Mathematical evaluation of plantaricin formation supports an auto-induced production mechanism

The production rate of a bacteriocin, produced by Lactobacillus plantarum TMW1.25 and previously named plantaricin1.25, was studied during pH-constant batch fermentations under various growth media conditions. The growth of L. plantarum and production of bacteriocin during the retardation phase were modelled, using 11 different empirical and mechanistic approaches. The optimal pH for bacteriocin production was 4.5. Among the different nitrogen sources tested, yeast extract was the most important, on the basis of the fact that the maximum growth rate decreased 16% without yeast extract, and only 7.2% or 8.1% without meat extract or peptone respectively. However, the change of nitrogen source did not have a significant effect on bacteriocin production. The progression of plantaricin1.25 production during the retardation phase and growth of L. plantarum TMW1.25 could be described by a structured model in which the bacteriocin concentration induces its own production. Among those models not implementing bacteriocin induction, only the one with an exponential increase of bacteriocin yield per unit biomass was suitable to describe bacteriocin production. Computer-aided evaluation of experimental data appears to be helpful in elucidating the relationship between the growth of lactic acid bacteria and bacteriocin production. Received: 22 May 1998 / Received last revision: 9 November 1998 / Accepted: 14 November 1998     

Acetate enhances solvent production and prevents degeneration in Clostridium beijerinckii BA101

Addition of sodium acetate to chemically defined MP2 medium was found to increase and stabilize solvent production by Clostridium beijerinckii BA101, a solvent-hyperproducing mutant derived from C. beijerinckii NCIMB 8052. C. beijerinckii BA101 demonstrated a greater increase in solvent production than C. beijerinckii NCIMB 8052 when sodium acetate was added to MP2 medium. In 1-l batch fermentations, C. beijerinckii BA101 produced 32.6 g/l total solvents, with butanol at 20.9 g/l, when grown in MP2 medium containing 60 mM sodium acetate and 8% glucose. To our knowledge, these values represent the highest solvent and butanol concentrations produced by a solventogenic Clostridium strain when grown in batch culture. Received: 29 September 1998 / Received revision: 13 February 1999 / Accepted: 26 February 1999     

Compostable packaging materials – test methods and limit values for biodegradation

In order to classify packaging materials as capable of organic recovery according to the packaging regulation of the European Union, the intended materials must be tested for their compostability. An important prerequisite is the determination of biodegradability by standardized test methods. Details of the intended tests are not comprehensible without further knowledge of the problems of biodegradation testing. The test methods and the limit values used to evaluate the biodegradation results are presented and discussed against the background of established test methods and limit values for chemicals. Furthermore the problem of ecotoxicity tests in connection with compost quality is discussed and an overview of European test laboratories is given. Received: 27 August 1998 / Received revision: 4 November 1998 / Accepted: 7 November 1998     

Cultivation of Tetrahymena thermophila in a 1.5-m3 airlift bioreactor

A large-scale cultivation system for the mass cell production and extraction of the protozoon Tetrahymena thermophila has been developed on the basis of a low-cost complex nutrient medium. Cell growth and the production of extracellular proteases were investigated using a 15-l stirred-tank reactor and 13-l and 1500-l airlift reactors. Processes using defined and complex medium formulations were compared. After cell mass production by 1200 l cell suspension in the large airlift bioreactor, two different extraction methods, based on the use of an extraction decanter and a sedimentation procedure, were compared and followed by cell lyophilization. Cell sedimentation was shown to be the more efficient extraction method as it enabled cell retention/separation while preserving the cell structure. Maximum cell growth was achieved in the stirred-tank bioreactor, supporting the hypothesis that higher shear forces reduce the particle size of the medium, which is responsible for an optimized nutrient supply. The highest glucose uptake rates were found in defined medium lacking the nutrient particles that are present in complex medium formulations. The cell-specific proteolytic activity in culture supernatants of airlift bioreactors using complex medium conditions was higher than that of a culture broth with cells grown under defined medium formulations. Received: 24 September 1998 / Received revision: 23 November 1998 / Accepted: 29 November 1998     

Growth and amino acid requirements of hyaluronic-acid-producing Streptococcus zooepidemicus

A chemically defined medium has been developed for anaerobic cultivation of hyaluronic-acid(HA)-producing Streptococcus zooepidemicus, which contains 11 amino acids essential to growth, and glutamine as a principal nitrogen source. The final HA concentration, the specific rate of HA production and HA-to-glucose yields were similar for growth in the chemically defined medium relative to growth in complex medium. Consequently cells cultivated on chemically defined medium can be expected to have similar activity regarding HA synthesis as compared to cells grown on complex media. However, the specific growth rate and volumetric HA production rate were found to be less favourable in the chemically defined media. Received: 4 October 1996 / Accepted: 25 October 1996     

Fungal laccase grafts acrylamide onto lignin in presence of peroxides

Laccase (EC 1.10.3.2) from the white-rot basidomycete Trametes versicolor in the presence of organic peroxides, particularly dioxane peroxide, tetrahydrofuran peroxide and t-butylhydroperoxide, initiated free-radical copolymerization of acrylamide and lignin. Hydrogen peroxide showed no such effect. Both the type of peroxide and the catalytic efficiency of the enzyme were important to ensure a significant yield of copolymerisate and a high rate of acrylamide incorporation into a lignin backbone. The mechanism of the enzymatic grafting is discussed. Received: 12 August 1998 / Received revision: 18 November 1998 / Accepted: 21 November 1998     

Effect of feeding strategy on Zymomonas mobilis CP4 fed-batch fermentations and mathematical modeling of the system

In this work, the effect of the feeding strategy in Zymomonas mobilis CP4 fed-batch fermentations on the final biomass and ethanol concentrations was studied. Highest glucose yields to biomass (0.018 g/g) and to ethanol (0.188 g/g) were obtained in fed-batch fermentations carried out using different feeding rates with a glucose concentration in the feed equal to 100 g/l. Lower values (0.0102 g biomass/g glucose and 0.085 g ethanol/g glucose) were obtained when glucose accumulated to levels higher than 60 g/l. On the other hand, the highest biomass (5 g/l) and ethanol (39 g/l) concentrations were obtained using a glucose concentration in the feed equal to 220 g/l and exponentially varied feeding rates. Experimental data were used to validate the mathematical model of the system. The prediction errors of the model are 0.39, 14.36 and 3.24 g/l for the biomass, glucose and ethanol concentrations, respectively. Due to the complex relationship for describing the specific growth rate, a fed-batch culture in which glucose concentration is constant would not optimize the process. Received: 30 November 1999 / Received revision: 24 March 2000 / Accepted: 7 April 2000     

Production of polyhydroxybutyrate by Ralstonia eutropha from protein hydrolysates

Polyhydroxybutyrate (PHB) was produced by Ralstonia eutropha DSM 11348 (formerly Alicaligenes eutrophus) in media containing 20–30 g l⁻¹ casein peptone or casamino acids as sole sources of nitrogen. In fermentations using media based on casein peptone, permanent growth up to a cell dry mass of 65 g l⁻¹ was observed. PHB accumulated in cells up to 60%–80% of dry weight. The lowest yields were found in media without any trace elements or with casamino acids added only. The residual cell dry masses were limited to 10–15 g l⁻¹ and did not contain PHB. The highest productivity amounted to 1.2 g PHB l⁻¹ h⁻¹. The mean molecular mass of the biopolymer was determined as 750 kDa. The proportion of polyhydroxyvalerate was less than 0.2% in PHB. The bioprocess was scaled up to a 300-l plant. During a fermentation time of 39 h the cells accumulated PHB to 78% w/w. The productivity was 0.98 g PHB l⁻¹ h¹. Received: 8 July 1998 / Accepted: 26 August 1998     

In vivo-decolorization of coal-derived humic acids by laccase-excreting fungus Trametes versicolor

Lignite (brown coal) can be liquefied/solubilized with several fungi by different mechanisms. When applied industrially, only catalytic mechanisms can compete with chemical methods. The well-known fungal ligninolytic peroxidases are at a disadvantage, in that the relatively expensive hydrogen peroxide must be used as a cofactor. Comparing several fungal strains, we observed that the fungus Trametes versicolor is able to decolorize coal-derived humic acids, producing a considerable amount of laccase in the process. During this reaction the amount of humic acids decreases whilst that of fulvic acids increases; this was verified by optical density measurement and GPC after the two substance classes had been separated. Received: 27 August 1998 / Received revision: 4 November 1998 / Accepted: 7 November 1998     

Towards rice genome scanning by map-based AFLP fingerprinting

Map-based DNA fingerprinting with AFLP markers provides a fast method for scanning the rice genome. Three hundred AFLP markers identified with ten primer combinations were mapped in two rice populations. The genetic maps were aligned and almost full coverage of the rice genome was obtained. The transferability of AFLP markers between indica × japonica and indica × indica crosses was tested. The chromosomes were divided into DNA Fingerprint Linkage Blocks (DFLBs) defined by specific AFLP markers. Using these blocks, the degree of similarity or divergence within specific chromosome regions was calculated for nine varieties. Applications of map-based fingerprinting for biodiversity studies and maker-assisted selection are discussed. Received: 6 June 1998 / Accepted: 11 November 1998     

Production, recovery and purification of bacteriocins from lactic acid bacteria

Bacteriocins produced by lactic acid bacteria are a heterogeneous group of peptide inhibitors which include lantibiotics (class I, e.g. nisin), small heat-stable peptides (class II, e.g. pediocin AcH/PA1) and large heat-labile proteins (class III, e.g. helveticin J). Many bacteriocins belonging to the first two groups can be successfully used to inhibit undesirable microorganisms in foods, but only nisin is produced industrially and is licensed for use as a food preservative in a partially purified form. This review focuses on the production and purification of class I and class II bacteriocins from lactic acid bacteria. Bacteriocin production is growth associated but the yield of bacteriocin per unit biomass is affected by several factors, including the producing strain, media (carbohydrate and nitrogen sources, cations, etc.) and fermentation conditions (pH, temperature, agitation, aeration and dilution rate in continuous fermentations). Continuous fermentation processes with cell recycle or immobilized cells can result in a dramatic improvement in productivity over batch fermentations. Several simple recovery processes, based on adsorbing bacteriocin on resins or silica compounds, have been developed and can be used to build integrated production processes. Received: 29 December 1998 / Received revision: 23 April 1999 / Accepted: 23 April 1999     

Improved formation of regenerable callus in isolated microspore culture of maize: impact of carbohydrates, plating density and time of transfer

 Pure fractions of maize (Zea mays L.) microspores at various densities were exposed to defined media containing different concentrations of maltose and sucrose. In general, lower carbohydrate concentrations (60, 90 g/l) yielded higher frequencies of embryo-like structures than a high concentration (120 g/l). Optimum cell density seemed to depend on the genotype, but densities above 80,000 microspores/ml led to reduced embryogenesis in all genotypes tested. Direct comparison of maltose and sucrose as carbohydrate source in the induction medium clearly demonstrated the superiority of maltose with regard to the regeneration frequency. For two out of three genotypes tested, maltose also enhanced the formation of embryo-like structures. The time of embryo transfer to callus induction media had a significant effect on regeneration frequency. Received: 26 September 1997 / Revision received: 5 November 1998 / Accepted 24 March 1999     

Quantification of bacterial polyhydroxyalkanoic acids by Nile red staining

The fluorescence properties of one chemically and seven biologically produced polyhydroxyalkanoic acids were investigated as film castings and in living cells respectively after staining with Nile red. All these polyesters show a similar fluorescence behaviour, revealing a clear fluorescence maximum at an excitation wavelength between 540 nm and 560 nm and an emission wavelength between 570 nm and 605 nm. This could be shown by the use of two-dimensional fluorescence spectroscopy and flow cytometry. The examination of native poly(3-hydroxybutyric acid), poly(3HB), granules isolated from cells of Ralstonia eutropha H16 showed that the addition of 6.0 μg Nile red is necessary for total staining of 1.0 mg granules. The fluorescence intensity at an excitation wavelength of 550 nm and an emission wavelength of 600 nm showed high correlation to the poly(3HB) concentration of grana suspensions at different grana concentrations. These results and the staining of cell suspensions during cultivation experiments revealed that Nile red has a high potential for the quantitative determination of hydrophobic bacterial polyhydroxyalkanoic acids. Received: 13 November 1998 / Received revision: 4 February 1999 / Accepted: 12 February 1999     

Effects of yeast extract on the production and the quality of the exopolysaccharide, zooglan, produced by Zoogloea ramigera 115SLR

Although many studies have examined the influence of culture conditions on the production and composition of polysaccharides, little is known about the factors influencing the quality of exopolysaccharides (EPS). In this work we studied the effect of yeast extract on the production, composition and molecular weight of the EPS zooglan produced by Zoogloea ramigera 115SLR. This bacterium was grown on a new completely defined synthetic medium and on a medium containing yeast extract. Growth and polysaccharide production performances were comparable on the two media with a glucose to exopolysaccharide conversion yield of 35% (g/g). The polysaccharides produced on these two media have an identical composition but a different molecular weight and molecular weight distribution. The yeast extract medium leads to a more homogeneous polysaccharide solution. Received: 12 June 1998 / Received revision: 19 September 1998 / Accepted: 11 October 1998     

Carbon catabolite repression of invertase during batch cultivations of Saccharomyces cerevisiae: the role of glucose, fructose, and mannose

When Saccharomyces cerevisiae are grown on a mixture of glucose and another fermentable sugar such as sucrose, maltose or galactose, the metabolism is diauxic, i.e. glucose is metabolized first, whereas the other sugars are metabolized when glucose is exhausted. This phenomenon is a consequence of glucose repression, or more generally, catabolite repression. Besides glucose, the hexoses fructose and mannose are generally also believed to trigger catabolite repression. In this study, batch fermentations of S. cerevisiae in mixtures of sucrose and either glucose, fructose or mannose were performed. It was found that the utilization of sucrose is inhibited by concentrations of either glucose or fructose higher than 5 g/l, and thus that glucose and fructose are equally capable of exerting catabolite repression. However, sucrose was found to be hydrolyzed to glucose and fructose, even when the mannose concentration was as high as 17 g/l, indicating, that mannose is not a repressing sugar. It is suggested that the capability to trigger catabolite repression is connected to hexokinase PII, which is involved in the in vivo phosphorylation of glucose and fructose. Received: 5 May 1998 / Received revision: 3 August 1998 / Accepted: 8 August 1998     

Microbial heavy-metal resistance

We are just beginning to understand the metabolism of heavy metals and to use their metabolic functions in biotechnology, although heavy metals comprise the major part of the elements in the periodic table. Because they can form complex compounds, some heavy metal ions are essential trace elements, but, essential or not, most heavy metals are toxic at higher concentrations. This review describes the workings of known metal-resistance systems in microorganisms. After an account of the basic principles of homoeostasis for all heavy-metal ions, the transport of the 17 most important (heavy metal) elements is compared. Received: 25 November 1998 / Received revision: 18 February 1999 / Accepted: 20 February 1999     

Reversal of the inhibitory effect of surfactants upon germination and growth of a consortium of two strains of Bacillus

Anionic, cationic, amphoteric and non-ionic surfactants inhibited spore germination and subsequent growth of a mixture of two Bacillus strains at surfactant concentrations ranging from 1 ppm to 50 ppm. Germination appeared to be more affected than cell growth by the presence of surfactants, the inhibitory thresholds being largely increased when media were inoculated with vegetative cells. The bacterial species forming the consortium were incapable of growing on liquid and agar-solidified media prepared with non-diluted domestic wastewater. Addition of hydrolases (protease, cellulase, α-amylase and lipase) to the wastewater medium allowed the germination of spores and their vegetative growth. Received: 9 July 1998 / Received revision: 26 October 1998 / Accepted: 30 October 1998     

Extracellular laccase production during hyphal interactions between Trichoderma sp. and Shiitake, Lentinula edodes

Lentinula edodes (Berk.) Pegler was cultivated in liquid media containing malt and yeast extract. Extracellular laccase activity, measured in the culture fluids, was 5–18 times higher in cultures incubated for 29 days than in cultures incubated for 24 days. The addition of water-soluble lignin derivatives or Trichoderma sp. in cultures of L. edodes incubated for 11 days increased laccase activity 3- to 20 fold. The higher response was obtained with live mycelium of Trichoderma sp., but cell-free culture fluids of Trichoderma sp. in pure cultures were also effective. Trichoderma sp. induced changes in the laccase isoenzyme pattern as a result of the alteration of laccases secreted by L. edodes and not the induction of new isoforms. Received: 3 November 1997 /  Received revision: 19 January 1998 /  Accepted: 24 January 1998     

Biotransformation of citronellol by the basidiomycete Cystoderma carcharias in an aerated-membrane bioreactor

The basidiomycete Cystoderma carcharias transformed citronellol into 3,7-dimethyl-1,6,7-octanetriol as the main product. 3,7-Dimethyl-6,7-epoxy-1-octanol was identified as important intermediary product of the biotransformation, and the allylic diols 2,6-dimethyl-2-octene-1,8-diol, 3,7-dimethyl-5-octene-1,7-diol and 3,7-dimethyl-7-octene-1,6-diol were found to be minor products. Microbial formation of rose oxide, a flavour-impact component, was observed for the first time. The formation of the main products was inhibited by 70% after addition of 0.1 mmol l⁻¹ cytochrome monooxygenase inhibitors. Formation of 3,7-dimethyl-1,6,7-octanetriol was effective in a bioreactor with aeration over a coil of a hydrophobic microporous polypropene capillary membrane. Production rates of up to 150 mg l⁻¹ day⁻¹ were reached and led to a product concentration of 866 mg l⁻¹ (conversion rate: 52%). The total loss of the added volatile substrate via the exhaust air was 4.5% when this aeration method was used. Received: 30 July 1998 / Received revision: 2 November 1998 / Accepted: 7 November 1998     

Growth and bacteriocin production by Enterococcus faecium DPC1146 in batch and continuous culture

Production of the bacteriocin enterocin 1146 (E1146) by Enterococcus faecium DPC1146 was studied in batch and continuous fermentation. Growth was strongly inhibited by lactic acid. In batch fermentations maximum E1146 activity (2.8 MBU L⁻¹) was obtained in 9 h with 20 g L⁻¹ glucose. Increase in initial glucose concentration did not lead to a proportional increase in E1146 activity. A simple linear model was found to be adequate to explain the relationship between specific bacteriocin production rate and specific growth rate in batch fermentations with initial glucose concentration higher than 20 g L⁻¹. Maximum bacteriocin activity (2.9–3.2 MBU L⁻¹) was obtained in continuous fermentations at dilution rates between 0.12 and 0.17 h⁻¹ and specific bacteriocin production rate increased linearly with dilution rate. Received 31 July 1996/ Accepted in revised form 01 November 1996