% IMPORTANT: The following is UTF-8 encoded. This means that in the presence % of non-ASCII characters, it will not work with BibTeX 0.99 or older. % Instead, you should use an up-to-date BibTeX implementation like “bibtex8” or % “biber”. @PHDTHESIS{Deischter:849343, author = {Deischter, Jeff Gaston Jean}, othercontributors = {Palkovits, Regina and Rose, Marcus Sören}, title = {{G}ewinnung von biomassebasierten {V}erbindungen durch {A}dsorption an {A}ktivkohlen, {Z}eolithen und porösen {P}olymeren}, school = {RWTH Aachen University}, type = {Dissertation}, address = {Aachen}, publisher = {RWTH Aachen University}, reportid = {RWTH-2022-06740}, pages = {1 Online-Ressource : Illustrationen, Diagramme}, year = {2022}, note = {Veröffentlicht auf dem Publikationsserver der RWTH Aachen University; Dissertation, RWTH Aachen University, 2022}, abstract = {In this dissertation, the recovery of biobased products from aqueous phase by adsorption on commercial as well as tailored adsorbents was investigated. The understanding of structure-adsorption relationships could be extended by detailed studies of the adsorption of the products L-lysine, itaconic acid and D-glucose on activated carbons, covalent triazine-based frameworks (CTFs) and zeolites. This allows an establishment of adsorption-based separation processes for future biorefineries. In the first part of the work, a detailed insight into the liquid phase adsorption of L-lysine on activated carbons and its separation from D-glucose was given. Detailed characterization allowed the implementation of structure-adsorption relationships. By testing a variety of different commercial activated carbons, it was demonstrated that a large specific surface area in combination with a large amount of surface oxygen functionalities is required to achieve high L-lysine adsorption capacities of up to 256 mg g-1. A high amount of oxygen functionalities resulted in improved separation of L-lysine from lysine-glucose mixtures. The adsorption of L-lysine in a continuous fixed bed adsorber, a setup essential for an industrial application, was evaluated. In addition, up to 95 $\%$ of the adsorbed L-lysine could be desorbed by a suitable desorption strategy using water, ethanol or sulfuric acid. In the next chapter, CTFs, a material class that can be prepared via a variety of nitrile-based monomers, were investigated for itaconic acid, L-lysine and D-glucose adsorption applications. A number of different monomers were used to synthesize CTFs using ZnCl2 as solvent and catalyst. For itaconic acid/glucose mixtures, hydrophobic materials with a high C/N ratio showed the best adsorption performance, with itaconic acid capacities up to 400 mg g-1 and high separation efficiencies. For the lysine-glucose mixtures, high hydrophilicity proved to be beneficial to facilitate L-lysine separation. Overall, CTFs appear to combine the best of both worlds - polymer and carbonaceous material - and can serve as model systems for understanding N-based carbonaceous feedstocks. In the third chapter of this thesis, the selective adsorption of L-lysine from lysine-glucose mixtures was evaluated on various zeolites with different structural properties and Si/Al ratios. Zeolites can act as a molecular sieve and thus selectively adsorb or exclude compounds with specific molecular sizes. In the competitive adsorption of L-lysine and D-glucose, the effect of zeolites as a molecular sieve was highlighted. High separation factors could be achieved, due to the fact that D-glucose cannot enter the pore system of the zeolites because of its molecular size. In the last part of the work, the adsorption process was coupled with a bio-technological itaconic acid production process to investigate its suitability for in situ product re-covery. The in situ separation of itaconic acid prevented product inhibition, resulting in an in-crease of 11 $\%$ in the space-time yield of the bioprocess. In combination with highly selective product recovery, a promising downstream technology for future biorefinery processes can be achieved.}, cin = {155310 / 150000}, ddc = {540}, cid = {$I:(DE-82)155310_20140620$ / $I:(DE-82)150000_20140620$}, pnm = {TIB: BioSorp : Teilprojekt A; Das Potential von Adsorption zur energieeffizienten Stofftrennung in fermentativen Bioraffinerie-Prozessen (BMBF-031B0678A)}, pid = {G:(DE-82)BMBF-031B0678A}, typ = {PUB:(DE-HGF)11}, doi = {10.18154/RWTH-2022-06740}, url = {https://publications.rwth-aachen.de/record/849343}, }