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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 430-437 
    ISSN: 0006-3592
    Keywords: glucose ; glycerol ; γ-poly(glutamic acid) ; Bacillus licheniformis ATCC 9945a ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bacillus licheniformis ATCC 9945a is one of the bacterial strains that produce γ-poly(glutamic acid) (γ-PGA). The use of carbohydrate medium components for γ-PGA production was explored. Cells were grown in shake flasks or in controlled pH fermentors using medium formulations that contain different carbon sources. During the cultivations, aliquots were removed to monitor cell growth, carbon utilization, polymer production, and polymer molecular weight. Glucose was a better carbon source than glycerol for cell growth. Furthermore, glucose was utilized at a faster rate than glycerol, citrate, or glutamate. However, by using mixtures of glucose and glycerol in medium formulations, the efficiency of γ-PGA production increased. For example, by increasing the glycerol in medium formulations from 0 to 40 g/L, the γ-PGA broth concentration after 96 h increased from 5.7 to 20.5 g/L. Considering that glycerol utilization was low for the glucose/glycerol mixtures studied, it was unclear as to the mechanism by which glycerol leads to enhanced product formation. Cell growth and concomitant γ-PGA production (12 g/L) at pH 6.5 was possible using glucose as a carbon source if trace amounts (0.5 g/L each) of citrate and glutamate were present in the medium. We suggested that citrate and glutamate were useful in preventing salt precipitation from the medium. In addition, glutamate may be preferred relative to ammonium chloride as a nitrogen source. The conversion of glucose to γ-PGA by the strain ATCC 9945a was believed to occur by glycolysis of glucose to acetyl-CoA and tricarboxylic acid (TCA) cycle intermediates that were then metabolized via the TCA cycle to form α-ketoglutarate, which is a direct glutamate precursor. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 430-437, 1998.
    Additional Material: 9 Ill.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 50 (1996), S. 222-227 
    ISSN: 0006-3592
    Keywords: γ-poly(glutamate) ; γ-PGA ; Bacillus licheniformis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bacillus licheniformis ATCC 9945A was grown on Medium E in batch fermentations in which the pH was maintained at 5.5., 6.5, 7.4, and 8.25. The effects of pH on cell growth, carbon source utilization, and γ-polyglutamic acid (γ-PGA) production, molecular weight, and polymer stereochemistry were determined. The γ-PGA yield was highest (15 g/L, 96 h growth time) at pH 6.5. The increase in γ-PGA formation at pH 6.5 corresponded with a relatively high specific production rate at high γ-PGA concentration (0.09 h-1, ∼15 g/L γ-PGA). In contrast, the specific γ-PGA production rates at fermentor pH values of 5.5 and 7.4 decreased significantly for γ-PGA fermentor yields 〉∼5 g/L. Interestingly, alteration of the medium pH had little to no significant effects on the product quality as measured by stereochemical composition and molecular weight. While glutamate and glycerol utilization were similar as a function of pH, citrate consumption increased at pH 6.5, indicating that the formation of γ-PGA from citrate at pH 6.5 was of increased importance. The effect of aeration was evaluated by increasing the agitation speed (250 to 800 rpm) and aeration rate (0.5 to 2.0 L/min) at pH 6.5, the pH of maximal γ-PGA production. Increased aeration resulted in doubling of the cell dry weights (2 to 4 g/L), increasing γ-PGA yields (6.3 to 23 g/L by 48 h) and increasing in the maximum γ-PGA-specific production rate (0.09 to 0.11 h-1). Other effects of increased agitation included a rapid depletion of glutamate and citrate (by 50 h) and a decrease in product molecular weight. Despite the increase in agitation and aeration, oxygen limitation of the culture was not avoided, because the partial pressure decreased to 〈1.0% by 29 h. © 1996 John Wiley & Sons, Inc.
    Additional Material: 2 Ill.
    Type of Medium: Electronic Resource
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