A novel three-compartmented electrochemical bioreactor for enrichment of strict anaerobes based on metabolite production

In this study, a novel three-compartmented electrochemical bioreactor (3-CEB) was designed in an effort to overcome the disadvantages of the two-compartmented electrochemical bioreactor (2-CEB) separated with a cation-selective membrane for enrichment of strict anaerobes. The 3-CEB was comprised of an anode, outlet, and a cathode compartment. The outlet compartment was positioned between the anode and cathode compartment, and it was separated with the anode side by a rubber plate and with the cathode side by a porous glass membrane. A platinum wire bridging the anode and outlet compartment operated as a redox passage, however, through which no material could permeate. Butyrate fermentation bacteria were enriched on the basis of the metabolite production. Butyrate generated by strict anaerobes was significantly more abundant in the 3-CEB than in the 2-CEB. Acetic acid and lactic acid generated by facultative anaerobes was relatively higher in the 2-CEB than in the 3-CEB. Meanwhile, butyrate was not generated in the bioreactor utilized for the control test, to which the electrochemical potential was not charged. In a continuous culture using the 3-CEB, the majority of the glucose was fermented to butyrate, and the acetate additionally supplied to the bacterial culture was metabolically reduced to butyrate. More lactate than butyrate was generated from glucose in the 2-CEB.     

Nitrogen excretion of adult sheep fed silages made of a mixed sward or of pure unfertilised grass alone and in combination with barley

Four adult rumen-fistulated wether sheep were fed silages combined with barley. The silages consisted of 48% grasses, 28% legumes and 24% other forbs (GCF) or of pure grass (G). The swards received no mineral fertiliser. The dry matter (DM) and fibre contents were lower in GCF than in G. Crude protein content of DM in GCF and G were 145 g/kg and 102 g/kg respectively. DM content as ash, lipids and non-fibrous carbohydrates were rather similar in both silages. About 40g DM were offered per kg BW^0.75 and day either as silage alone or as a mixture of silage and barley (60:40). Faecal N excretion was greater with GCF than with G. The proportion of faecal bacterial and endogenous debris N reached 75 and 73% when GCF or G was fed, respectively. Undigested dietary N represented about 20%, and water soluble N accounted for 5–6% of faecal N. GCF caused more urinary N than G. Barley reduced urinary N excretion when supplemented to GCF. No dietary influence on urinary non-urea nitrogenous compounds was shown. GCF caused higher urinary urea N excretion than G and barley reduced this fraction when replacing part of GCF. Based on the urinary urea N proportions, it is concluded that N intake exceeded N requirement for any of the four diets fed. Dietary supplementation of ruminally fermentable carbohydrates can reduce urinary N excretion and this improves the efficiency of utilisation of N in N-unfertilised biodiverse grassland/ruminant farming systems.     

Biochemical and molecular characterization of thermo-alkali tolerant xylanase producing bacteria from thermal springs of Manikaran

1,2-Propanediol (propylene glycol) is an existing commodity chemical and can be produced from renewable resources using microbes. By virtue of being a natural product, relevant biochemical pathways can be harnessed into fermentation processes to produce 1,2-propanediol. In the present review, the chemical process and different biological strategies for the production of 1,2-propanediol are reviewed and compared with the potentials and limitations of all processes. For the successful commercial production of this diol, it is necessary to establish the metabolic pathways and production hosts (microorganisms), which are capable of delivering final product with high yields and volumetric productivity. Three pathways which have been recognized for 1,2-propanediol production are discussed here. In the first, de-oxy sugars like fucose and rhamnose are used as the carbon sources, while in the other route, the glycolytic intermediate-dihydroxyacetonephosphate (DHAP) is used to produce 1,2-propanediol via the formation of methylglyoxal. A new pathway of 1,2-propanediol production by lactic acid degradation under anoxic conditions and the enzymes involved is also discussed. The production of this diol has gained attention because of their newer applications in industries such as polymers, food, pharmaceuticals, textiles, etc. Furthermore, improvement in fermentation technology will permit its uses in other applications. Future prospect in the light of the current research and its potential as a major bulk chemical are discussed.     

Lactose metabolism in Lactobacillus curvatus and Lactobacillus sake

Abstract The lactose metabolism was investigated in five strains of Lactobacillus curvatus and 14 strains of L. sake isolated from meat or meat-derived products. Strains with the ability to ferment lactose were found in both species. They exhibited either phospho-β-galactosidase (P-β-gal) or β-galactosidase (β-gal) activity, or both. P-β-gal activity of L. curvatus and L. sake was induced and detected only in the presence of lactose or galactose. Furthermore, catabolite repression by glucose was demonstrated. The immunological properties of the P-β-gal enzymes of these organisms resemble those of Lactococcus lactis . Several strains of L. sake but none of L. curvatus exhibited β-gal activity which was constitutive. In hybridisation experiments, the β-gal genes of L. sake and L. casei ATCC393 showed over 60% DNA-homology. The presence of β-gal genes in L. sake was demonstrated in both β-gal-producing and non-producing strains. This observations is consistent with a genetic potential of lactic acid bacteria exceeding their physiological capabilities.     

Engineering aspects of solid state fermentation

Engineering aspects of solid state fermentation have not been available in spite of the recent interest in the technique and the appearance of a number of reviews on this subject. The present state of the art regarding substrate uptake, oxygen transfer, growth characteristics, growth estimation, control systems for maintaining parameters, mathematical models, design of fermenters and automation of fermentations does not provide a detailed insight. The work carried out at the Central Food Technological Research Institute, Mysore, on the development of a large-scale solid state fermenter, comparative cost estimation of SSF and submerged fermentation as well as development of know-how for production of a variety of food enzymes, has led to the commercial exploitation of the technology by industry. Future R&D needs in this area, neglected at present but yet so promising, are indicated.     

Continuous production of lactic acid from molasses by free and immobilized Sporolactobacillus cellulosolvens

Both free and immobilized cells of Sporolactobacillus cellulosolvens, in continuous culture on molasses (50 g sugar 1^-1) at 40°C, had maximum lactic acid productivities of 0.03 and 0.06 mol l^-1 h, at dilution rates of 0.27 and 0.25 h^-1, respectively.S.S. Kanwar is with the Department of Biotechnology, Guru Nanak Dev University, Amritsar-143 005, India; B.S. Chadha is with the Department of Microbiology, Guru Nanak Dev University, Amritsar-143 005, India. H.K. Tewari and V.K. Sharma are with the Department of Microbiology, Punjab Agricultural University, Ludhiana-141 004, India.     

Biotechnological Applications of Acetic Acid Bacteria

The acetic acid bacteria (AAB) have important roles in food and beverage production, as well as in the bioproduction of industrial chemicals. In recent years, there have been major advances in understanding their taxonomy, molecular biology, and physiology, and in methods for their isolation and identification. AAB are obligate aerobes that oxidize sugars, sugar alcohols, and ethanol with the production of acetic acid as the major end product. This special type of metabolism differentiates them from all other bacteria. Recently, the AAB taxonomy has been strongly rearranged as new techniques using 16S rRNA sequence analysis have been introduced. Currently, the AAB are classified in ten genera in the family Acetobacteriaceae. AAB can not only play a positive role in the production of selected foods and beverages, but they can also spoil other foods and beverages. AAB occur in sugar- and alcohol-enriched environments. The difficulty of cultivation of AAB on semisolid media in the past resulted in poor knowledge of the species present in industrial processes. The first step of acetic acid production is the conversion of ethanol from a carbohydrate carried out by yeasts, and the second step is the oxidation of ethanol to acetic acid carried out by AAB. Vinegar is traditionally the product of acetous fermentation of natural alcoholic substrates. Depending on the substrate, vinegars can be classified as fruit, starch, or spirit substrate vinegars. Although a variety of bacteria can produce acetic acid, mostly members of Acetobacter, Gluconacetobacter, and Gluconobacter are used commercially. Industrial vinegar manufacturing processes fall into three main categories: slow processes, quick processes, and submerged processes. AAB also play an important role in cocoa production, which represents a significant means of income for some countries. Microbial cellulose, produced by AAB, possesses some excellent physical properties and has potential for many applications. Other products of biotransformations by AAB or their enzymes include 2-keto-L-gulonic acid, which is used for the production of vitamin C; D-tagatose, which is used as a bulking agent in food and a noncalorific sweetener; and shikimate, which is a key intermediate for a large number of antibiotics. Recently, for the first time, a pathogenic acetic acid bacterium was described, representing the newest and tenth genus of AAB.     

Control of the production of individual fusicoccins at different dissolved oxygen concentrations

The regulatory effect of different concentrations of dissolved oxygen on the production of fusicoccins by the fungus Fusicoccum amygdali Del. was studied. The maximum output of total fusicoccins was obtained by using a profiled dissolved oxygen tension (DOT) regime, in which the DOT was maintained at 15–20% during the biomass growth phase and at 5–8% during the fusicoccins production phase. In comparison with the profiled regime, the maintenance of DOT at 15–20% during the whole fermentation shortened the fusicoccins production phase. The fermentation performance at a low DOT (5–8%) inhibited both the accumulation of biomass and the production of fusicoccins. At high DOT (40–50%), an accelerated accumulation of the biomass with an expressed autolysis of mycelia took place, and the production of fusicoccins was lowered. The qualitative composition of individual fusicoccins varied substantially at different DOTs. Fusicoccins, A, C, D, J, H, 16-O-demethyl-J, detretpentenylfusicoccin and some minor fusicoccin metabolites were found in the fermentation broth using the method of liquid secondary ion mass spectrometry. It was established that the profiled DOT regime (15–20% to 5–8%) provided both the maximum concentration of fusicoccins and an enhanced accumulation of the main metabolite – fusicoccin A (FC A). The performance of the fermentation at a DOT of 15–20% decreased the content of FC A by 2–6% in comparison with the profiled DOT regime, and increased the content of fusicoccin C to 14–20% of the total fusicoccins. Fermentation at DOT of 5–8% was characterized by the highest content of the precursors of FC A, the less oxidized fusicoccins H and J, the contents of which were in range 7–12% and 16–17% of total fusicoccins, respectively.     

Data acquisition and control of a continuous fermentation unit

Summary Data acquisition and computer control ofZymomonas mobilis fermentation for ethanol production has been studied. An HP 200 series microcomputer system was used in conjunction with an HP 3497A data acquisition unit. On-line ethanol, glucose and cell mass were measured for use as possible control variables. Dilution rate was used as the manipulative variable. A versatile, user-friendly data acquisition program was written to gather, control and analyze data from the continuous fermentation. The program allows user-given control and calibration algorithms so that sophisticated control policies, e.g., self-tuning regulator (STR) and instrumentation, can be implemented with relative ease.