can increase the cephalexin yield by no more than several percent because of the same polarity of 7-ADCA and cephalexin charge numbers. If compared to classical batch reactors, the suggested microreactor-microseparator brings the following benefits: (i) continuous cephalexin synthesis, (ii) effective and continuous separation of cephalexin due to proper partitioning of these species in the used ATPS, (iii) the use of free and highly active enzyme with efficient recyclation. Moreover, the productivity of the suggested microreactor is solely determined by the interfacial area that can be easily provided by thin separating membranes, i.e. no technically demanding numbering up solution is necessary.

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database

  • CEP classification

  • OECD FORD branch

    20402 - Chemical process engineering

Result continuities

  • Project

    <a href="/en/project/GA17-09914S" target="_blank" >GA17-09914S: Reaction-transport fundamentals in integrated microfluidic bioreactors-separators operating with aqueous two-phase systems</a><br>

  • Continuities

    P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Others

  • Publication year

    2020

  • Confidentiality

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Data specific for result type

  • Name of the periodical

    Reaction Chemistry &amp; Engineering

  • ISSN

    2058-9883

  • e-ISSN

  • Volume of the periodical

    5

  • Issue of the periodical within the volume

    3

  • Country of publishing house

    GB - UNITED KINGDOM

  • Number of pages

    14

  • Pages from-to

    570-583

  • UT code for WoS article

    000519210200010

  • EID of the result in the Scopus database

    2-s2.0-85081140247