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  • 1985-1989  (16)
  • 1
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 469 (1986), S. 0 
    ISSN: 1749-6632
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Natural Sciences in General
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 542 (1988), S. 0 
    ISSN: 1749-6632
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Natural Sciences in General
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 501 (1987), S. 0 
    ISSN: 1749-6632
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Natural Sciences in General
    Type of Medium: Electronic Resource
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  • 4
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The repeated batch and continuous operations for transphosphatidylation reaction were carried out for phosphatidylglycerol (PG) synthesis from phosphatidylcholine (PC) with the help of immobilized cabbage phospholipase D (PLD) in the presence of glycerol. The biphasic reaction system was used which included the aqueous phase containing immobilized PLD along with high concentrations of glycerol (30%–50%) and buffer, whereas the main part of substrate (PC) and products (mainly PG) formed were in the organic phase (diethyl ether). Octyl-Sepharose CL-4B having a hydrophobic octyl group was chosen for the PLD immobilization. Both immobilization yield and activity yield of immobilized enzyme were 100%. The effects of solvents, temperature and glycerol concentrations on the immobilized PLD were examined. Repeated batch conversion of PC (15 g/l) to PG was examined with the immobilized PLD in 30% glycerol. In all five batch cycles examined, 100% selectivity was obtained and there was no significant decrease in the fractional conversion of PC to PG (98%–99%) in the first three batch cycles. In the cases of a packed-bed reactor (PBR) and a continuous stirred-tank reactor (CSTR) used for continuous synthesis of PG with the immobilized PLD, the operational stabilities of the immobilized enzyme were almost the same (half life=14 h at 30°C) when purified PC was used, while in the case of partially purified PC in CSTR the half life increased more than five times.
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 25 (1987), S. 526-531 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary High concentration production of an antibiotic, thiostrepton, was achieved by the fed-batch culture of Streptomyces laurentii. To produce thiostrepton efficiently, the pH of the medium had to be maintained in a very narrow range between 6.0 and 6.2. As the substrates, not only glucose but also natural nutrients such as defatted soy bean meal and corn steep liquor were demanded. All of these substrates (multi-substrate) had to be supplied during the cultivation. pH was used as the indicator to detect the deficiency of substrates. When the glucose in the medium had been exhaustively consumed, the pH increased immediately; the multi-substrate solution (MS-solution) was then supplied. The composition of the feeding solution was determined from data obtained in batch cultures. During the fed-batch culture, glucose concentration was kept lower than 5 g/l by regulating the feed amount of MS-solution with this pH-stat modal control. By this control strategy a high concentration of thiostrepton, 10.5 g/l, was obtained, while total cell mass concentration reached 157 g/l. The productivity of thiostrepton was greatly increased compared with the conventional batch culture.
    Type of Medium: Electronic Resource
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  • 6
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary An automatic feeding system to supply olive oil in semi-batch culture was established by monitoring cell concentration with a laser turbidimeter combined with a microcomputer and a pulse motor. In this automatic feeding system, specific olive oil supply rate (g olive oil) · (g dry cell)-1 · h-1, q 0, was changed in an appropriate range. Attempts were made to produce lipase by a turbidity-dependent automatic fed-batch culture of Pseudomonas fluorescens. It was found from the semi-batch cultures with turbidity-dependent feeding of olive oil and with varied initial Fe ion concentrations that excess Fe ion was inhibitory to formation of the lipase. Turbidity-dependent automatic simultaneous feeding of olive oil and Fe ion was performed to obtain semi-deficiencies of both the oily substrate in the culture liquid and Fe content of the cells. Using this semi-batch culture, high lipase activity, 5600 units/ml, was attained at an optimal value of q 0.
    Type of Medium: Electronic Resource
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  • 7
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 27 (1988), S. 417-422 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary High concentration production of an extracellular enzyme, lipase, was achieved by a fed-batch culture of Pseudomonas fluorescens. During the cultivation, temperature, pH and dissolved oxygen concentration wwre maintained at 23°C, 6.5 and 2–5 ppm, respectively. Olive oil was used as a carbon source for microbial growth. To produce lipase effectively the specific feed rate of olive oil had to be maintained in a range of 0.04–0.06 (g oil) · (g dry cell)-1 · h-1. The CO2 evolution rate was monitored to estimate the requirement of olive oil. The ratio of feed rate of olive oil to the CO2 evolution rate was varied in the range of 20–60 g oil/mol CO2. The higher value of the ratio accelerated microbial growth, but did not favour lipase production. Once the high cell concentration of 60 g/l had been achieved, the ratio was changed from 50 to 30 g oil/mol CO2 to accelerate the lipase production. By this CO2-dependent method a very high activity of lipase, 1980 units/ml, was obtained. Both the productivity and yield of lipase were prominently increased compared with a conventional batch culture.
    Type of Medium: Electronic Resource
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  • 8
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary To control molecular weight of poly-β-hydroxybutyric acid (PHB) produced in a fedbatch culture of Protomonas extorquens, the effects of cultural temperature, pH, molar ratio of methanol and ammonia, and concentration of methanol in the medium on polymerization were inverstigated. Change of methanol concentration affected average molecular weight of PHB. When the cultivation was carried out at 0.05 g/l of methanol, average molecular weight of PHB reached above 8×105. On the other hand, in the case of 32 g/l of methanol average molecular weight of PHB was less than 0.5×105. Although every sample had a wide molelcular weight distribution, it became possible to control voluntarily average molecular weight of PHB.
    Type of Medium: Electronic Resource
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  • 9
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 23 (1986), S. 322-329 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Fifty-one methylotrophs were checked with respect to their ability of poly-β-hydroxybutyric acid (PHB) production from methanol. One of them, Pseudomonas sp. K, was chosen from its good growth on a minimum synthetic medium. Optimal temperature and pH for its growth were 30° C and 7.0, respectively. Concentrations of PO 4 3- and NH 4 + in the medium should be kept at low levels. PHB formation was stimulated by deficiency of nutrient such as NH 4 + , SO 4 2- , Mg2+, Fe2+ or Mn2+. Among them, nitrogen deficiency was chosen from its effectiveness and easiness for PHB accumulation. The microorganism was cultivated to produce a large amount of poly-β-hydroxybutyric acid (PHB) from methanol by means of microcomputer-aided fully automatic fed-batch culture technique. During the cultivation, temperature, dissolved oxygen concentration (DO), and methanol concentration in the culture broth were maintained at 30° C 2.5±0.5 ppm and 0.5±0.2 g/l, respectively. Other nutrients, nitrogen source and mineral ions, were also controlled to maintain their initial concentrations in the medium during cell growth phase. When the high cell concentration was achieved (160 g/l), feedings of ammonia and minerals were stopped and only methanol was supplied successively to accumulate PHB. At 175 h, high concentration of PHB (136 g/l) was obtained and total cell concentration became 206 g/l. DO must be maintained above the critical level during the PHB formation phase, too. PHB yield from methanol (g PHB/g methanol) was 0.18 and the maximum PHB content reached 66% of dry weight. Solid PHB produced by the strain had the melting point of 176° C and the average molecular weight of 3.0x105.
    Type of Medium: Electronic Resource
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  • 10
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 24 (1986), S. 370-374 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The effect of the ratio of methanol to ammonia, in the feeding solution the C/N ratio, on microbial PHB production was investigated. A constant C/N ratio regulated both the PHB content and the specific rate of PHB production. The results indicated that to produce the maximum PHB effectively in a short time the C/N ratio should be controlled automatically according to the increase in PHB content. Variation of the PHB content was estimated by tracing the timecourse of CO2 concentration in exhaust gas. When the cell concentration reached 70 g/l, C/N ratio was gradually increased from the initial C/N ratio of 10 (mol methanol/mol ammonia). At 121 h, concentration of PHB reached 136 g/l, which was the maximum level so far obtained. The reaction time was considerably shortened compared with our previous study (175 h). Furthermore, PHB concentration reached 149 g/l at 170 h and total cell concentration became 233 g/l. PHB yield from methanol was 0.20 (g PHB/g methanol), which was also superior to the previous result of 0.18.
    Type of Medium: Electronic Resource
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