Monitoring of staphylococcal starters in two French processing plants manufacturing dry fermented sausages

AIMS: The growth and survival of Staphylococcus xylosus and Staphylococcus carnosus were monitored during sausage manufacture in two processing plants. METHODS AND RESULTS: The gram-positive, catalase-positive cocci isolated from the processing plants F10 and F11 were identified by Staphylococcus-specific PCR and species-specific oligonucleotide array. In the inoculated products with starter cultures, 90% of staphylococcal strains isolated in F10 were identified as S. xylosus and 10% as S. carnosus. In F11, 77% were identified as S. xylosus and 20% as S. carnosus. Staphylococcus xylosus dominated the staphylococcal microbiota while S. carnosus survived during the process. The pulse-field gel electrophoresis analysis revealed that all S. xylosus and S. carnosus strains isolated corresponded to the starter strains inoculated. The two starter strains of S. xylosus co-dominated in the isolates from sausages of F11, whereas the strain with pattern A1 was dominant in the isolates from sausages of F10. In the environments, no S. carnosus and S. xylosus were found, whereas Staphylococcus equorum and Staphylococcus saprophyticus were the main species isolated. CONCLUSIONS: This work highlighted the domination of S. xylosus starter strains, which showed a strong capacity to grow during sausage process, while S. carnosus survived during the process. SIGNIFICANCE AND IMPACT OF THE STUDY: Successful implantation of starter cultures is obviously a prerequisite for their contribution to sensorial qualities. Thus, the monitoring of the growth and the survival of S. xylosus and S. carnosus are required to guarantee a well-adapted starter culture. This study revealed that the two Staphylococcus species are suitable for manufacturing sausages in processing plants with very different capacities of production.     

Effect of binary combinations of selected toxic compounds on growth and fermentation of Kluyveromyces marxianus

The inhibitory effects of various lignocellulose degradation products on glucose fermentation by the thermotolerant yeast Kluyveromyces marxianus were studied in batch cultures. The toxicity of the aromatic alcohol catechol and two aromatic aldehydes (4-hydroxybenzaldehyde and vanillin) was investigated in binary combinations. The aldehyde furfural that usually is present in relatively high concentration in hydrolyzates from pentose degradation was also tested. Experiments were conducted by combining agents at concentrations that individually caused 25% inhibition of growth. Compared to the relative toxicity of the individual compounds, combinations of furfural with catechol and 4-hydroxybenzaldehyde were additive (50% inhibition of growth). The other binary combinations assayed (catechol with 4-hydroxybenzaldehyde, and vanillin with catechol, furfural, or 4-hydroxybenzaldehyde) showed synergistic effect on toxicity and caused a 60-90% decrease in cell mass production. The presence of aldehydes in the fermentation medium strongly inhibited cell growth and ethanol production. Kluyveromyces marxianus reduces aldehydes to their corresponding alcohols to mitigate the toxicity of these compounds. The total reduction of aldehydes was needed to start ethanol production. Vanillin, in binary combination, was dramatically toxic and was the only compound for which inhibition could not be overcome by yeast strain assimilation, causing a 90% reduction in both cell growth and fermentation.     

Tourmaline ceramic balls stimulate growth and metabolism of three fermentation microorganisms

Effects of tourmaline ceramic balls on growth and metabolism of Saccharomyces cerevisiae, Lactobacillus acidophilus and Aspergillus oryzae were studied. Treatments with 3, 6, 9 or 12 g of tourmaline ceramic balls in a 50 ml culture showed significant stimulation of the growth of the three microorganisms. In optimal treatments with 12 g of tourmaline balls, the growth of S. cerevisiae, L. acidophilus, and A. oryzae was increased by 34, 32 and 10%, respectively. After 72 h fermentation of S. cerevisiae, total carbohydrate content in the culture medium was decreased by 65% and ethanol production was increased by 150%. Total carbohydrate content was decreased by 80% and the pH value was decreased by 0.3, as a result of organic acid production in the medium of L. acidophilus after 72 h fermentation. In the case of A. oryzae, enzyme activities of protease and amylase were increased by 90 and 31%, respectively, after 96 h fermentation. Results indicated that tourmaline stimulates initiation of growth in the early lag stage and increases production of metabolites at a later stage of fermentation. The strong stimulatory effect of tourmaline on growth, utilization of substrates and production of metabolites in the three microorganisms suggests a potential application in the fermentation industry.     

Monoclonal antibody productivity and the metabolic pattern of perfusion cultures under varying oxygen tensions

The metabolic pattern and cell culture kinetics of high-cell-density perfusion cultures were compared under two different oxygen transfer conditions: oxygen limiting and not limiting. When oxygen was a limiting factor during perfusion culture, both specific glucose uptake and lactate production rates increased, compared to non-oxygen-limited condition, by about 60% and 30%, respectively. The specific glutamine uptake rate under oxygen-limited conditions was almost 4.0 times higher than that under non-oxygen-limited conditions. The activity of lactate dehydrogenase (LDH) released into the medium by the dead cells can be used as an indicator for the metabolic and physiological conditions related to oxygen limitation. There was a 3.2 times higher specific rate of LDH activity released by dead cells in oxygen-limited cultures than those in non-oxygen-limited cultures. The specific production rate of monoclonal antibody was not significantly affected by the oxygen transfer conditions during the rapid cell growth period, but it rapidly increased toward the end of perfusion cultures. The higher perfusion rate may have limited further cell growth during high-cell-density perfusion culture, because cell damage was caused by the hydrodynamic shear within a hollow fiber microfiltration cartridge installed to withdraw the spent medium and the waste metabolites. (c) 1993 John Wiley & Sons, Inc.     

Continuous hydrogen production during fermentation of alpha-cellulose by the thermophillic bacterium Clostridium thermocellum

Continuous hydrogen (H2) production during fermentation of alpha-cellulose was established using the thermophillic, anaerobic bacterium Clostridium thermocellum ATCC 27405. The objectives of this work were to characterize growth of C. thermocellum, quantify H2 production and determine soluble end-product synthesis patterns during fermentation of a cellulosic substrate under continuous culture conditions. A 5 L working volume fermentor was established and growth experiments were maintained for over 3,000 h. Substrate concentrations were varied from 1 to 4 g/L and the feed was introduced with continuous nitrogen gas sparging to prevent clogging of the feed-line. The pH and temperature of the reactor were maintained at 7.0 and 600 degrees C, respectively, throughout the study. At concentrations above 4 g/L, the delivery of alpha-cellulose was impaired due to feed-line clogging and it became difficult to maintain a homogenous suspension. The highest total gas (H2 plus CO2) production rate, 56.6 mL L(-1) h(-1), was observed at a dilution rate of 0.042 h(-1) and substrate concentration of 4 g/L. Under these conditions, the H2 production rate was 5.06 mmol h(-1). Acetate and ethanol were the major soluble end-products, while lactate and formate were greatly reduced compared to production in batch cultures. Concentrations of all metabolites increased with increasing substrate concentration, with the exception of lactate. Despite a number of short-term electrical and mechanical failures during the testing period, the system recovered quickly, exhibiting substantial robustness. A carbon balance was completed to ensure that all end-products were accounted for, with final results indicating near 100% carbon recovery. This study shows that long-term, stable H2 production can be achieved during direct fermentation of an insoluble cellulosic substrate under continuous culture conditions.     

Development of a high throughput screening method to test flavour-forming capabilities of anaerobic micro-organisms

AIM: Development of a fast, automated and reliable screening method for screening of large collections of bacterial strains with minimal handling time. METHODS AND RESULTS: The method is based on the injection of a small headspace sample (100 microl) from culture vials (2 ml) in 96-well format directly into the mass spectrometry (MS). A special sample tray has been developed for liquid media, and anaerobically grown cultures. In principle, all volatile components can be measured, but a representative mass fragment has to be obtained in the MS. Representative masses for 3-methylbutanal, 2-methylpropanal and benzaldehyde are 58, 72 and 105, respectively. In 1 day over 1500 samples could be analysed and the coefficient of variation for the response was <5%. CONCLUSION: Screening of 72 strains belonging to the genus Lactococcus in quadruple on the production of the key-flavour compound 3-methylbutanal illustrated the effectiveness of the method. Furthermore, knowledge of the biochemistry and physiology of 3-methylbutanal formation was used to optimize the composition of the growth medium to enhance 3-methylbutanal production, and thereby improve the screening. SIGNIFICANCE AND IMPACT OF THE STUDY: A commonly used method to control flavour formation in fermented food products is the selection of bacterial strains, which are able to produce the desired flavour compounds. As large collections of strains are available for such screenings, studying biodiversity of micro-organisms on the level of metabolic routes is strongly facilitated by highly automated high throughput screening methods for measuring enzyme activities or production of metabolites. Therefore, this method will be a useful tool for selecting flavour-producing strains and for enhancing starter culture development.     

Assessment of in-line near-infrared spectroscopy for continuous monitoring of fermentation processes

The application of NIR in-line to monitor and control fermentation processes was investigated. Determination of biomass, glucose, and lactic and acetic acids during fermentations of Staphylococcus xylosus ES13 was performed by an interactance fiber optic probe immersed into the culture broth and connected to a NIR instrument. Partial least squares regression (PLSR) calibration models of second derivative NIR spectra in the 700-1800 nm region gave satisfactory predictive models for all parameters of interest: biomass, glucose, and lactic and acetic acids. Batch, repeated batch, and continuous fermentations were monitored and automatically controlled by interfacing the NIR to the bioreactor control unit. The high frequency of data collection permitted an accurate study of the kinetics, supplying lots of data that describe the cultural broth composition and strengthen statistical analysis. Comparison of spectra collected throughout fermentation runs of S. xylosus ES13, Lactobacillus fermentum ES15, and Streptococcus thermophylus ES17 demonstrated the successful extension of a unique calibration model, developed for S. xylosus ES13, to other strains that were differently shaped but growing in the same medium and fermentation conditions. NIR in-line was so versatile as to measure several biochemical parameters of different bacteria by means of slightly adapted models, avoiding a separate calibration for each strain.     

Development of specific PCR primers for a rapid and accurate identification of Staphylococcus xylosus, a species used in food fermentation

Twenty-seven Staphylococcus strains isolated from food and food environments were assigned to Staphylococcus xylosus by API-Staph system. But only seven isolates had similar patterns to this species when compared to the pulse-field gel electrophoresis patterns of 12 S. xylosus strains. To perform a rapid identification of the S. xylosus species, a random amplified polymorphic DNA product of 539-bp shared by all of the S. xylosus strains was used to design a pair of primers. These primers were species-specific for S. xylosus when tested by PCR on 21 staphylococci species. This specific PCR assay confirms the identification of the seven isolates identified by PFGE to S. xylosus. In conclusion, we developed specific PCR primers for a rapid and accurate identification of the S. xylosus species.     

优良性状蚕蛹虫草的筛选及高产虫草素液态发酵条件优化

蛹虫草是重要的食药用真菌,虫草素为其主要活性成分,在抗肿瘤、抗菌、降血糖等方面具有较为突出的功效。蛹虫草菌株间的形态及环境条件差异,对菌株次级代谢产物虫草素产生影响显著。本研究对不同来源的6株蛹虫草菌株（YCC-B、YCC-C、YCC-H、YCC-W、YCC-Y、CGMCC 3.4655）,从蚕蛹体培养子实体性状,液体发酵条件（培养天数、培养方式、外源金属离子等）和传代稳定性等方面筛选优良性状菌株,提高其发酵合成虫草素的能力及稳定性。结果表明,蛹虫草菌株YCC-W在蚕蛹子实体出草及菌体液体发酵产虫草素上综合表现优良,传代稳定;液体发酵培养基中添加外源金属离子Mn²⁺作为酶的辅基,可以促进虫草素合成;采用振荡-静置相结合的混合发酵培养方式,可以避免单纯振荡培养溶氧量大、菌丝体生长旺盛,而虫草素产生不佳的问题。先振荡培养3d后静置培养至25d时,菌株YCC-W合成虫草素含量最高,可达(874.13±24.25)μg/mL,且稳定性良好。为进一步开发菌种及扩大规模生产提供参考。     

Effect of aliphatic aldehydes on the lipid peroxidation and chemiluminescence of biological systems under oxidative stress

The effect of several aliphatic aldehydes on lipid peroxidation was evaluated by measuring the oxygen uptake rate, thiobarbituric acid-reactive products formation and the emitted visible chemiluminescence intensity. Measurements were carried out in brain homogenates and erythrocyte plasma membrane and liver microsomal fractions. In all systems studied, aldehydes (25 mmol/L) (e.g. acetaldehyde, 2,2-dimethylpropanal), increased the intensity of the luminescence associated with the oxidation process. In contrast, aldehyde incorporation decreased TBARS production and the rate of oxygen uptake. The increased luminescence intensity is explained in terms of secondary reactions of aldehyde derived free radicals. These results clearly indicate that extreme care must be exercized in the intepretation of chemiluminescence data in the presence of aldehydes. © 1997 John Wiley & Sons, Ltd.     

Reductions of 2-enals, dehydrogenation of saturated aldehydes and their racemisation

Enoate reductase or clostridia containing this enzyme (Clostridium tyrobutyricum or C. kluyveri) catalyse the reduction of alpha,beta-unsaturated aldehydes (enals). The enantiomeric purity of the saturated aldehydes obtained from alpha-substituted enals is usually rather low and depends heavily on the reaction conditions. The reduction of the corresponding allyl alcohols to the saturated alcohols leads to much higher enantiomeric purities, though the reduction of the enal corresponding to the allyl alcohol to the saturated aldehyde is an intermediary step in the reaction sequence allyl alcohol----saturated alcohol. The explanation seems to be the racemisation of saturated aldehydes caused by enoate reductase. This is illustrated by the reduction of (E)-2-methylcinnamyl aldehyde to (R)-2-methyl-3-phenylpropanal or (R)-2-methyl-3-phenylpropanol under different conditions and measuring the racemisation of the aldehyde as well as the hydrogen-deuterium exchange of 3-phenylpropanal. In contrast to saturated carboxylates saturated aldehydes can be dehydrogenated to alpha,beta-unsaturated aldehydes (enals) by enoate reductase in the presence of electron acceptors such as oxygen or dichlorophenol indophenol. Under these conditions enoate reductase shows in the presence of oxygen a surprisingly high half life (greater than 20 h) as compared to that which is observed when the enzyme was used as a reductase with NADH in the presence of oxygen. In this case the enzyme is inactivated within a few minutes.     

Culture of Staphylococcus xylosus in fish processing by‐product‐based media for lipase production

Aims: The objective of this study was to demonstrate that fish‐processing by‐products could be used as sole raw material to sustain the growth of Staphylococcus xylosus for lipase production. Methods and Results: Bacterial growth was tested on supernatants generated by boiling (100°C for 20 min) of tuna, sardine, cuttlefish and shrimp by‐products from fish processing industries. Among all samples tested, only supernatants generated from shrimp and cuttlefish by‐products sustained the growth of S. xylosus. Shrimp‐based medium gave the highest growth (A₆₀₀ = 22) after 22 h of culture and exhibited the maximum lipase activity (28 U ml^?1). This effect may be explained by better availability of nutrients, especially, in shrimp by‐products. Standard medium (SM) amendments to sardine and tuna by‐product‐based media stimulated the growth of S. xylosus and the highest A₆₀₀ values were obtained with 75% SM. Lipase activity, however, remained below 4 U ml^?1 for both sardine and tuna by‐product‐based media. Conclusions: Fish by‐products could be used for the production of highly valuable enzymes. Significance and Impact of the Study: The use of fish by‐products in producing S. xylosus‐growth media can reduce environmental problems associated with waste disposal and, simultaneously, lower the cost of biomass and enzyme production.     

Inhibition by reactive aldehydes of superoxide anion radical production in stimulated human neutrophils

alpha,beta-Unsaturated aldehydes were investigated in vitro for their ability to inhibit superoxide anion radical (O2-.) production in stimulated human polymorphonuclear leukocytes (PMN). The aldehydes investigated were (i) trans-4-hydroxynonenal and malonaldehyde (MDA), two toxic lipid peroxidation products; (ii) acrolein and crotonaldehyde, two air pollutants derived from fossil fuel combustion; (iii) trans,trans-muconaldehyde, a putative hematotoxic benzene metabolite. Preincubation of PMN with reactive aldehydes followed by stimulation with the oxygen burst initiator phorbol myristate acetate (PMA) resulted in a dose-dependent inhibition of O2-. production. The concentration at which 50% inhibition (IC50) was observed was 21 microM for acrolein, 23 microM for trans,trans-muconaldehyde, 27 microM for trans-4-hydroxynonenal and 330 microM for crotonaldehyde. A similar inhibitory effect by these aldehydes was observed in digitonin- and concanavalin A-stimulated PMN. MDA inhibited O2-. production in PMA-stimulated PMN by 100% at 10(-2) M but gave no inhibition at 10(-3) M. The standard aldehyde propionaldehyde did not inhibit O2-. production at 10(-3)-10(-6) M. Preincubation of PMN with acrolein in the presence of cysteine completely protected against the inhibitory effect of this reactive aldehyde. The results indicate that the ability of toxic aldehydes to inhibit O2-. production in stimulated PMN correlates directly with their alkylation potential which is a function of the electrophilicity of the beta carbon.     

Characterization of superoxide production from aldehyde oxidase: an important source of oxidants in biological tissues

Aldehyde oxidase, a molybdoflavoenzyme that plays an important role in aldehyde biotransformation, requires oxygen as substrate and produces reduced oxygen species. However, little information is available regarding its importance in cellular redox stress. Therefore, studies were undertaken to characterize its superoxide and hydrogen peroxide production. Aldehyde oxidase was purified to >98% purity and exhibited a single band at approximately 290 kDa on native polyacrylamide gradient gel electrophoresis. Superoxide generation was measured and quantitated by cytochrome c reduction and EPR spin trapping with p-dimethyl aminocinnamaldehyde as reducing substrate. Prominent superoxide generation was observed with an initial rate of 295 nmol min(-1) mg(-1). Electrochemical measurements of oxygen consumption and hydrogen peroxide formation yielded values of 650 and 355 nmol min(-1) mg(-1). In view of the ubiquitous distribution of aldehydes in tissues, aldehyde oxidase can be an important basal source of superoxide that would be enhanced in disease settings where cellular aldehyde levels are increased.     

Effect of hydrogen acceptors on D-xylose fermentation by anaerobic culture of immobilized Pachysolen tannophilus cells

The effect of hydrogen acceptors on the kinetic parameters of D-xylose fermentation under anaerobic conditions was studied in a transient culture of immobilized Pachysolen tannophilus cells. Addition of oxygen to a steady-state culture resulted in a rapid increase (up to fivefold) in the rates of ethanol production and D-xylose uptake, but the rate of xylitol production was unaffected. Furthermore, the molar ethanol yield increased from 0.97 to 1.43 in the presence of oxygen. The moles of ethanol produced per moles of oxygen utilized were considerably greater than would be predicted from the stoichiometry of D-xylose fermentation, which suggests that the organism required oxygen for other functions in addition to its role as a hydrogen acceptor in D-xylose metabolism. When the artificial hydrogen acceptors acetone, acetaldehyde, and acetoin were added to the culture, the rate of ethanol production increased while the xylitol production rate decreased but the rate of xylose uptake was unaffected. The molar ethanol yields increased from 1.03 to 1.63, 1.43, and 1.24 upon addition of acetaldehyde, acetone, and acetoin, respectively, at the expense of the molar xylitol yields. The hydrogen acceptors sodium acetate, methylene blue, benzyl viologen, phenazine methosulfate, indigo carmine, and tetrazolium chloride had no effect on ethanol production.     

The pH mediated effects of initial glucose concentration on the transitory occurrence of extracellular metabolites, gas exchange and growth yields of aerobic batch cultures of Klebsiella pneumoniae

The changes in growth kinetics in aerobic batch cultures of Klebsiella pneumoniae were followed by measurements of extracellular metabolites, rates of gas exchange, dissolved oxygen tension, pH, and carbon balance at all stages of growth. When the initial growth-limiting glucose concentration in media without pH control was increased from 1.0 g carbon L(-1) to 2.2 g carbon L(-1), the number of different, mainly acidic, extracellular metabolites of glucose at the end of exponential growth increased, while the proportion of acetate decreased. During the postexponential growth phase, the extracellular metabolites were oxidized, resulting in an increasing complexity of changes in pH, gas exchange, and dissolved oxygen tension with increasing initial substrate concentration. All these parameters showed concomitant stepwise changes. This pattern was independent of the dissolved oxygen tension in the range 30-200 muM. When pH was kept constant, the number, slope, and relative magnitude of the steps in gas exchange and dissolved oxygen tension were pH-dependent, being most complex at low pH. Detailed carbon balances showed that 20% of the initial glucose was converted into extracellular metabolites at the end of exponential growth at neutral pH. In the postexponential phase, pyruvate (2%) was reoxidized first followed by acetate (13%). The observed molar growth yield coefficient (Y(ATP)) was 8.4 if the transitory occurrence of pyruvate and acetate was accounted for, and 6.4 if it was neglected. The corrected observed molar growth yield coefficient (Y'(ATP)) was 9.4 and compared well with the true molar growth yield coefficient (Y(Max) (ATP)), which was found to be 11.0. Specific in situ respiration rates of the exponential growth phase of cultures grown at different controlled pH values compared well with in situ values for energy-limited chemostat grown cells at the same growth rates, suggesting that growth in the batch culture was energy-limited throughout the exponential growth phase. This view was supported by low levels of intracellular glycogen and exopolysaccharides of all cultures, by the value of Y'(ATP) of 9.4, and by a constant specific production rate of the extracellular metabolites throughout exponential growth. It was concluded that even under strictly aerobic conditions, control of pH is as important as control of dissolved oxygen tension during growth of enterobacteriaceae in batch cultures.     

Utility of culture redox potential for identifying metabolic state changes in amino acid fermentation

We investigated the relationship of dissolved oxygen and culture redox potential (CRP) on amino acid production. Corynebacterium glutamicum ATCC 14296 was used for all experiments. The fermentation can be divided into a growth phase and a production phase. Our results indicate that in order to get higher amino acid production, a lower oxygen supply during the exponential phase is favored. A higher oxygen supply rate appears to be necessary during the production phase. Culture redox potential (CRP) was used to monitor the fermentation. CRP readings were observed to drop to a characteristic minimum value as the metabolic state changed from a growth to production phase. This was evidenced by the commencement of amino acid production and a simultaneous uptake of lactate. Upon lactate exhaustion, the CRP increased abruptly. At the same time, maximal amino acid yields were observed. By the use of minimum CRP as an indication of metabolic phase changes, the agitation rate was changed to increase oxygen supply during the production phase. This significantly increased amino acid production. These results show that culture redox potential measurements can be used to monitor and optimize amino acid production by process manipulation.     

Continuous production of non-alcohol beer by immobilized yeast at low temperature

Summary A system for production of non-alcohol beer is described. A limited fermentation is carried out with immobilized cells ofSaccharomyces cerevisiae in a packed bed reactor. In the reactor, combined stress factors such as low temperature (2–4°C) and anaerobic conditions limit cell metabolism. Of the available sugars only a small amount of glucose is metabolized, resulting in low concentrations of ethanol (<0.08%). The absence of oxygen affects the redox balance of the yeast cell, and thus stimulates formation of esters and higher alcohols. Products are formed by reduction of wort aldehydes, as well as reduction of intracellular metabolites. Despite the stress conditions, biomass increases during prolonged production periods. In batch experiments,S. cerevisiae strain W34 grows at low temperatures and a mininum growth temperature of –2 °C was found, indicating that a further reduction of temperature during production will not inhibit growth. The characteristics of the system allow its use in very different applications. Potential applications of the immobilized system are discussed.This paper is dedicated to Professor Herman Jan Phaff in honor of his 50 years of active research which still continues.