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  • 1
    In: Chemical Engineering and Processing - Process Intensification, Elsevier BV, Vol. 189 ( 2023-07), p. 109407-
    Type of Medium: Online Resource
    ISSN: 0255-2701
    RVK:
    Language: English
    Publisher: Elsevier BV
    Publication Date: 2023
    detail.hit.zdb_id: 843648-4
    detail.hit.zdb_id: 2013149-5
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  • 2
    In: ELECTROPHORESIS, Wiley, Vol. 43, No. 13-14 ( 2022-07), p. 1387-1398
    Abstract: Megaporous adsorbents were prepared based on nonwoven polyethylene terephthalate (PET) fabrics and functionalized by covalent modification with polyvinylamine (PVAm) or monotriazinyl‐β‐cyclodextrin‐substituted polyvinylamine (PVAm‐MCT‐β‐CD). Mechanical properties of the resulting fabrics were maintained, as judged by tensile strength tests and scanning electron microscopy. Exceptional porosity (≥82%) and preserved hydrodynamic characteristics ( Pe  ≥ 63) indicated excellent structural stability when packed. The performance of the constructed adsorbents was evaluated with high molecular weight (proteins) and low molecular weight (dyes) model compounds. The static binding capacity (SBC) for bovine serum albumin (BSA) was 79.7 ± 1.3 and 92.9 ± 8.2 mg/g for PVAm‐modified and PVAm‐MCT‐β‐CD‐modified fabrics, respectively. The mentioned materials also adsorbed Orange II, an acidic dye (92.4 ± 2.6 and 101.9 ± 2.6 mg/g, respectively), indicating that the hydrophobicity was a prevailing binding mechanism operating at a pH close to isoelectric point. SBC for lysozyme and toluidine blue O (TBO, a basic dye) onto PVAm‐MCT‐β‐CD functionalized PET was 52.7 ± 5.1 and 73.3 ± 0.6 mg/g, respectively. TBOs have also shown some affinity for PVAm functionalized PET, but this was most likely to be mediated by hydrophobicity. On the other hand, operating at a superficial velocity of 90 cm/h, dynamic binding capacity for BSA was 11.4 ± 3.5 and 2.5 ± 0.6 mg/g indicating the importance of possible aggregation mechanisms during protein binding at equilibrium. Thus, PET‐based adsorbents require further functional improvement for chromatography applications. However, the easy‐to‐construct, scalable nonwoven adsorbents deserve further attention as a potential alternative to packed‐bed‐chromatography adsorbents.
    Type of Medium: Online Resource
    ISSN: 0173-0835 , 1522-2683
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2022
    detail.hit.zdb_id: 1475486-1
    SSG: 12
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  • 3
    Online Resource
    Online Resource
    Wiley ; 2023
    In:  Journal of Chemical Technology & Biotechnology Vol. 98, No. 4 ( 2023-04), p. 833-837
    In: Journal of Chemical Technology & Biotechnology, Wiley, Vol. 98, No. 4 ( 2023-04), p. 833-837
    Abstract: The Monod model has been widely used in activated sludge and biofilm models to mathematically describe the kinetics of microbial growth. Mathematical models of biological systems can be distinguished according to their dimensionality as zero‐dimensional (0D), one‐dimensional (1D), two‐dimensional (2D) and three‐dimensional (3D). The Monod model is a 0D model, which does not take cell (aggregate) structure into account, yet has been used in different ways in activated sludge and biofilm modelling: In activated sludge modelling, it is used in its original sense (i.e. 0D), whilst in dimensional biofilm modelling, it is used to model intrinsic kinetics in the biofilm and thus in 1D, 2D and 3D. We believe that the latter is not the correct use of the Monod model, because both activated sludge and biofilm systems consist of similar cell aggregates that both feature concentration gradients. Diffusional mass transfer limitations are manifested by the values of kinetic parameters in the Monod model and should not be described explicitly by Fick's laws of diffusion. The 0D concept has been adopted in state‐of‐the‐art activated sludge models and more recently in 0D biofilm models. Measured kinetic parameters can be directly transferred to 0D models. The application of Fick's second law of diffusion in combination with the Monod model (i.e. the reaction–diffusion equation) therefore becomes irrelevant. In this manner, the Monod equation becomes a simple, universal approach to modelling that contains variable parameters. © 2022 Society of Chemical Industry (SCI).
    Type of Medium: Online Resource
    ISSN: 0268-2575 , 1097-4660
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2023
    detail.hit.zdb_id: 1479465-2
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  • 4
    Online Resource
    Online Resource
    Wiley ; 2022
    In:  Journal of Chemical Technology & Biotechnology Vol. 97, No. 9 ( 2022-09), p. 2305-2316
    In: Journal of Chemical Technology & Biotechnology, Wiley, Vol. 97, No. 9 ( 2022-09), p. 2305-2316
    Abstract: The biological industry, but also biorefining platforms in the context of the circular economy, have been fertile terrains for the development of a palette of novel products of increasing structural diversity and fields of application. To mention only a few of the more complex bioproducts, we can consider monoclonal antibodies, plasmid DNA, virus‐like particles and exosomes. Of course, some products of industrial relevance are much simpler in nature. Irrespective of the product class and field of application, a shift from batch processing to continuous manufacturing is currently happening. This is due to the fact that operating in the continuous mode can result in process intensification, and therefore increased productivity with lower environmental impact can be realized. Some biological production schemes, e.g. those based on perfusion cultures, are well known in the pharmaceutical industry. Likewise, continuous fermentation is now utilized to produce ethanol from biomass. In many cases, continuous downstream operations are desired but difficult to implement; there is a pressing need to better understand the available options for product recovery and purification. Some traditional methods require re‐evaluation in modern contexts and some others, of experimental nature, require further improvement before actual implementation. In this article, we present an overview of the most promising methods that would allow for robust downstream bioprocessing options in the near future – with a focus on adsorption technologies. © 2021 The Authors. Journal of Chemical Technology and Biotechnology published by John Wiley & Sons Ltd on behalf of Society of Chemical Industry (SCI).
    Type of Medium: Online Resource
    ISSN: 0268-2575 , 1097-4660
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2022
    detail.hit.zdb_id: 1479465-2
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  • 5
    In: Catalysis Letters, Springer Science and Business Media LLC, Vol. 152, No. 7 ( 2022-07), p. 2033-2046
    Type of Medium: Online Resource
    ISSN: 1011-372X , 1572-879X
    RVK:
    Language: English
    Publisher: Springer Science and Business Media LLC
    Publication Date: 2022
    detail.hit.zdb_id: 1501518-X
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  • 6
    Online Resource
    Online Resource
    Wiley ; 2022
    In:  Journal of Food Science Vol. 87, No. 10 ( 2022-10), p. 4348-4362
    In: Journal of Food Science, Wiley, Vol. 87, No. 10 ( 2022-10), p. 4348-4362
    Abstract: Calf rennet has been traditionally used for cheese making all over the world since ancient times. It is primarily a type of aspartic protease. Calf rennet, also known as chymosin, is considered the best milk coagulant in cheese manufacturing. Its usage and demand are increasing day by day in the food industry; however, some ethical issues are also related since it is naturally present in the calf's stomach and obtained by the slaughtering of young animals. Therefore, researchers are trying to introduce some new and better alternatives for chymosin in the food industry. Mucor racemosus f. racemosus CBS 381, Mucor racemosus DSM 62760, and Aspergillus oryzae were cultivated by solid substrate fermentation using the design of experiment (DoE) (MODDE; Umetrics, Sweden) to optimize and analyze the various combinations of different factors and responses (milk‐clotting activity, proteolytic activity, specific activity). Based on the analysis of the screening and optimization results, Mucor racemosus CBS 381 was found to be the potential strain in terms of high production of aspartic protease, as well as had high milk‐clotting activity under a solid‐state fermentation system. However, molasses and casein were determined to be significant carbon and nitrogen sources, respectively, under conditions such as 70% moisture content and 25°C temperature. The molecular weight of the enzyme ( Mucor CBS 381) is ∼30 KDa and it exhibits maximum activity at pH 4.8 at 45°C. The investigated enzyme was pronounced as thermal‐sensitive and lost activity completely after 10 min incubation at 55°C. The remarkable qualities of the studied enzyme, such as cost‐effective production, milk‐clotting and proteolytic activity make Mucor racemosus CBS 381 a promising alternate to calf chymosin in the cheese‐making industry. Practical Application The milk‐clotting enzyme (aspartic protease) produced by the Mucor racemosus is the alternative to calf chymosin. It can be used to produce cheese on the industrial level with some desired properties such as good taste and texture that includes gumminess. Nowadays, consumers prefer products that do not involve any animal cruelty whereas a huge group of consumers oppose the use of genetically modified enzymes. Therefore, the enzyme by Mucor racemosus would produce the cheese that is going to meet the demands of various types of cheese consumers.
    Type of Medium: Online Resource
    ISSN: 0022-1147 , 1750-3841
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2022
    detail.hit.zdb_id: 2006705-7
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  • 7
    Online Resource
    Online Resource
    Springer Science and Business Media LLC ; 2020
    In:  Brazilian Journal of Microbiology Vol. 51, No. 2 ( 2020-06), p. 571-584
    In: Brazilian Journal of Microbiology, Springer Science and Business Media LLC, Vol. 51, No. 2 ( 2020-06), p. 571-584
    Type of Medium: Online Resource
    ISSN: 1517-8382 , 1678-4405
    Language: English
    Publisher: Springer Science and Business Media LLC
    Publication Date: 2020
    detail.hit.zdb_id: 2017175-4
    SSG: 12
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  • 8
    In: Frontiers in Bioengineering and Biotechnology, Frontiers Media SA, Vol. 11 ( 2023-6-1)
    Abstract: A continuous protein recovery and purification system based on the true moving bed concept is presented. A novel adsorbent material, in the form of an elastic and robust woven fabric, served as a moving belt following the general designs observed in known belt conveyors. The composite fibrous material that forms the said woven fabric showed high protein binding capacity, reaching a static binding capacity equal to 107.3 mg/g, as determined via isotherm experiments. Moreover, testing the same cation exchange fibrous material in a packed bed format resulted in excellent dynamic binding capacity values (54.5 mg/g) even when operating at high flow rates (480 cm/h). In a subsequent step, a benchtop prototype was designed, constructed, and tested. Results indicated that the moving belt system could recover a model protein (hen egg white lysozyme) with a productivity up to 0.5 mg/cm 2 /h. Likewise, a monoclonal antibody was directly recovered from unclarified CHO_K1 cell line culture with high purity, as judged by SDS-PAGE, high purification factor (5.8), and in a single step, confirming the suitability and selectivity of the purification procedure.
    Type of Medium: Online Resource
    ISSN: 2296-4185
    Language: Unknown
    Publisher: Frontiers Media SA
    Publication Date: 2023
    detail.hit.zdb_id: 2719493-0
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  • 9
    Online Resource
    Online Resource
    Wiley ; 2023
    In:  Journal of Chemical Technology & Biotechnology Vol. 98, No. 2 ( 2023-02), p. 369-380
    In: Journal of Chemical Technology & Biotechnology, Wiley, Vol. 98, No. 2 ( 2023-02), p. 369-380
    Abstract: Aerobic granular sludge (AGS) has emerged as a novel wastewater treatment technology and as a suppressing alternative to conventional activated sludge. The development of mathematical models of the AGS process, which can be used for wastewater treatment plant (WWTP) design and optimization, is therefore necessary to support successful implementation of AGS technology. This study aims to develop a zero‐dimensional (0D) AGS model that can be used in engineering practice for the above‐mentioned purposes. Results A laboratory AGS sequencing batch reactor (SBR), removing soluble organic substrate, nitrogen and phosphorus, was fed with artificial wastewater and modelled using a 0D approach. Model development was supported by bacterial characterization using 16S rRNA gene amplicon high‐throughput sequencing. The mathematical model was based on the activated sludge model no. 2d (ASM2d) and extended with both two‐step nitrification as implemented in the wastewater treatment plant simulator Sumo19 (Dynamita SARL) and ammonia nitrogen adsorption and desorption according to the Langmuir model. The variations of ammonia nitrogen, nitrite nitrogen, nitrate nitrogen, orthophosphate phosphorus and dissolved oxygen concentrations during one cycle of the SBR were successfully reproduced by the model (all Pearson's r values ≥0.93 and all r 2  ≥ 0.86). Conclusions The 0D modelling approach was proven to be applicable to AGS. It is possible that the 0D approach can fill the gap that has developed between engineering and research in the biofilm modelling community. The 0D modelling approach therefore merits further exploration using reactors fed with real wastewater, as well as on pilot and full‐scale WWTPs. © 2022 Society of Chemical Industry (SCI).
    Type of Medium: Online Resource
    ISSN: 0268-2575 , 1097-4660
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2023
    detail.hit.zdb_id: 1479465-2
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  • 10
    In: AMB Express, Springer Science and Business Media LLC, Vol. 8, No. 1 ( 2018-12)
    Type of Medium: Online Resource
    ISSN: 2191-0855
    Language: English
    Publisher: Springer Science and Business Media LLC
    Publication Date: 2018
    detail.hit.zdb_id: 2621432-5
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