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  • 1
    In: Discover Chemical Engineering, Springer Science and Business Media LLC, Vol. 3, No. 1 ( 2023-01-18)
    Abstract: Rhamnolipids are biosurfactants that tend to cause strong foaming, making microbial production in an aerated stirred tank fermenter challenging. The continuous removal of rhamnolipids from the cultivation broth via in situ liquid-liquid extraction can remedy this foam challenge, and thereby supports long-term cultivation and production. However, for efficient processing and stable phase separation, a specialized apparatus is required. In this study, the novel multiphase loop reactor, which is a modified airlift reactor with an internal loop enabling continuous in situ liquid-liquid extraction, was designed and adapted to produce rhamnolipids with a recombinant bacterium, Pseudomonas putida KT2440. The initially designed multiphase loop reactor showed a low oxygen transfer rate, unable to meet the oxygen demand of the whole-cell biocatalyst, resulting in inefficient growth and production. A re-design of the sparger via 3D printing enabled a high oxygen supply allowing rhamnolipid production at key performance indicators that matched stirred-tank reactor cultivations. Advantageously, the multiphase loop reactor allowed stable and constant phase separation and solvent removal enabling continuous cultivation in the future. Concluding, the successful use of the multiphase loop reactor for rhamnolipid synthesis is presented, highlighting its potential to become a new platform technology for intensified bioprocessing.
    Type of Medium: Online Resource
    ISSN: 2730-7700
    Language: English
    Publisher: Springer Science and Business Media LLC
    Publication Date: 2023
    detail.hit.zdb_id: 3048897-7
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  • 2
    Online Resource
    Online Resource
    Wiley ; 2023
    In:  Biotechnology and Bioengineering Vol. 120, No. 5 ( 2023-05), p. 1269-1287
    In: Biotechnology and Bioengineering, Wiley, Vol. 120, No. 5 ( 2023-05), p. 1269-1287
    Abstract: Bioreactors are the operative backbone, for example, for the production of biopharmaceuticals, biomaterials in tissue engineering, and sustainable substitutes for chemicals. Still, the Achilles' heel of bioreactors nowadays is the aeration which is based on intense stirring and gas sparging, yielding inherent drawbacks such as shear stress, foaming, and sterility concerns. We present the synergistic combination of simulations and experiments toward a membrane stirrer for the efficient bubble‐free aeration of bioreactors. A digital twin of the bioreactor with an integrated membrane‐module stirrer (MemStir) was developed with computational fluid dynamics (CFD) studies addressing the determination of fluid mixing, shear rates, and local oxygen concentration. Usability of the MemStir is shown in a foam‐free recombinant production process of biosurfactants (rhamnolipids) from glucose with different strains of Pseudomonas putida KT2440 in a 3‐L vessel and benchmarked against a regular aerated process. The MemStir delivered a maximal oxygen transfer rate (OTR max ) of 175 mmol L −1 h −1 in completely foam‐free cultivations. With a high space‐time yield (STY) of 118 mg RL L −1 h −1 during a fed‐batch fermentation, the effectiveness of the novel MemStir is demonstrated. Simulations show the generic value of the MemStir beyond biosurfactant production, for example, for animal cell cultivation.
    Type of Medium: Online Resource
    ISSN: 0006-3592 , 1097-0290
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2023
    detail.hit.zdb_id: 1480809-2
    detail.hit.zdb_id: 280318-5
    SSG: 12
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  • 3
    Online Resource
    Online Resource
    Wiley ; 2021
    In:  Biotechnology and Bioengineering Vol. 118, No. 9 ( 2021-09), p. 3545-3558
    In: Biotechnology and Bioengineering, Wiley, Vol. 118, No. 9 ( 2021-09), p. 3545-3558
    Abstract: The bioeconomy is a paramount pillar in the mitigation of greenhouse gas emissions and climate change. Still, the industrialization of bioprocesses is limited by economical and technical obstacles. The synthesis of biosurfactants as advanced substitutes for crude‐oil‐based surfactants is often restrained by excessive foaming. We present the synergistic combination of simulations and experiments towards a reactor design of a submerged membrane module for the efficient bubble‐free aeration of bioreactors. A digital twin of the combined bioreactor and membrane aeration module was created and the membrane arrangement was optimized in computational fluid dynamics studies with respect to fluid mixing. The optimized design was prototyped and tested in whole‐cell biocatalysis to produce rhamnolipid biosurfactants from sugars. Without any foam formation, the new design enables a considerable higher space–time yield compared to previous studies with membrane modules. The design approach of this study is of generic nature beyond rhamnolipid production.
    Type of Medium: Online Resource
    ISSN: 0006-3592 , 1097-0290
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2021
    detail.hit.zdb_id: 1480809-2
    detail.hit.zdb_id: 280318-5
    SSG: 12
    Location Call Number Limitation Availability
    BibTip Others were also interested in ...
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