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@PHDTHESIS{Wachtmeister:573792,
      author       = {Wachtmeister, Jochen},
      othercontributors = {Rother, Dörte and Blank, Lars M.},
      title        = {{M}odularization and optimization of enzymatic reactions
                      applying whole cell biocatalysis in micro-aqueous solvent
                      systems},
      school       = {RWTH Aachen},
      type         = {Dissertation},
      address      = {Aachen},
      reportid     = {RWTH-2016-03741},
      pages        = {1 Online-Ressolurce (XI, 155 Seiten) : Illustrationen,
                      Diagramme},
      year         = {2016},
      note         = {Veröffentlicht auf dem Publikationsserver der RWTH Aachen
                      University; Dissertation, RWTH Aachen, 2016},
      abstract     = {Growing understanding of enzymatic reactions and their
                      utilization for synthetic purposes has led to a rising
                      interest in development of artificial, biocatalytic
                      multi-step reactions. These synthetic enzyme cascades
                      selectively convert inexpensive substrates into valuable
                      compounds of varying applications. Despite their many
                      advantages, the productivity of biocatalytic cascade
                      reactions is oftentimes considered unsatisfactory for
                      implementation into industrial scale processes. To overcome
                      this limitation and facilitate investigation, application,
                      optimization, and scale-up of biocatalytic cascade reactions
                      was the objective of this thesis. Representing a valuable
                      chiral building block for pharmaceutical synthesis,
                      1-phenylpropane-1,2-diol was chosen as a model product,
                      accessed by subsequent carboligation and oxidoreduction.In
                      order to increase the economic and ecologic relevance of the
                      model process and of synthetic enzyme cascades in general,
                      lyophilized whole cell catalyst was used in a micro-aqueous
                      solvent system. In doing so, a cheap and stable catalyst
                      formulation was employed, independent of costly external
                      cofactor addition. The cofactor, supplied by the whole cell
                      catalyst itself, was recycled by substrate-coupled
                      regeneration. Furthermore, the reaction in organic solvent
                      enabled outstandingly high substrate and product titers
                      together with facilitated downstream processing by
                      straightforward solvent evaporation.To enable an easy
                      cascade investigation and setup, the compartmentalized
                      entrapment or encapsulation of whole cell catalyst was
                      envisaged, allowing to serve as a catalytic module.
                      Therefore, whole cell catalyst was retained in a polymeric
                      membrane, resulting in a catalytic teabag. The catalytic
                      teabag was proven a useful modularization tool, enabling (i)
                      simplified and flexible handling and combination of
                      biocatalysts, (ii) straightforward catalyst recovery and
                      recycling, (iii) facilitated cascade optimization and
                      set-up, as well as (iv) small scale preparative production
                      of chiral compounds. In a second project part, the teabag
                      approach was demonstrated scalable up to 150 mL,
                      facilitating the gram-scale manufacturing of
                      (1R,2R)-1-phenylpropane-1,2-diol in a 1-pot 2-step cascade.
                      As suitable reaction vessel, not only novel reactor concepts
                      such as the SpinChem reactor (Nordic Chemquest AB) were
                      proven useful, but also ubiquitously available lab
                      equipment. In a third project part, the investigated
                      concepts were demonstrated transferable to two more
                      catalysts, now granting stereoselective access to all four
                      diastereoisomers of 1-phenylpropane-1,2-diol at industrially
                      relevant product concentrations. To achieve this goal, a
                      combination of reaction engineering and solvent engineering
                      was applied. By the implementation of “smart” diol
                      co-substrates up to 90 $mol\%$ of co-substrate could be
                      saved during oxidoreduction in two of the final cascades. At
                      the same time, product yield and space-time-yields obtained
                      met industrial benchmarks while outstandingly small amounts
                      of waste were generated.In summary, the investigation of
                      synthetic enzyme cascades was strongly facilitated by the
                      teabag approach. The developed module is quickly
                      manufactured and easily manageable, also by users
                      unexperienced in handling of biological systems and can even
                      be used for the preparative production of chiral compounds.
                      The combination of solvent and reaction engineering allowed
                      exceeding industrial threshold and thus illustrated the
                      potential of synthetic enzyme cascades even beyond the
                      investigatory scale.},
      cin          = {163930 / 160000 / 161700},
      ddc          = {570},
      cid          = {$I:(DE-82)163930_20160511$ / $I:(DE-82)160000_20140620$ /
                      $I:(DE-82)161700_20140620$},
      pnm          = {GRK 1166 - GRK 1166: Biokatalyse in unkonventionellen
                      Medien - Ionische Flüssigkeiten, organische Lösungsmittel,
                      überkritische Fluide und Gase als Reaktionsphasen für
                      biokatalysierte Synthesen (811503)},
      pid          = {G:(GEPRIS)811503},
      typ          = {PUB:(DE-HGF)11},
      urn          = {urn:nbn:de:hbz:82-rwth-2016-037410},
      url          = {https://publications.rwth-aachen.de/record/573792},
}