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  • 1
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The production of lankacidin-group antibiotics was markedly stimulated by adding β-cyclodextrin (β-CyD) to the fermentation medium. This stimulatory effect was observed for all Streptomyces species known to produce lankacidins. β-CyD had no marked effect on microbial growth, consumption rate of carbon source and pH changes throughout fermentation. β-CyD was not consumed by the microorganism during fermentation, and the lankacidins produced existed as inclusion complexes in the culture filtrate. Comparing α-CyD, β-CyD and γ-CyD, β-CyD was the most effective when it was added at the onset of fermentation. From the results of experiments on the replacement culture and the incorporation of a 14C-labelled precursor to the lankacidins, it was confirmed that the cells grown in the presence of β-CyD had a potent productivity of lankacidins.
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 32 (1990), S. 556-559 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Gel-filtration analysis of a mixture of cyclodextrin (CyD) and lankacidin C showed that β-CyD had strong, γ-CyD weak and α-CyD no affinity for lankacidin C. Lankacidin C production activity, which was assayed by measuring the incorporation of l-[methyl-14C-]methionine into the lankacidin molecule, was the greatest with cells grown in the presence of β-CyD, less with γ-CyD and the least with α-CyD. Lankamycin and T-2636M, which are by-products in lankacidin C fermentation, were not included by β-CyD and their production was not stimulated by β-CyD. It was apparent that the stimulatory effect of CyD was closely related to the formation of an inclusion complex between CyD and the antibiotic. Lankacidin C biosynthesis was repressed by preincubating cells with lankacidin C, while the repressive effect of lankacidin C was abrogated by the inclusion by β-CyD. Thus, abrogation of feed-back repression seems to be a main mechanism of the effect of CyD. However, α-CyD, which had no affinity for lankacidin C, stimulated the production to the least extent and exhibited a complementary effect on the stimulation by β-CyD or γ-CyD. α-CyD also caused a change in cell morphology and cell-surface hydrophobicity. It was assumed that the modification of the cell surface is a secondary mechanism of the effect of CyD.
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 25 (1986), S. 132-136 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Aminopterin (10 μg/ml) was found to inhibit the formation of 5-hydroxymethylcytosine (HMC), a constituent of mildiomycin, without affecting the growth ofStreptoverticillium rimofaciens. This was available for selecting high-producing mutants.d-Cycloserine caused its morphological mutations at high frequency. In addition, mildiomycin (MIL) production varied widely among the strains picked up from colonies that developed on agar medium containing cycloserine at the inhibitory concentration to the growth. Consequently, we selected the mutants which were capable of producing MIL on agar medium containing 10 μg/ml of aminopterin, among mutants enriched by cycloserine. A high-producing mutant thus obtained, C R 4 -257, exhibited higher enzymatic activity of the HMC formation and higher resistance todl-serine hydroxamate than the original strain.l-Canavanine resistant mutants were furthermore selected to enhance the biosynthetic activity of the arginine-like moiety of MIL. Among them, we finally obtained an excellent mutant, CVR-48, with an MIL production 2.6 times that of the original strain,S. rimofaciens B-98891.
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 25 (1986), S. 132-136 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Aminopterin (10 μg/ml) was found to inhibit the formation of 5-hydroxymethylcytosine (HMC), a constituent of mildiomycin, without affecting the growth ofStreptoverticillium rimofaciens. This was available for selecting high-producing mutants.d-Cycloserine caused its morphological mutations at high frequency. In addition, mildiomycin (MIL) production varied widely among the strains picked up from colonies that developed on agar medium containing cycloserine at the inhibitory concentration to the growth. Consequently, we selected the mutants which were capable of producing MIL on agar medium containing 10 μg/ml of aminopterin, among mutants enriched by cycloserine. A high-producing mutant thus obtained, C R 4 -257, exhibited higher enzymatic activity of the HMC formation and higher resistance todl-serine hydroxamate than the original strain.l-Canavanine resistant mutants were furthermore selected to enhance the biosynthetic activity of the arginine-like moiety of MIL. Among them, we finally obtained an excellent mutant, CVR-48, with an MIL production 2.6 times that of the original strain,S. rimofaciens B-98891.
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  • 5
    ISSN: 1573-0778
    Keywords: cell-line improvement ; human-human hybridoma ; human monoclonal antibodies ; mouse-human-human heterohybridoma ; perfusion culture ; serum-free medium
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Two hybridoma systems, mouse·human-human (m·h-h) heterohybridoma and human-human (h-h) hybridoma, have been established, and hybridomas secreting anti-tetanus toxoid and anti-HBsAg human monoclonal antibodies (MoAbs), both having a neutralizing activity have been obtained. Cell-line improvement was shown to be an efficient method for improving the productivity in a cell culture process. Two kinds of serum-free media, GFS (a serum substitute)-containing media and polyethylene glycol (PEG)-containing media, have been established to produce human MoAbs. m·h-h Heterohybridomas could be cultivated for a long period by perfusion culture in an agitation vessel, but h-h hybridomas could not. We found that h-h hybridomas show growth-associated antibody production kinetics and established two kinds of long-term cultivation systems: continuous perfusion culture and semicontinuous immobilized perfusion culture. We also scaled up batch culture and short-term perfusion culture to 200-L and 50-L fermentors, respectively. Processes for large-scale purification from the culture supernatants of both GFS- and PEG-containing serum-free media have also been developed.
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  • 6
    ISSN: 1573-0778
    Keywords: cell improvement ; FGF ; hepatitis B virus ; human-human hybridoma ; monoclonal antibody ; proliferative activity
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Highly purified recombiaant basic fibroblast growth factor (rbFGF) and acidic FGF (aFGF) stimulated the proliferation of human-human (h-h) hybridomas to the extent of over four-fold from a low cell density such as 1×103 cells per ml in a serum-free medium in 24-well plates. The stimulatory effect of rbFGF was also observed in various lymphoid cell lines. Expecting that FGF could be an autocrine growth factor, we introduced bFGF gene into a h-h hybridoma using an expression plasmid induced by dexamethasone. The transformed cells thus obtained, HPO-75.11bbFGF-7, were able to grow well from a low inoculum density in a serum-free medium and antibody production was also increased when bFGF gene expression was induced. The transformed cells could grow at clonal density in a serum-free medium in 96-well plates, though the original cells could not. We also obtained a more practical transfectant, HPO-75.29-H74, using a high-shear stress adapted clone as the recipient and an expression plasmid having bFGF gene under the control of metallothioneine-I promoter. The HOP-75.29-H74 cells were capable of growing and producing human monoclonal antibody against hepatitis B virus surface antigen from an inoculum density of 1×103 cells per ml in an agitation vessel without addition of an inducer.
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  • 7
    ISSN: 1573-0778
    Keywords: growth-associated production ; hepatitis B virus ; human-human hybridoma ; immobilized culture ; monoclonal antibody ; perfusion culture
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Human-human hybridomas which secrete a human monoclonal antibody (h-MoAb) against hepatitis B virus surface antigen showed growth associated production kinetics. The rate of h-MoAb production rapidly decreased after cell growth was arrested in a perfusion culture, even if the perfusion rate was increased. A continuous suspended-perfusion culture, in which both culture broth and culture supernatant are continuously harvested and the same volume of fresh medium is continuously fed into the reactor, was developed to maintain continuous growing conditions during cultivation. In this culture system, the production of h-MoAb continued for more than 50 days with an average productivity of 5.0 mg/l of working volume/day. A semicontinuous immobilized-perfusion culture in which parts of the cells are repeatedly removed from the immobilized reactor was another useful technique for the long term cultivation of these h-h hybridomas. As an average h-MoAb production rate, 62 mg/l of immobilized-bed volume/day was achieved for 65 days of cultivation using a ceramic matrix reactor, and 327 mg/l/day was achieved over 47 days of cultivation using a hollow fiber reactor equipped with Cultureflo MTM Thus, the antibody productivity per reactor volume per day by the semicontinuous immobilized-perfusion culture was much higher than that of the continuous perfusion culture in an agitation reactor.
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  • 8
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 25 (1983), S. 2735-2755 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The cultural properties of an obligate methanol utilizer, Methylomonas methanolovorans, were investigated in batch and continuous cultures, and the problems of mass-energy balances were examined. Among the culture data, an exponential increase of growth lag with increased methanol concentration, as well as the inhibition kinetics in the relation between attainable maximum specific growth rate (μm ≦ 0.52) and methanol concentration are of interest. In the latter case, the inhibition constant (Ki) and the index number were 40 g/L, and 3 (dimensionless), respectively. The maximum yield coefficient (Y) in both batch and chemostat cultures was around 0.52. An analysis of the behavior of respiratory activity (Qo2) in response to the dissolved oxygen concentration (DO) indicated that the oxygen-terminal entity should be regarded as a single one with a saturation constant for DO of 32 μg/L (1.1 × 10-6M). Chemostat data showed that the saturation constant for methanol is as low as 2.2 mg/L or 7 × 10minus;5M. A linear relationship was observed between the respiratory activity (mol O2g-1h-1) and the specific growth rate (μ i h-1), with the relationship Qo2 = 0.0504μ + 0.00112. The theory of mass and energy balances used by Roels has been reformed to give useful relationships between RQ or the cell yield and μ. In the case of M. methanolovorans, the relations can be greatly simplified since the influence of metabolic by-product formation was negligible. Experimental RQ values (theoretical values for Y = 0.52 and 0.445) at varying μ-values were compared with theoretical ones; despite considerable fluctuations, the results were regarded to conform with theory. By use of mass balance equations and enthalpy data of known compounds, the heat evolution in methanol fermentation was estimated indirectly to be 612 kcal/100 g biomass formed. The YATP problems are also discussed.
    Additional Material: 13 Ill.
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  • 9
    Publication Date: 1990-02-01
    Print ISSN: 0175-7598
    Electronic ISSN: 1432-0614
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Published by Springer
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  • 10
    Publication Date: 1986-11-01
    Print ISSN: 0175-7598
    Electronic ISSN: 1432-0614
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Published by Springer
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