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Effect of primary sludge fermentation products on mass balance for biological treatment.

Laboratory batch experiments were conducted at 20 degrees C to investigate the potential of primary sludge fermentation for the generation of readily biodegradable substrate and to evaluate the effect of fermentation products on mass balance for organic carbon, nitrogen and phosphorus, emphasizing COD fractionation. Fermentation converted between 18 to 30% of the initial volatile suspended solids in the sludge into soluble biodegradable COD. The volatile fatty fraction of the soluble COD was approximately 85% after the fermentation process. The average volatile fatty acid composition in fermentation involved 50% acetic acid, 33% propionic acid, 9% butyric acid and 8% valeric acid, indicating that the most important volatile fatty acid obtained during the biological fermentation process was acetate with more than half of total VFA concentration, which is one of the most important carbon sources for denitrification and biological nutrient removal processes. The recoverable fraction of the fermented sludge supernatant could potentially increase the readily biodegradable COD content of the primary effluent by 5%, together with a potential increase of the soluble nitrogen and phosphorus content by 2%.

Fatty Acids, Volatile↗

[Effect of pH value on fermentation pathways of biodegradable organic waste].

Batch reactors were set up to evaluate the effect of pH value on the anaerobic fermentation of biodegradable organic waste. The results show that pH=7 of fermentative media is favorable for the microbial growth and proliferation, thereby promoting hydrolysis and acidogenesis of particulate biodegradable organic waste. The predominant fermentation types are diverse at different pH value, butyric acid fermentation dominates at pH=7, and at the later phase of pH= 8, propionic acid fermentation dominates at the later phase of pH=5. Lactic acid is produced at the early phase of fermentation, but gradually degrades at pH=5 and pH=7, while remains constant at pH=8. The predominant metabolic pathway shifts from alcohol-forming pathway to acid-forming pathway except for pH=5, where alcoholic fermentation still dominates at the later phase. The first-order hydrolysis constants k(h) for pH 5, 7 and 8 are equal to 0.000 8 h(-1), 0.000 9 h(-1) and 0.0002 h(-1), respectively. The soluble total organic carbon is mainly composed of acidogenic products after 100 h, 300 h and 600 h for pH=7, 5 and 8, respectively.

Acetic Acid↗

[Effect of a novel soy fermented product enriched with isoflavones and calcium on bone tissue of rats].

The objective was to evaluate the effect of soy fermented product intake on the corporal weight and bone tissue of ovariectomized mature rats. This product was fermented with Enterococcus faecium and Lactobacillus jugurti and enriched with isoflavones and calcium. The animals were divided in 5 groups: sham-ovariectomized; ovariectomized; ovariectomized treated with soy fermented product enriched with isoflavones and calcium; ovariectomized treated with soy fermented product enriched with calcium and ovariectomized treated with non-fermented product enriched only with calcium. In order to evaluate the effect of the tested product on bone tissue (femur and tibia), the following parameters were analyzed: length; mechanical assay of three points; density (Archimedes principle); mineral content; calcium content; measure of the trabecular widths. The corporal weight of group treated with soy fermented product containing isoflavones and calcium showed no statistical difference from sham-ovariectomized group and trabecular widths tended to have larger than ovariectomized group. However, there was no significant difference to the other evaluated parameters in result of the diverse treatments. Thus, soy fermented product enriched with isoflavones and calcium inhibited the increasing of corporal weight caused by ovariectomy and revealed a tendency to trabecular protection after castration.

Animals↗

[Properties of mitochondria from cells of the "fermentative" variant of Endomyces magnusii].

The properties of mitochondria from the cells of the "fermentative" variant of End. magnusii were studied. The induced fermentative transformation was brought about by a non-balanced vitamin cultivation. It was shown that the "fermentative" variant of End. magnusii represents an interesting model, in which the energy required for the cell functioning is provided for by a high fermentative activity and a normally functioning respiratory chain. The "fermentative" variant mitochondria were tightly coupled and possessed theoretical efficiency during oxidation of NAD-dependent substrates, which suggested the existence of all the three sites of energy coupling and phosphorylation at the substrate level. A specificity of energy regulation of the End. magnusii "fermentative" variant mitochondria, e. g. tight coupling during oxidation of succinate and lack of tight coupling during oxidation of exogenous NADH, is discussed. The tight coupling during succinate oxidation is confirmed by the observation of reverse electron transfer. Thus, the energy-dependent reduction of NAD during succinate oxidation has been firstly demonstrated for the mitochondria of yeast grown on a fermentable substrate.

Ascomycota↗

Dietary fibre, fermentation and large bowel cancer.

Diet, especially the amount of starch and dietary fibre which escape digestion in the small intestine, are major determinants of colon function in man. These carbohydrates are the principal substrates for fermentation by the large bowel flora. Carbohydrate fermentation results in lowered caecal pH and the production of short chain fatty acids of which butyric acid may protect the colon epithelium from dysplastic change. Protein digestion and amino acid fermentation also occur in the large bowel but the nature of its endproducts varies in relation to the amount of carbohydrate available. During active carbohydrate breakdown amino acid fermentation endproducts such as ammonia are used by the bacteria for protein synthesis during microbial growth, but in carbon-limited fermentation amines, ammonia, phenols and indoles, etc, accumulate. Fermentation also results in changes in colon pH which alters the metabolism of bile acids, nitrate, sulphate and other substances. Fermentation is thus controlled to a great extent by substrate availability, especially of carbohydrates which are derived from the diet. The potential to induce mutagenic change in colon epithelial cells and promote tumour growth may readily be influenced by diet.

Ammonia↗

Hypocholesterolaemic effect of a new fermented milk product in healthy middle-aged men.

OBJECTIVE: There are still controversies as to the potential beneficial effects of milk and fermented milk products on the level of lipoproteins. The objective of the present investigation was to test the effect of a moderate daily intake of a new fermented milk product, which was based on a bacterial culture obtained from the intestinal flora of inhabitants of Abkhasia, on the lipoprotein levels of a homogeneous group of middle-aged Danish men. DESIGN: The study was randomised, double-blind, and placebo-controlled, and the intervention was performed for a period of 6 weeks. SUBJECTS: Fifty-eight healthy, non-obese, normocholesterolaemic, male volunteers born in 1949 of Danish descent participated (i.e. all were 44 years old). INTERVENTIONS: During the intervention period the subjects' habitual diets were supplemented with 200 ml/day of either the new fermented milk product or a placebo product (chemically fermented). The biologically fermented milk product contained Enterococcus faecium and two strains of Streptococcus termophilus. Fasting blood samples were drawn initially and after 3 and 6 weeks and analysed for plasma values of total cholesterol, high-density lipoprotein (HDL)-cholesterol and triglyceride. In addition, LDL-cholesterol was estimated. RESULTS: After these 6 weeks total cholesterol was reduced significantly in the group given biologically fermented milk (-0.37 mmol/l, confidence interval: -0.51 to -0.23) while no changes were observed in the placebo group (-0.02 mmol/l) (P < 0.01). This reduction in total cholesterol could be completely ascribed to a fall in LDL-cholesterol by 10% (i.e. -0.42 mmol/l) since HDL-cholesterol and triglyceride were unchanged in both groups. CONCLUSIONS: Thus, this short-term study (6 weeks) demonstrated an LDL-cholesterol-lowering effect (10% reduction) of a new fermented milk product in middle-aged Danish men.

Adult↗

Digestion, absorption, and fermentation of carbohydrates in the newborn.

In the newborn, sugars present in human milk and formulas are assimilated by both small intestinal digestion and, especially in the case of lactose, colonic bacterial fermentation. Colonic fermentation of carbohydrate serves three major functions: (1) conservation of a fraction of the metabolizable energy of dietary carbohydrate that is not absorbed in the small intestine; (2) prevention of osmotic diarrhea; and (3) production of short-chain fatty acids that stimulate sodium and water absorption, serve as fuel for colonocytes, and stimulate cell replication in colon and small intestine. Diarrhea produced in association with small bowel malabsorption of sugar may be caused by three, potentially overlapping mechanisms: (1) osmotic effects of unfermented sugar, which may cause secondary disruption of fermentation by purging the bacteria or diluting the bacteria mass; (2) damage to the colon mucosa from excessive fermentation leading to SCFA malabsorption and osmotic diarrhea on this basis; and (3) excessive fermentation leading to lowering of luminal pH and inhibition of bacterial enzymes. Therapy aimed at reducing diarrhea associated with sugar malabsorption might involve either slowing of motility to facilitate fermentation or stimulation of fermentative activity, but such interventions would depend on greater understanding of the mechanisms for colonic dysfunction in this condition.

Bacteria↗

Pulsed feeding during fed-batch fungal fermentation leads to reduced viscosity without detrimentally affecting protein expression.

The goal in this study was to determine if pulsed addition of substrate could be used to alter filamentous fungal morphology during fermentation, to result in reduced broth viscosity. In all experiments, an industrially relevant strain of Aspergillus oryzae was grown in 20-liter fermentors. As a control, cultures were fed limiting substrate (glucose) continuously. Tests were performed by altering the feeding strategy so that the same total amount of glucose was fed in repeated 300-s cycles, with the feed pump on for either 30 or 150 s during each cycle. Variables indicative of cellular metabolic activity (biomass concentration, oxygen uptake rate, base consumed for pH control) showed no significant difference between continuous and pulse-fed fermentations. In addition, there was no significant difference between total extracellular protein expression or the apparent distribution of these proteins. In contrast, fungal mycelia during the second half of pulse-fed fermentations were approximately half the size (average projected area) of fungi during fermentations with continuous addition of glucose. As a result, broth viscosity during the second half of pulse-fed fermentations was approximately half that during the second half of continuous fermentations. If these results prove to be applicable for other fungal strains and processes, then this method will represent a simple and inexpensive means to reduce viscosity during filamentous fungal fermentation.

Aspergillus oryzae↗

Extractive fermentation for butyric acid production from glucose by Clostridium tyrobutyricum.

A novel extractive fermentation for butyric acid production from glucose, using immobilized cells of Clostridium tyrobutyricum in a fibrous bed bioreactor, was developed by using 10% (v/v) Alamine 336 in oleyl alcohol as the extractant contained in a hollow-fiber membrane extractor for selective removal of butyric acid from the fermentation broth. The extractant was simultaneously regenerated by stripping with NaOH in a second membrane extractor. The fermentation pH was self-regulated by a balance between acid production and removal by extraction, and was kept at approximately pH 5.5 throughout the study. Compared with conventional fermentation, extractive fermentation resulted in a much higher product concentration (>300 g/L) and product purity (91%). It also resulted in higher reactor productivity (7.37 g/L. h) and butyric acid yield (0.45 g/g). Without on-line extraction to remove the acid products, at the optimal pH of 6.0, the final butyric acid concentration was only approximately 43.4 g/L, butyric acid yield was 0.423 g/g, and reactor productivity was 6.77 g/L. h. These values were much lower at pH 5.5: 20.4 g/L, 0.38 g/g, and 5.11 g/L. h, respectively. The improved performance for extractive fermentation can be attributed to the reduced product inhibition by selective removal of butyric acid from the fermentation broth. The solvent was found to be toxic to free cells in suspension, but not harmful to cells immobilized in the fibrous bed. The process was stable and provided consistent long-term performance for the entire 2-week period of study.

Bioreactors↗

Inhibitory effect of fermented milk on delayed-onset muscle damage after exercise.

Milk fermented with a starter containing Lactobacillus helveticus and Saccharomyces cerevisiae is drunk on a daily basis by many people in Japan and has several beneficial effects. We studied the influence of this fermented milk product on muscle damage after prolonged exercise in rats. Wistar rats were divided into four groups: rested controls, rested rats given fermented milk diet, exercised rats and exercised rats given fermented milk diet. After 3 weeks of acclimatization, both exercise groups were made to run on a treadmill at 26 m/min for 60 min. Exercise increased the serum creatine kinase level, as well as myeloperoxidase activity and the level of thiobarbituric-acid-reactive substances in the gastrocnemius muscle after 24 h. These changes were ameliorated by intake of fermented milk. An increase of CINC-1 was also ameliorated by fermented milk. Furthermore, milk diet increased the mRNA and protein levels of protective proteins such as antioxidants and chaperone proteins. These results indicate that fermented milk can ameliorate delayed-onset muscle damage after prolonged exercise, which is associated with an increased antioxidant capacity of muscles.

Animals↗

Carbohydrate fermentation by three species of polycentric ruminal fungi from cattle and water buffalo in tropical Australia.

Fructose, glucose and xylose were the only monosaccharides to be fermented by the polycentric fungi, Orpinomyces joyonii (three cattle isolates) and O. intercalaris (two cattle isolates) and Anaeromyces spp. (four cattle isolates and two water buffalo isolates). Both Orpinomyces spp. utilised a similar range of oligosaccharides and polysaccharides by fermenting cellobiose, gentiobiose, lactose, maltose, sucrose, cellulose, glycogen, starch and xylan. In contrast, there was considerable variation in carbohydrate fermentation amongst Anaeromyces spp., with only cellobiose, gentiobiose and cellulose being fermented by all strains. Formate, acetate and ethanol were the major fermentation end-products formed from glucose by all polycentric fungi. In addition, Anaeromyces spp. produced considerable amounts of lactate, although only small amounts were formed by Orpinomyces spp. This difference was explained by the low specific activity for lactate dehydrogenase in Orpinomyces spp. Several Anaeromyces spp. also produced malate as a significant end-product of glucose fermentation. Fermentation of specifically-labelled Z14C]glucose molecules by polycentric fungi showed that hexose was catabolised by both polycentric and monocentric fungi via the glycolysis pathway with end-products being derived from the following carbon atoms: lactate and malate (C1-C3; C4-C6), acetate and ethanol (C1-C2; C5-C6), CO2 and formate (C3; C4). The results were compared to those obtained for monocentric and polycentric fungi isolated from temperate climate ruminants.

Journal Article↗

Production of cell-free xanthan fermentation broth by cell adsorption on fibers

Xanthan gum is a microbial polysaccharide widely used in food and oil-drilling industries. Xanthan gum produced from the current commercial fermentation process usually contains cells and cell debris, which lower the filterability of the xanthan solution and limit its applications. The production of cell-free xanthan gum fermentation broth is thus desirable. The feasibility of removing cells from the xanthan fermentation broth by cell adsorption to various woven fibrous materials was studied. It was found that both cotton and polyester fibers could be used to adsorb Xanthomonas campestris cells present in the fermentation broth either during batch fermentation or after the fermentation. Almost all cells were removed from the fermentation broth by adsorption to fibers. Cotton terry cloth had rough surfaces and was the preferred material for cell adsorption. Cell adsorption to cotton was faster than to polyester fibers. The adsorption kinetics can be modeled by a first-order rate equation. The adsorption rate constants were 30-40% higher for cotton than for polyester. Cell adsorption was not efficient in the absence of xanthan gum, suggesting that the exopolysaccharide, xanthan gum, was important for efficient cell adsorption to fibers.

Journal Article↗

Production of amylases from rice by solid-state fermentation in a gas-solid spouted-Bed bioreactor

A gas-solid spouted-bed bioreactor was developed to produce amylases from rice in solid-state fermentation by Aspergillus oryzae. The spouted-bed bioreactor was developed to overcome many of the problems inherent to large-scale solid-state fermentation, including mass- and heat-transfer limitations in the conventional tray reactors and solids-handling difficulties seen in packed-bed bioreactors. The solid-state fermentation results from the tray-type reactor with surface aeration were poor because of mass- and heat-transfer problems. A packed-bed bioreactor with continuous aeration through the rice bed produced high protein and enzymes, but the fermented rice was difficult to remove and process due to the formation of large chunks of rice aggregates knitted together with fungal mycelia. Also, the fermentation was not uniform in the packed bed. The spouted-bed bioreactor with intermittent spouting with air achieved high production levels in both total protein and enzymes (alpha-amylase, beta-amylase, and glucoamylase) that were comparable to those found in the packed-bed bioreactor, but without the nonuniformity and solids-handling problems. However, continual spouting was found to be detrimental to this solid-state fermentation, possibly because of shear or impact damage to fungal mycelia during spouting. Increasing spouting frequency from 4-h intervals to 1-h intervals decreased protein and enzyme production. Other operating conditions critical to the fermentation include proper humidification to prevent drying of the substrate and control of reactor wall temperature to prevent excessive condensation, which would interfere with proper spouting.

Journal Article↗

Immobilized yeast bioreactor systems for continuous beer fermentation

Two different types of immobilized yeast bioreactors were examined for continuous fermentation of high-gravity worts. One of these is a fluidized bed reactor (FBR) that employs porous glass beads for yeast immobilization. The second system is a loop reactor containing a porous silicon carbide cartridge (SCCR) for immobilizing the yeast cells. Although there was some residual fermentable sugar in the SCCR system product, nearly complete attenuation of the wort sugars was achieved in either of the systems when operated as a two-stage process. Fermentation could be completed in these systems in only half the time required for a conventional batch process. Both the systems showed similar kinetics of extract consumption, and therefore similar volumetric productivity. As compared to the batch fermentation, total fusel alcohols were lower; total esters, while variable, were generally higher. The yeast biomass production was similar to that in a conventional fermentation process. As would be expected in an accelerated fermentation system, the levels of vicinal diketones (VDKs) were higher. To remove the VDKs, the young beer was heat-treated to convert the VDK precursors and processed through a packed bed immobilized yeast bioreactor for VDK assimilation. The finished product from the FBR system was found to be quite acceptable from a flavor perspective, albeit different from the product from a conventional batch process. Significantly shortened fermentation times demonstrate the feasibility of this technology for beer production.

Journal Article↗

Reactor Design Issues for Synthesis-Gas Fermentations.

Synthesis gas is readily obtained by gasifying coal, oil, biomass, or waste organics and represents an abundant, potentially inexpensive, feedstock for bioprocessing. The primary components of synthesis gas, carbon monoxide and hydrogen, can be converted into methane, organic acids, and alcohols via anaerobic fermentations. Bioconversion of synthesis gas is an attractive alternative to catalytic processing because the biological catalysts are highly specific and often more tolerant of sulfur contaminants than inorganic catalysts. However, because the aqueous solubilities of carbon monoxide and hydrogen are low, synthesis-gas fermentations are typically limited by the rate of gas-to-liquid mass transfer. Consequently, a major engineering challenge in commercial development of synthesis-gas fermentations is to provide sufficient gas mass transfer in an energy-efficient manner. This paper reviews recent progress in the development of synthesis-gas fermentations, with emphasis on efforts to increase the efficiency of gas mass transfer. Metabolic properties of several microbes able to ferment synthesis gas are described. Results of synthesis-gas fermentations conducted in various bioreactor configurations are summarized. Recent results showing enhancement of synthesis-gas fermentations using microbubble dispersions are presented, and studies of the mass-transfer and coalescence properties of microbubbles are described.

Journal Article↗

Indonesian tapé ketan fermentation.

Indonesian tapé ketan is a fermentation in which a mold, Amylomyces rouxii Calmette (Chlamydomucor oryzae Went and Prinsen Geerligs), in combination with one or more yeasts such as Endomycopsis burtonii converts steamed rice to a sweet-sour, slightly alcoholic paste. A study was made to determine the biochemical changes that occur in the substrate during fermentation. It was found that the product was ready for consumption after fermentation at 30 degrees C for 36 to 48 h. A. rouxii used about 30% of the total rice solids, resulting in a crude protein of 12% in 96 h, whereas the combination of the mold with E. burtonii reduced total solids by 50% in 192 h, causing crude protein to increase to 16.5%. Soluble solids increased from 5 to about 67% in 36 h and decreased to 12% at 192 h with A. rouxii alone, whereas soluble solids fell to about 8% at 192 h in the fermentation with both the mold and the yeast. The mold, by itself, reduced the starch content of the rice from 78 to 10% in 48 h and to less than 2% in 144 h. The mold plus yeast reduced the starch content to about 18% in 48 h; however the "starch" content did not fall below 6% even at 192 h, presumably because the yeast was producing glycogen, which was determined along with the residual starch. With both the mold and the mold plus yeast fermentations, reducing sugars increased from less than 1% to approximately 5% in 24 h and reached maximum concentration, 16 to 17%, between 36 and 48 h. A. rouxii by itself produced a maximum of about 5.6% (vol/vol) ethanol at 96 h. The highest concentration of ethanol (8%, vol/vol) was produced by the mold plus E. burtonii at 144 h. The mold by itself reduced the starting pH from 6.3 to about 4.0 in 48 h. The combination of the mold and yeast reduced the pH to 4.1 in 144 h. The mold increased total acidity to approximately 6.2 meq of H per 100 ml, and the combination of the mold and yeast increased the total acidity to 7.8 meq of H per 100 ml in 192 h. At 48 h there was practically no difference in the volatile acidity (0.20) for the combined fermentation compared with 0.26 meq of H per 100 ml for the mold fermentation. The mold and at least one species of yeast were required to develop the rich aroma and flavor of typical Indonesian tapé.

Journal Article↗

Fermentation of aqueous plant seed extracts by lactic Acid bacteria.

The effects of lactic acid bacterial fermentation on chemical and physical changes in aqueous extracts of cowpea (Vigna unguiculata), peanut (Arachis hypogea), soybean (Glycine max), and sorghum (Sorghum vulgare) were studied. The bacteria investigated were Lactobacillus helveticus, L. delbrueckii, L. casei, L. bulgaricus, L. acidophilus, and Streptococcus thermophilus. Organisms were inoculated individually into all of the seed extracts; L. bulgaricus and S. thermophilus were also evaluated together as inocula for fermenting the legume extracts. During fermentation, bacterial population and changes in titratable acidity, pH, viscosity, and color were measured over a 72-h period at 37 degrees C. Maximum bacterial populations, titratable acidity, pH, and viscosity varied depending upon the type of extract and bacterial strain. The maximum population of each organism was influenced by fermentable carbohydrates, which, in turn, influenced acid production and change in pH. Change in viscosity was correlated with the amount of protein and titratable acidity of products. Color was affected by pasteurization treatment and fermentation as well as the source of extract. In the extracts inoculated simultaneously with L. bulgaricus and S. thermophilus, a synergistic effect resulted in increased bacterial populations, titratable acidity, and viscosity, and decreased pH in all the legume extracts when compared to the extracts fermented with either of these organisms individually. Fermented extracts offer potential as substitutes for cultured dairy products.

Journal Article↗

Influence of Calcium Ion on Ethanol Tolerance of Saccharomyces bayanus and Alcoholic Fermentation by Yeasts.

The addition of Ca (as CaCl(2)) in optimal concentrations (0.75 to 2.0 mM) to a fermentation medium with a trace contaminating concentration of Ca (0.025 mM) led to the rapid production of higher concentrations of ethanol by Saccharomyces cerevisiae, Saccharomyces bayanus, and Kluyveromyces marxianus. The positive effect of calcium supplementation (0.75 mM) on alcoholic fermentation by S. bayanus was explained by the increase in its ethanol tolerance. The ethanol inhibition of growth and fermentation followed the equation mu(xi) = mu(oi) [1 - (X/X(mi))], where mu(oi) and mu(xi) are, respectively, the specific growth (i = g) and fermentation (i = f) rates in the absence or presence of a concentration (X) of added ethanol, and X(mi) is the maximal concentration of ethanol which allows growth or fermentation. The toxic power is given by n(i). In Ca - supplemented medium (0.75 mM), n(g) = 0.42 for growth and n(f) = 0.43 for fermentation compared with 0.52 and 0.55, respectively, in unsupplemented medium; for both media, X(mg) = 10% (vol/vol) and X(mf) = 13% (vol/vol). For lethal concentrations of ethanol, the specific death rates were minimal for cells that were grown and incubated with ethanol in medium with an optimal concentration of Ca, maximal for cells grown and incubated with ethanol in unsupplemented medium, and intermediate for cells grown in unsupplemented medium and incubated with ethanol in calcium-supplemented medium. The effect of Ca on the acidification curve of energized cells in the presence of ethanol was found to be closely associated with its protective effect on growth, fermentation, and viability.

Journal Article↗