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  • 1
    Electronic Resource
    Electronic Resource
    [s.l.] : Nature Publishing Group
    Nature 271 (1978), S. 568-570 
    ISSN: 1476-4687
    Source: Nature Archives 1869 - 2009
    Topics: Biology , Chemistry and Pharmacology , Medicine , Natural Sciences in General , Physics
    Notes: [Auszug] It is difficult to run quantities of whole cell protein sufficient to reveal the PBPs by fluorography in a reasonable time, without overloading the polyacrylamide gel. Because all the PBPs of B. megaterium are located in the membrane, it was possible to carry out the experiment by incubating intact ...
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  • 2
    Electronic Resource
    Electronic Resource
    [s.l.] : Nature Publishing Company
    Nature biotechnology 6 (1988), S. 721-725 
    ISSN: 1546-1696
    Source: Nature Archives 1869 - 2009
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: [Auszug] Cells of the organism Alcaligenes denitrificans were immobilised in Celite, particles of calcined diatomaceous earths. The kinetics of adsorption of non-growing cells was tested under varying conditions of cell concentration, salt concentration and pre-saturation of the beads with growth substrate. ...
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 45 (1996), S. 427-433 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract  Transformation of 1,2,3- and 1,2,4-trichlorobenzene in the presence of 20 mM sodium formate, by the methanotrophic bacterium Methylosinus trichosporium OB3b, was studied using cells grown in batch and continuous culture. Only 1,2,3-trichlorobenzene was transformed and transformation was strictly co-metabolic, only catalysed in the presence of the soluble form of methane monooxygenase. The kinetics of transformation could be described by simple first-order kinetics (0.00193 l min-1 g-1). Also the kinetics of transformation were found to be linearly proportional to cell density. No chloride ion release was observed during the reaction and the products of transformation (2,3,4- and 3,4,5-trichlorophenol) were identified by gas chromatography/mass spectroscopy and 1H-NMR and a 1.84:1 ratio of products in favour of para hydroxylation was observed. It was also observed that the relationship between mass of substrate transformed and cell density was linear giving a transformation capacity of 88.8±11.8 μmol g-1, after which the transformation of 1,2,3-trichlorobenzene was inhibited. This inhibition was not due to O2 limitation, co-substrate (CHOONa) limitation or product inhibition. Recovery and washing of the cells did not reverse this inhibition, indicating that inhibition was irreversible. During transformation a substantial decrease in the endogenous and formate-dependent O2 consumption rates was observed, although the methanol-dependent O2 consumption rate varied little between fresh cell samples and samples that had been used to transform 1,2,3-trichlorobenzene.
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 25 (1987), S. 453-458 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Alcaligenes denitrificans was isolated from sewage sludge and showed a strong degradative ability towards volatile fatty acids. The organism was tested both as free cells and immobilised in calcium alginate, for the ability to degrade the sodium salt of a typical volatile fatty acid, valeric acid. In shake flask culture the immobilised cells could be used to fully degrade 18 mM valerate over ten 48 h runs before bead break up occurred. The use of beads in conventional stirred tank fermenters, and a bubble column reactor was also investigated, with a 50 ml bubble column containing 5 ml of beads giving the highest overall degradation rate of 1.8 mmol/h, for 40 h in a fed batch mode of operation.
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  • 5
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 204-216 
    ISSN: 0006-3592
    Keywords: expanded bed adsorption ; bakers' yeast ; G6PDH ; STREAMLINE ion exchange adsorbents ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The use of expanded beds of STREAMLINE ion exchange adsorbents for the direct extraction of an intracellular enzyme glucose-6-phosphate dehydrogenase (G6PDH) from unclarified yeast cell homogenates has been investigated. It has been demonstrated that such crude feedstocks can be applied to the bed without prior clarification steps. The purification of G6PDH from an unclarified yeast homogenate was chosen as a model system containing the typical features of a direct extraction technique. Optimal conditions for the purification were determined in small scale, packed bed experiments conducted with clarified homogenates. Results from these experiments were used to develop a preparative scale separation of G6PDH in a STREAMLINE 50 EBA apparatus. The use of an on-line rotameter for measuring and controlling the height of the expanded bed when operated in highly turbid feedstocks was demonstrated. STREAMLINE DEAE has been shown to be successful in achieving isolation of G6PDH from an unclarified homogenate with a purification factor of 12 and yield of 98% in a single step process. This ion exchange adsorbent is readily cleaned using simple cleaning-in-place procedures without affecting either adsorption or the bed expansion properties of the adsorbent after many cycles of operation. The ability of combining clarification, capture, and purification in a single step will greatly simplify downstream processing flowsheets and reduce the costs of protein purification. © 1996 John Wiley & Sons, Inc.
    Additional Material: 3 Ill.
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  • 6
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 512-526 
    ISSN: 0006-3592
    Keywords: expanded bed adsorption ; ion exchange purification ; processing time ; productivity ; protein purification ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A strategy for the optimization of an expanded bed adsorption process has been developed by studying a model system involving the adsorption of lysozyme onto the adsorbent STREAMLINE SP. The hydrodynamic and adsorption properties of this ion exchange adsorbent in a variety of viscosities of feedstocks have been compared by analyzing bed expansion characteristics, liquid phase dispersion characteristics, equilibrium adsorption isotherms, and mass transfer characteristics. Additionally, the influences of the degree of bed expansion on adsorption performance have been investigated by frontal analysis. In these experiments, viscous feedstocks were simulated by the inclusion of glycerol in the adsorption buffers. Breakthrough curves for lysozyme were characterized and compared in terms of overall purification processing time and productivity. On the basis of these results, the relative productivities of different operating modes with the same process liquid were found to be almost the same. However, the processing time for each purification cycle decreased with increasing velocity of process liquid. It is demonstrated that an adsorption process carried out at a constant degree of bed expansion (twice its settled bed height, corresponding to bed voidage of 0.7) is more efficient, when characterized by the apparent dynamic binding capacity, than operation at a constant liquid velocity of 300 cm/h. These results have significant implications on the design and operation of the expanded bed adsorption procedures. The advantages and problems encountered in the use of expanded bed techniques for the direct extraction of proteins from unclarified feedstocks are also discussed. © 1996 John Wiley & Sons, Inc.
    Additional Material: 3 Ill.
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  • 7
    Publication Date: 1987-02-01
    Print ISSN: 0175-7598
    Electronic ISSN: 1432-0614
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Published by Springer
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  • 8
    Publication Date: 1996-04-23
    Print ISSN: 0175-7598
    Electronic ISSN: 1432-0614
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Published by Springer
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  • 9
    Publication Date: 1988-06-01
    Print ISSN: 0733-222X
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Published by Springer Nature
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  • 10
    Publication Date: 1978-02-01
    Print ISSN: 0028-0836
    Electronic ISSN: 1476-4687
    Topics: Biology , Chemistry and Pharmacology , Medicine , Natural Sciences in General , Physics
    Published by Springer Nature
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