Increased production of bacteriocin ST4SA byEnterococcus mundtii ST4SA in modified corn steep liquor

Enterococcus mundtii ST4SA produces a broad-spectrum bacteriocin (bacST4SA), active against Gram-positive and Gramnegative bacteria. Growth in corn steep liquor (CSL) with a sugar content of 5.0 and 10.0 g/l yielded bacST4SA levels of 12800 AU/ml. A four-fold increase in bacST4SA production (51200 AU/ml) was recorded in CSL with a sugar content of 7.5 g/l supplemented with 6.5 g/l yeast extract (CSL-YE). Poor growth and low levels of bacST4SA production were observed when cells were grown in CSL-YE controlled at pH 5.5. Fermentation at pH 7.5 yielded 25600 AU/ml after 6 h, but the activity levels decreased to approximately 1000 AU/ml during the next 6 h. Adjustment of the culture pH from 6.5 to 5.5 after 6 h of fermentation extended bacST4SA activity (51200 AU/ml) over 8 h. Activity then decreased to 25600 AU/ml and was maintained this level for 10 h. Optimal levels of bacST4SA production (102400 AU/ml) were obtained after 6 h of fermentation in CSL-YE supplemented with 7.5 g/l glucose at the start of the fermentation. This level of production was maintained by changing the culture pH from 6.5 after 6 h of fermentation to pH 5.5. This study proved that bacST4SA could be produced at high levels in an inexpensive industrial medium byE. mundtii ST4SA.     

High nisin Z production by Lactococcus lactis UL719 in whey permeate with aeration

The influence of controlled pH (5.0–6.5) and initial dissolved oxygen level (0–90% air saturation) on nisin Z production in a yeast extract/Tween 80-supplemented whey permeate (SWP) was examined during batch fermentations with citrate positive Lactococcus lactis subsp. lactis UL719. The total activity corresponding to the sum of soluble and cell-bound activities, as measured by a critical dilution method, was more than 50% lower at pH 5.0 than in the range 5.5–6.5, although the specific production decreased as pH increased. A maximum nisin Z activity of 8200 AU/ml (4100IU/ml) was observed in the supernatant after 8h of culture for pH ranging from 5.5 to 6.5. Prolonging the culture beyond 12h decreased this activity at pH 6.0 and 6.5 but not at pH 5.5 or 5.0. A corresponding increase in cell-bound activity was probably due to adsorption of soluble bacteriocin to the cell wall. Aeration increased cell-bound and total activity to maximum values of 32800 and 41000 AU/ml (16400 and 20500IU/ml), respectively, with an initial level of 60% air saturation after 24h of incubation at pH 6.0. The specific production at 60% or 90% initial air saturation was eight-fold higher than at 0%.     

Effect of medium components on bacteriocin production by Lactobacillus plantarum strains ST23LD and ST341LD, isolated from spoiled olive brine

Bacteriocin ST23LD levels of 2930AU/OD were recorded in MRS broth (pH of 6.5) and in the presence of tryptone and yeast extract as sole nitrogen sources. Growth in MRS broth at an initial pH of 6.0 yielded only 1460AU/OD bacteriocin ST23LD. Activities of 5861AU/OD were recorded with maltose (20, 30 and 40 g/l) as sole carbon source and 9036AU/OD with the addition of 2.0-10.0 g/l KH2PO4. Bacteriocin ST341LD levels of 2850 and 2841AU/OD were recorded in MRS broth at an initial pH of 6.0 or 5.5, respectively. Only 709AU/OD was recorded in the same medium with an initial pH of 6.5. Bacteriocin ST341LD production was stimulated by the presence of tryptone. However, glucose at 10 and 40 g/l, or the presence of 5.0 or 10.0 g/l K2HPO4, resulted in a 50% reduction of bacteriocin activity. Glycerol in the growth medium repressed bacteriocin production. No increased bacteriocin production was recorded in medium supplemented with vitamins.     

Effect of pH on organic acid production byClostridium propionicum in test tube and fermentor cultures

Summary Clostridum propionicum is a chemical autotroph that metabolizes alanine to propionic acid (reduction product) and acetic acid (oxidation product). The ratio of propionate/acetate predicted by the electron balance is 2:1. This study reports the effect of pH on growth and organic acid production by this organism when grown in both test tube cultures initially buffered from pH 7.0 to 5.0, and in fermentors maintained at pH 7.0 and 6.5. Highest growth and organic acid production was found at pH 7.0 in both cases. HPLC analysis showed that at pH 7.0, the ratios of propionate to acetate were 0.45:1 (stationary tube, 24 h). The highest ratio observed was 1.8:1 (stationary tube, pH 6.0, 24h). This tube produced 8.5% of the acids produced in the pH 7.0 culture tube. The identify of the major portion of the reduction products of the organism remains unknown.     

Factors influencing biohydrogenation and conjugated linoleic acid production by mixed rumen fungi

The objective of this study was to evaluate the effect of soluble carbohydrates (glucose, cellobiose), pH (6.0, 6.5, 7.0), and rumen microbial growth factors (VFA, vitamins) on biohydrogenation of linoleic acid (LA) by mixed rumen fungi. Addition of glucose or cellobiose to culture media slowed the rate of biohydrogenation;only 35-40% of LA was converted to conjugated linoleic acid (CLA) or vaccenic acid (VA) within 24 h of incubation, whereas in the control treatment, 100% of LA was converted within 24 h. Addition of VFA or vitamins did not affect biohydrogenation activity or CLA production. Culturing rumen fungi at pH 6.0 slowed biohydrogenation compared with pH 6.5 or 7.0. CLA production was reduced by pH 6.0 compared with control (pH 6.5), but was higher with pH 7.0. Biohydrogenation of LA to VA was complete within 72 h at pH 6.0, 24 h at pH 6.5, and 48 h at pH 7.0. It is concluded that optimum conditions for biohydrogenation of LA and for CLA production by rumen fungi were provided without addition of soluble carbohydrates, VFA or vitamins to the culture medium; optimum pH was 6.5 for biohydrogenation and 7.0 for CLA production.     

Effect of pH and buffer on butyric acid production and microbial community characteristics in bioconversion of rice straw with undefined mixed culture

This study was conducted to identify the optimum pH range and the appropriate buffer for butyric acid production from rice straw by fermentation using an undefined mixed culture. A series of experiments conducted at pH levels of 5.0 ~ 7.0 showed that neutral pH improved rice straw conversion and consequently carboxylic acid production. The highest butyric acid production (up to 6.7 g/L) was achieved at pH of 6.0 ~ 6.5, while it was only 1.7 g/L without pH control or at pH 5.0. Another series of experiments conducted at pH 6.0 ~ 6.5 buffered with CaCO₃, NaHCO₃, NH₄HCO₃ and their combinations indicated that different buffers had different effects onthe product spectrum, and that CaCO₃ combined with NaHCO₃ was an effective buffer for butyric acid production. The highest total volatile fatty acids (about 12.6 g/L) production and one of the two highest butyric acid concentrations (about 7.6 g/L) were obtained by buffering with CaCO₃ combined with NaHCO₃. PCR-DGGE analysis revealed that different pH and buffers also influenced the microbial population distribution. Bacteria were suppressed at low pH, while the bacterial community structures at higher pH varied slightly. Overall, this study presents an alternative method for butyric acid production from lignocellulosic biomass without supplementary cellulolytic enzyme.     

Dissolved-oxygen-stat fed-batch fermentation of 1,3-dihydroxyacetone from glycerol by Gluconobacter oxydans ZJB09112

This study investigated the effects of DO concentration on DHA fermentation and of DO-stat fed-batch fermentation using a pH control strategy, on 1,3-dihydroxyacetone (DHA) production. The results showed that DO-stat fed-batch fermentation with pH-shift control was the optimal bioprocess for DHA production. DO-stat fed-batch fermentation was carried out at 30% air saturation, and the culture pH was automatically maintained at pH 6.0 during the first 20 h and then shifted to pH 5.0 until the end of the fermentation. An optimal DHA concentration of 175.9 ± 6.7 g/L, with a production yield to glycerol of 0.87 ± 0.04 g/g, was obtained at 72 h of DO-stat fed-batch fermentation at 30°C in a 15 L fermenter.     

Cell Expansion and Tracheary Element Differentiation Are Regulated by Extracellular pH in Mesophyll Cultures of Zinnia elegans L

The effects of medium pH on cell expansion and tracheary element (TE) differentiation were investigated in differentiating mesophyll suspension cultures of Zinnia elegans L. In unbuffered cultures initially adjusted to pH 5.5, the medium pH fluctuated reproducibly, decreasing about 1 unit prior to the onset of TE differentiation and then increasing when the initiation of new Tes was complete. Elimination of large pH fluctuations by buffering the culture medium with 20 mM 2-(N-morpholino)ethanesulfonic acid altered both cell expansion and TE differentiation, whereas altering the starting pH of unbuffered culture medium had no effect on either process. Cell expansion in buffered cultures was pH dependent with an optimum of 5.5 to 6.0. The direction of cell expansion was also pH dependent in buffered cultures. Cells elongated at pH 5.5 to 6.0, whereas isodiametric cell expansion was predominant at pH 6.5 to 7.0. The onset of TE differentiation was delayed when the pH was buffered higher or lower than 5.0. However, TEs eventually appeared in cultures buffered at pH 6.5 to 7.0, indicating that a decrease in pH to 5.0 is not necessary for differentiation. Very large TEs with secondary cell wall thickenings resembling metaxylem differentiated in cultures buffered at pH 5.5 to 6.0, which also showed the greatest cell expansion. The correlation between cell expansion and delayed differentiation of large, metaxylem-like TEs may indicate a link between the regulatory mechanisms controlling cell expansion and TE differentiation.     

Influence of growth conditions on the production of a nisin-like bacteriocin by Lactococcus lactis subsp. lactis A164 isolated from kimchi

The influence of growth parameters on the fermentative production of a nisin-like bacteriocin by Lactococcus lactis subsp. lactis A164 isolated from kimchi was studied. The bacteriocin production was greatly affected by carbon and nitrogen sources. Strain A164 produced at least 4-fold greater bacteriocin in M17 broth supplemented with lactose than other carbon sources. The amount of 3% yeast extract was found to be the optimal organic nitrogen source. While the maximum biomass was obtained at 37 degrees C, the optimal temperature for the bacteriocin production was 30 degrees C. The bacteriocin production was also affected by pH of the culture broth. The optimal pH for growth and bacteriocin production was 6.0. Although the cell growth at pH 6.0 was nearly the same level at pH 5.5 and 6.5, the greater bacteriocin activity was observed at pH 6.0. Exponential growth took place only during an initial period of the cultivation, and then linear growth was observed. Linear growth rates increased from 0.160 g(DCW) x l(-1) x h(-1) to 0.245 g(DCW) x l(-1) x h(-1) with increases in lactose concentrations from 0.5 to 3.0%. Maximum biomass was also increased from 1.88 g(DCW) x l(-1) to 4.29 g(DCW) x l(-1). However, increase in lactose concentration did not prolong the active growth phase. After 20 h cultivation, cell growth stopped regardless of lactose concentration. Production of the bacteriocin showed primary metabolic kinetics. However, bacteriocin yield based on cell mass increased greatly during the late growth phase. A maximum activity of 131x10(3) AU x ml(-1) was obtained at early stationary growth phase (20 h) during the batch fermentation in M17L broth (3.0% lactose) at 30 degrees C and pH 6.0.     

Production of high level of cellulase-free and thermostable xylanase by a wild strain of Thermomyces lanuginosus using beechwood xylan

Thermomyces lanuginosus, isolated from self-heated jute stacks in Bangladesh, was studied for production of high level of cellulase-free thermostable xylanase at 50°C using xylan. Optimization of the medium composition was carried out on shake-flask level using Graeco-Latin square technique. This increased xylanase production from 527 nkat ml⁻¹ in the original medium to 9168–9502 nkat ml⁻¹ in the optimized medium under optimized culture conditions e.g. initial medium pH (6.0–6.5), culture temperature (50°C) and time (5–6 d). The lag phase was very much shorter in the laboratory reactor compared to which existed in the shake cultures and 7111 nkat of xylanase activity were obtained per ml of culture filtrate at 60 h of cultivation. With a 15 min reaction time, the optimal pH and temperature for the xylanase activity were at 6.5 and 65°C, respectively. The enzyme was almost stable over a broad range of pH 3–9 at 20°C, with an optimum stability at pH 6.5. After 51 h heating at 50°C the enzyme retained 60%, 100% and 90% activity at pH 5.0, 6.5 and 8.0, respectively. The crude enzyme could hydrolyse xylan effectively and in only 6 h 67.3%, 54.0% and 49.2% saccharifications were achieved for 2%, 5% and 10% substrate levels, respectively. The principal product of hydrolysis was xylobiose together with smaller amounts of xylooligosaccharides (degree of polymerization 3–7) and xylose.     

Production of biomass and ligninolytic enzymes by Pleurotus ostreatus in submerged culture.

The production of biomass and ligninolytic enzymes by Pleurotus ostreatus was analysed in synthetic medium with yeast extract and different glucose concentrations (0.5 - 20 g/l), at different pH (3.5-6.5) and incubation temperatures (23-32 degrees C). The best culture condition were: initial glucose concentration of 5 g/l, initial pH between 5.5-6.5 and incubation temperature between 26-29 degrees C. The saturation constant for glucose (Ks) was 1.75 g/l. The biomass concentration reached 8.6 g/l with a glucose addition of 20.0 g/l to the culture medium. The control of pH allowed an increment of 0.5 g/l of biomass concentration. The birreactor produced pellets with a homogeneous distribution of diameter size of 3.4 -/+ 0.2 mm. Approximately, 307 U/l of laccase and 0.41 U/l of manganese peroxidase were obtained in extracellular liquid medium and 0.015 U/g of laccase and 0.809 U/g of manganese peroxidase were obtained in solid substrate. Lignin peroxidase activity was not detected at any condition.     

Galacto-oligosaccharide production by a thermostable recombinant β-galactosidase from <Emphasis Type="Italic">Thermotoga maritima</Emphasis>

Summary A β-galactosidase from Thermotoga maritima produced galacto-oligosaccharides (GOS) from lactose by transgalactosylation when expressed in Escherichia coli. The enzyme activity for GOS production was maximal at pH 6.0 and 90 °C. In thermal stability experiments, the enzyme followed first-order kinetics of pH and thermal inactivation, and half-lives at pH 5.0, pH 8.0, 80 °C, and 95 °C were 27 h, 82 h, 41 h, and 14 min, respectively, suggesting that the enzyme was stable below 80 °C and in the pH range of 5.0–8.0. Mn²⁺ was the most effective divalent cation for GOS production. Cu²⁺ and EDTA inhibited more than 84% of enzyme activity. GOS production increased with increasing lactose concentrations and peaked at 500 g lactose/l. Among tested enzyme concentrations, the highest production of GOS was obtained at 1.5 units enzyme/ml. Under the optimal conditions of pH 6.0, 80 °C, 500 g lactose/l, and 1.5 units enzyme/ml, GOS production was 91 g/l for 300 min, with a GOS productivity of 18.2 g/l · h and a conversion yield of GOS to lactose of 18%.     

An Integrated Control Strategy for the Fermentation of the Marine-Derived Fungus Aspergillus glaucus for the Production of Anti-cancer Polyketide

An integrated control strategy of pH, shear stress, and dissolved oxygen tension (DOT) for fermentation scale-up of the marine-derived fungus Aspergillus glaucus HB 1–19 for the production of the anti-cancer compound aspergiolide A was studied. Keeping initial pH of 6.5 and shifting pH from 6.0 to 7.0 intermittently during the production phase greatly facilitated biosynthesis of aspergiolide A in shake flask cultures. Thus, a pH-shift strategy was proposed that shifting pH to 7.0 once it went lower than 6.0 by pulsed feeding NaOH solution during the production phase in bioreactor fermentation of A. glaucus HB 1–19. As a result, aspergiolide A production in a 30-L bioreactor was increased to 37.6?mg/L, which was 48.6% higher than that in 5-L bioreactor without pH shift. Fermentation scale-up was then performed in a 500-L bioreactor on the basis of an integrated criterion of near-same impeller tip velocity of early phase, DOT levels, and pH shift. The production of aspergiolide A was successfully obtained as 32.0?mg/L, which was well maintained during the process scale-up. This work offers useful information for process development of large-scale production of marine microbial metabolites.     

The effect of pH on the growth and metabolism of Streptococcus bovis in continuous culture

Streptococcus bovis H13/1 was grown anaerobically at pHs between 5.0 and 6.5 in a glucose-limited chemostat at a dilution rate of 0.05/h. The growth yield and the production of acetate, ethanol and formate decreased at pHs less than 6.5 whereas the production of lactate increased at the lower pH values. When a culture was subjected to sequential pH changes, growth yield and fermentation products were influenced not only by the pH existing in the culture medium but also by the metabolic activity of the cells at the preceding pHs in the sequence. The results are discussed in relation to the mechanisms available for the maintenance of pH homeo-stasis and for the metabolic control of fermentation pathways in Strep. bovis.     

The effect of pH on the growth and metabolism of Streptococcus bovis in continuous culture

Streptococcus bovis H13/1 was grown anaerobically at pHs between 5.0 and 6.5 in a glucose-limited chemostat at a dilution rate of 0.05/h. The growth yield and the production of acetate, ethanol and formate decreased at pHs less than 6.5 whereas the production of lactate increased at the lower pH values. When a culture was subjected to sequential pH changes, growth yield and fermentation products were influenced not only by the pH existing in the culture medium but also by the metabolic activity of the cells at the preceding pHs in the sequence. The results are discussed in relation to the mechanisms available for the maintenance of pH homeostasis and for the metabolic control of fermentation pathways in Strep. bovis.     

Use of high culture pH for the decreased proteolysis of human parathyroid hormone secreted by Saccharomyces cerevisiae

Human parathyroid hormone (hPTH) was expressed and secreted in Saccharomyces cerevisiae. In batch fermentations performed at pH = 5.6, 6.5, 7.2 and 7.5, optimal production of hPTH (12.1 mg/l) was obtained at pH 7.2 after 24 h of culture. At pH 5.6, most of secreted hPTH was degraded. Proteolysis of hPTH was significantly decreased by increasing the culture pH.     

Influence of growth conditions on the production of lactocin 705, a bacteriocin produced by Lactobacillus casei CRL 705

G.M. VIGNOLO, M.N. DE KAIRUZ, A.P. DE RUIZ HOLGADO AND G. OLIVER. 1995. The effect of growth parameters on the production of lactocin 705 by Lactobacillus casei CRL 705 isolated from dry sausages was studied. The antimicrobial compound was produced during the growth cycle at temperatures between 15 and 30°C. Maximal activity in MRS broth was achieved at pH 6.5-7.5. Investigation into the influence of supplementation and/or replacement of nutrients on lactocin 705 production demonstrated that large quantities of the bacteriocin could be obtained by addition of Tween 80 (0.5-2.0%), glucose (2.0%), tryptone (1.0%) and yeast extract (2.0%). Bacteriocin production did not decrease in the presence of (w/v) 3% NaC1 and 0.02% NaNO₂ in the culture medium. High titres of the antimicrobial compound were obtained in whey permeate supplemented with 2.0% yeast extract and 1.0% Tween 80. Lactocin 705, proved to be stable to pH and temperature at ripening conditions (pH 5.0-6.0 and 15°C) of dry cured sausages.     

Pentachlorophenol removal from slightly acidic mineral salts,commercial sand,and clay soil by recovered Arthrobacter strain ATCC 33790

Arthrobacter strain ATCC 33790, a pentachlorophenol (PCP)-metabolizer isolated by the author, has been recovered after 10 years of storage. The freeze-dried preparation grown on half-strength Trypticase Soy Broth adapted to utilize PCP within 1 week. Cultures grown on PCP-nutrient agar were found to utilize PCP in mineral salts medium within 2–3 days. The culture was prepared for continuous growth at pH 6.5 by successive feeding of 100–110 mg solid aliquots of PCP to a 1-l culture initially grown at pH 7.4. Continuous culture growth at pH 6.5 was possible on a mineral salts feed containing 1800 ppm PCP. Continuous cultures grown at pH 6.7 on mineral salts feeds containing 500 and 340 mg PCP/l were especially efficient in removing PCP. Less than 4 mg PCP/l were detected in the effluent at dilution rates near washout. In batch culture studies at pH 6.5 the PCP utilization kinetics were found to be similar at low PCP concentration to those at pH 7.4 for the approximately same inoculum size. Utilization of 35 mg PCP/l was very slow at pH 6.0. Growth rates at pH 6.5 at controlled PCP concentration ranges of 5–35 and 75–115 mg/l were 0.09 h^–1 and 0.05 h^–1, respectively. The ability of strain ATCC 33790 to utilize PCP in mineral salts media containing naphthalene, methylnaphthalenes, and cresols was examined. Naphthalene, 1-, and 2-methylnaphthalenes at their solubility limit, and o- and m-cresols at 900–1000 mg/l prevented utilization of 80–90 mg PCP/l. PCP was rapidly removed from both commercial sand at 30°C and from clay soil at room temperature. Estimated inoculum sizes of 6.6 × 10⁶, 6.6 × 10⁴, and 656 cells/g were found to be effective in removing approximately half the starting amount of PCP from sand in 3, 19, and 42 h, respectively. Nearly complete disappearance of extractable PCP was observed after 1 day in clay soil inoculated with 6 × 10⁶ cells/g.     

枯草芽孢杆菌中性β—甘露聚糖酶的产生及性质

由土壤中分离出一株产中性β甘露聚糖酶的枯草芽孢杆菌（Ｂａｃｉｌｕｓｓｕｂｔｉｌｉｓ）,编号ＢＭ９６０２。该菌在液体培养条件下,产生中性β甘露聚糖酶。多糖能作为碳源,而单糖不能作为碳源;有机氮源优于无机氮源。产酶最适培养基组成：魔芋粉４％,牛肉蛋白胨和酵母膏各１％。产酶最适培养条件：培养基起始ｐＨ８５,３５℃,振荡培养３６ｈ。以槐豆胶为底物,培养滤液中性β甘露聚糖酶活力为９６ＩＵ／ｍＬ。酶在ｐＨ５０～１００和５０℃下稳定;作用最适条件为ｐＨ６０和５０℃;水解魔芋粉和槐豆胶均产生寡聚糖。     

Characterization of Thermoanaerobacter Glucose Isomerase in Relation to Saccharidase Synthesis and Development of Single-Step Processes for Sweetener Production

Regulation of glucose isomerase synthesis was studied in Thermoanaerobacter strain B6A, which fermented a wide variety of carbohydrates including glucose, xylose, lactose, starch, and xylan. Glucogenic amylase activities and β-galactosidase were produced constitutively, whereas the synthesis of glucose isomerase was induced by either xylose or xylan. Production of these saccharidase activities was not significantly repressed by the presence of glucose or 2-deoxyglucose in the growth media. Glucose isomerase production was optimized by controlling the culture pH at 5.5 during xylose fermentation. The apparent temperature and pH optima for these cell-bound saccharidase activities were as follows: glucose isomerase, 80°C, pH 7.0 to 7.5; glucogenic amylase, 70°C, pH 5.0 to 5.5; and β-galactosidase, 60°C, pH 6.0 to 6.5 Glucose isomerase, glucogenic amylase, and β-galactosidase were produced in xylose-grown cells that were active and stable at 60 to 70°C and pH 6.0 to 6.5. Under single-step process conditions, these saccharidase activities in whole cells or cell extracts converted starch or lactose directly into fructose mixtures. A total of 96% of initial liquefied starch was converted into a 49:51 mixture of glucose and fructose, whereas 85% of initial lactose was converted into a 40:31:29 mixture of galactose, glucose, and fructose.