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  • 1
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    FEMS microbiology letters 195 (2001), S. 0 
    ISSN: 1574-6968
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Biology
    Notes: Levan fructotransferase (LFTase) from Arthrobacter ureafaciens K2032 was expressed with N-terminal fusion of a LacZ-derived secretion motif (TMITNSSSVP) using the lac promoter system in recombinant Escherichia coli JM109 [pUDF-A81]. In flask cultures, recombinant enzyme activity was detected in culture media, and sequence analysis of N-terminal residues showed that about 40% of the extracellular recombinant LFTase had an authentic N-terminus. In a fed-batch bioreactor containing recombinant E. coli at high cell concentrations (OD600〉200), the extracellular LFTase accumulated to 46 000 U ml−1 (∼2.0 g l−1) which was almost 40% of total (intra- and extracellular) recombinant LFTase. The synthesized recombinant enzyme was secreted soon after gene expression was induced by IPTG. Prolonged high secretion caused cell lysis and growth inhibition during the production phase in fed-batch cultures. When lactose was added by continuous feed mode, the secretion of recombinant LFTase and hence the cell lysis were significantly delayed in spite of the increased synthesis level. Therefore the induced cell culture of recombinant E. coli could grow up to a much higher cell concentration with continuing recombinant enzyme synthesis. In the case of the controlled feed of lactose, the maximum activities (U ml−1) of total and extracellular LFTase were nearly 100% and 70% higher, respectively.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    FEMS microbiology letters 179 (1999), S. 0 
    ISSN: 1574-6968
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Biology
    Notes: In fed-batch cultures of recombinant Escherichia coli BL21(DE3)[pT7-G3IL2] at high cell concentration, the post-induction specific growth rate was carefully regulated by controlled medium feed to maximize the synthesis level of recombinant fusion interleukin-2, G3·IL-2. A maximum concentration of G3·IL-2 (11.25 g l−1) was achieved in the induced recombinant culture growing at the rate of 0.056 h−1. A steep decrease in the expression level of G3·IL-2 was observed at the post-induction specific growth rates higher than its optimal value (0.056 h−1). In the induced recombinant cultures, plasmid multimerization was observed and highly dependent on specific growth and production rate: a higher post-induction specific growth rate and an increased specific production rate tended to significantly promote it much further. Moreover, plasmid stability was found to decrease rapidly in a faster growing culture.
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology techniques 10 (1996), S. 679-682 
    ISSN: 1573-6784
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary A recombinant E. coli BL21[pET3a-T2M2] was cultivated in fed-batch cultures and cell mass increased to more than 70g/L. The volumetric oxygen transfer coefficient was estimated in a range of various fermentation parameters (agitation speed, oxygen flow rate and cell mass concentration) and finally the oxygen transfer correlation in bioreactor containing the recombinant E. coli cultures was determined as: kspla = 0.0195 (Pg/V)0.55 (Vs)0.64 (1+2.12X+0.20X2)−0.25.
    Type of Medium: Electronic Resource
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology letters 20 (1998), S. 295-299 
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract A bioreactor system equipped with a hollow fiber cross-filtration module was used for continuous cultivation of Lactobacillus acidophilus at high cell concentrations. The growth rate did not correlate with the lactate concentration if the residual glucose concentration was kept nearly zero in the culture broth. To achieve this, an effective control method of medium feed rate was developed on the basis of the correlation between the specific glucose consumption rate (nu) and the specific cell growth rate (mu), i.e. nu = 52.90 mu + 0.39. Growth up to 50 g dry wt l-1 was achieved without glucose accumulation under the total cell recycle. Via the partial cell recycle, continuous biomass production was achieved with a steady-state L. acidophilus concentration and dilution rate being 40 gl-1 and 0.09 h-1. © Rapid Science Ltd. 1998
    Type of Medium: Electronic Resource
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  • 5
    ISSN: 1573-6776
    Keywords: Escherichia coli ; interleukin-2 ; lactose ; symport
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Using lactose as an inducer, recombinant human interleukin-2 (rhIL-2) was synthesized with an N-terminus fusion partner, G3 (three tandem-arranged glucagon peptides) in fed-batch cultures at high cell concentration (60–90 g l−1) of Escherichia coli BL21(DE3) [pT7-G3IL2]. With batch additions of lactose (4 × 13.5 g), the fusion rhIL-2 was synthesized up to 9.3 g l−1. However, if all the lactose (54 g) was added at once to the culture, synthesized fusion rhIL-2 decreased to 5.4 g l−1 with a decreased cell growth rate. A statistical optimization of the production medium containing glucose, yeast extract, and lactose led to fusion rhIL-2 being produced at 〉 9 g l−1.
    Type of Medium: Electronic Resource
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  • 6
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology techniques 10 (1996), S. 419-424 
    ISSN: 1573-6784
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Pancreatic enzymes were recovered with enhanced activity by a newly designed extraction process. The protease activity was increased to the extent of 65% by using MES buffer, 64mM and duodenum enzyme extracts containing enterokinase at autolysis stage. The decrease in amylase activity due presumably to proteolytic degradation was effectively prevented by treating the enzyme solution with calcium prior to the autolysis.
    Type of Medium: Electronic Resource
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  • 7
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology letters 18 (1996), S. 903-908 
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The steady-state concentration of M. trichosporium OB3b increased about two-fold in the continuous culture when the feeding medium was supplemented by ferrous sulphate (50mg/L) and citric acid (100mg/L) at a steady state. In batch and continuous cultures, the cell growth was significantly inhibited by excess N-sources (NH4OH, NH4Cl, NH4NO3, HNO3, and NaNO3) and ammonium N-sources were more inhibitory. Both volumetric O2 transfer coefficient and specific O2 uptake rate increased monotonously in an extensive range of air flow rate (0.1–7 vvm) and the methane interfered with the O2 transfer even at very low flow rates (0.01–0.1 vvm).
    Type of Medium: Electronic Resource
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  • 8
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology letters 19 (1997), S. 655-659 
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The recombinant human granulocyte-colony-stimulating factor (rhG-CSF) was synthesized in a fusion protein using a GAL1-10 UAS in recombinant Saccharomyces cerevisiae and the intracellular KEX2 cleavage led excretion of mature rhG-CSF into the extracellular culture broth. The recombinant yeast growth in fed-batch cultures was controlled by precise computer-aided medium feed. The optimal C/N ratio in preinduction (glucose/Casamino acids) and post-induction (galactose/yeast extract) feed media was determined at 3 and 2, respectively. The final rhG-CSF and cell concentration was more than 60 mg/L and 70 g/L, respectively, with around 90% plasmid stability and negligible ethanol accumulation. Comparing the cell growth between the hG-CSF + and hG-CSF - recombinant strains shows that the cloned gene product does not hamper the host cell growth.
    Type of Medium: Electronic Resource
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  • 9
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Using cell recycle, the concentration of M. trichosporium OB3b was increased to more than 12g/L in continuous culture and biomass productivity was enhanced up to 0.708g/L/h. The optimal temperature and pH for soluble MMO activity were 35°C and 6.2–6.4. The Optimal concentrations of methanol and sodium formate, as cofactor regenerators, were 0.5mM and 10 mM, respectively, at which the soluble MMO activity was about 8 times enhanced.
    Type of Medium: Electronic Resource
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  • 10
    ISSN: 0006-3592
    Keywords: rhG-CSF ; fusion protein ; secretion efficiency ; glycosylation ; multimer ; conformation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The synthesis and secretion of recombinant human granulocyte colony-stimulating factor (rhG-CSF) are investigated in fed-batch cultures at high cell concentration of recombinant Saccharomyces cerevisiae, and some important characteristics of the secreted rhG-CSF are demonstrated. Transcription of the recombinant gene is regulated by a GAL1-10 upstream activating sequence (UASG), and the rhG-CSF is expressed in a hybrid fusion protein consisting of signal sequence of Kluyveromyces lactis killer toxin and N-terminal 24 amino acids of human interleukin 1β. The intracellular KEX2 cleavage leads to excretion of mature rhG-CSF into extracellular culture broth, and the cleavage process seems to be highly efficient. In spite of relatively low copy number the plasmid propagation is stably maintained even at nonselective culture conditions. The rhG-CSF synthesis does not depend on galactose level, whereas the production of extracellular rhG-CSF was significantly enhanced by increasing the inducer concentration above a certain level and also by supplementing the nonionic surfactant to the culture medium, which is notably due to the enhanced secretion efficiency. Various immunoblotting analyses demonstrate that none of the rhG-CSF is accumulated in the cell wall fraction and that a significant amount of intracellular rhG-CSF antibody-specific immunoreactive proteins is located in the ER. A core N-glycosylation at fused IL-1β fragment is likely to play a critical role in directing the high-level secretion of rhG-CSF, and the O-glycosylation of secreted rhG-CSF seems nearly negligible. Also the extracellular rhG-CSF is observed to exist as various multimers, and the nature of molecular interaction is evidently not the covalent disulfide bridges. The CD spectra of purified rhG-CSF and Escherichia coli-derived standard show that the conformations of both are similar and are almost identical to that reported for natural hG-CSF. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 600-609, 1998.
    Additional Material: 8 Ill.
    Type of Medium: Electronic Resource
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