Enzymatic production of pyruvate from fumarate — an application of microbial cyclic-imide-transforming pathway

For the purpose of producing pyruvate from fumarate through microbial cyclic-imide-transforming pathway, various cyclic-imide-utilizing microorganisms were isolated from soil. Among them, strain g31 was the best producer and was identified as Pseudomonas sp. With the resting cells of the strain, the conditions were optimized for pyruvate production from fumarate. The cells cultivated in the medium containing 2% (w/v) of fumarate showed the highest production with sufficient yield. The optimized wet-cell concentration, pH and temperature of the reaction were 1% (w/v), pH 6 to 7, and 30°C, respectively. Aeration was found to be an effective factor, and vigorous shaking during the reaction mixture resulted in higher production. Under the optimized reaction conditions, 100 mM of fumarate was almost stoichiometrically converted into pyruvate (94 mM) in 24 h.     

Inulinase production by a marine yeast <Emphasis Type="Italic">Pichia guilliermondii</Emphasis> and inulin hydrolysis by the crude inulinase

Marine yeast strain 1, isolated from the surface of a marine alga, was found to secrete a large amount of inulinase into the medium. This marine yeast was identified as a strain of Pichia guilliermondii according to the results of routine yeast identification and molecular methods. The crude inulinase produced by this marine yeast worked optimally at pH 6.0 and 60°C. The optimal medium for inulinase production was seawater containing 4.0% (w/v) inulin and 0.5% (w/v) yeast extract, while the optimal cultivation conditions for inulinase production were pH 8.0, 28°C and 170 rpm. Under the optimal conditions, over 60 U ml⁻¹ of inulinase activity was produced within 48 h of fermentation in shake flasks. A large amount of monosaccharides and a trace amount of oligosaccharides were detected after the hydrolysis, indicating that the crude inulinase had a high exoinulinase activity.     

Optimization of Process Parameters for the Production of Inulinase from a Newly Isolated Aspergillus niger AUP19

Summary Fifty strains were isolated from different soil samples on synthetic medium containing inulin as a sole carbon source for the production of extracellular inulinase. Of them, five isolates showed high inulinase activity and one of them was selected for identification and medium optimization studies. The isolate was identified as Aspergillus niger. Various physical and chemical parameters were optimized for inulinase production. Maximum productivity of inulinase (176 U ml⁻¹) was achieved by employing medium containing 5% (w/v) inulin, galactose as additional carbon source, corn steep liquor and (NH₄)H₂PO₄ as nitrogen sources, incubation period of 72 h, incubation temperature of 28 °C, pH 6.5, inoculum load at 10% (v/v) level and medium volume to flask volume ratio of 1:20 (v/v) with indented flasks.     

Enhancement of extracellular bispecific anti‐MUC1 nanobody expression in E. coli BL21 (DE3) by optimization of temperature and carbon sources through an autoinduction condition

Escherichia coli is one of the most suitable hosts for production of antibodies and antibody fragments. Antibody fragment secretion to the culture medium improves product purity in cell culture and diminishes downstream costs. In this study, E. coli strain BL21 (DE3) harboring gene encoding bispecific anti‐MUC1 nanobody was selected, and the autoinduction methodology for expression of bispecific anti‐MUC1 nanobody was investigated. Due to the replacement of IPTG by lactose as inducer, less impurity and toxicity in the final product were observed. To increase both intracellular and extracellular nanobody production, initially, the experiments were performed for the key factors including temperature and duration of protein expression. The highest amount of nanobody was produced after 21 h at 33°C. The effect of different carbon sources, glycerol, glucose, lactose, and glycine as a medium additive at optimum temperature and time were also assessed by using response surface methodology. The optimized concentrations of carbon sources were obtained as 0.75% (w/v), 0.03% (w/v), 0.1% (w/v), and 0.75% (w/v) for glycerol, glucose, lactose, and glycine, respectively. Finally, the production of nanobody in 2 L fermenter under the optimized autoinduction conditions was evaluated. The results show that the total titer of 87.66 µg/mL anti‐MUC1 nanobody, which is approximately seven times more than the total titer of nanobody produced in LB culture medium, is 12.23 µg/L .     

Optimization of an ethanol production medium in very high gravity fermentation

Concentrations of Mg²⁺, glycine, yeast extract, biotin, acetaldehyde and peptone were optimized by a uniform design process for ethanol production by Saccharomyces cerevisiae. Using non-linear step-wise regression analysis, a predictive mathematical model was established. Concentrations of Mg²⁺ and peptone were identified as the critical factors: 50 mM Mg²⁺ and 1.5% (w/v) peptone in the medium increased the final ethanol titre from 14.2% (v/v) to 17% (v/v) in 48 h.     

出芽短梗霉Aureobasidium sp. SRF的菌株特性分析及胞外多糖结构鉴定

菌株SRF是1株从意大利树莓(Rubus corchorifolius)果实表面分离、可产胞外多糖的新菌株。在鉴定其分类归属的基础上,对其产生的胞外多糖进行了结构分析和发酵条件优化,为寻找微生物多糖提供新的菌株,为开发利用资源微生物提供借鉴。通过形态学和ITS序列对比分析进行菌株鉴定;通过薄层层析和红外光谱分析,确定胞外多糖结构;通过单因素检测试验,确定影响产糖量的主要因素;响应面Plackett-Burman和Box-Behnken设计筛选发酵产胞外多糖的最优条件。结果表明,出发菌株SRF隶属于出芽短梗霉属,命名为Aureobasidium sp. SRF;SRF所产胞外多糖为普鲁兰多糖;单因素检测表明,对多糖产量影响最大的因素为碳源浓度、氮源浓度、无机离子浓度,其次是碳源、氮源、无机离子、pH值;根据响应面结果确定最优发酵条件为麦芽糖8%(质量分数)、酵母提取物3%(质量分数)、钙离子0.3 g/L、pH 6,产糖量达5.93 g/L。SRF是1株来源于树莓浆果表面,可产胞外普鲁兰多糖的出芽短梗霉新菌株,是1株产微生物多糖的候选菌株。     

Production of 1,3-propanediol by <Emphasis Type="Italic">Clostridium butyricum</Emphasis> VPI 3266 using a synthetic medium and raw glycerol

Growth inhibition of Clostridium butyricum VPI 3266 by raw glycerol, obtained from the biodiesel production process, was evaluated. C. butyricum presents the same tolerance to raw and to commercial glycerol, when both are of similar grade, i.e. above 87% (w/v). A 39% increase of growth inhibition was observed in the presence of 100 g l^–1 of a lower grade raw glycerol (65% w/v). Furthermore, 1,3-propanediol production from two raw glycerol types (65% w/v and 92% w/v), without any prior purification, was observed in batch and continuous cultures, on a synthetic medium. No significant differences were found in C. butyricum fermentation patterns on raw and commercial glycerol as the sole carbon source. In every case, 1,3-propanediol yield was around 0.60 mol/mol glycerol consumed.     

Optimized protocol for the pilot-scale preparation of fungal cellulase

Summary A 25-l scale protocol is devised for the optimal secretion and recovery of fungal cellulase. Using a selected higher yieldingTrichoderma viride SMC strain, a protocol consisted of: a) an optimized production medium rich in microcrystalline cellulose (MCC), fortified with 1% (w/v) ammonium sulphate, 0.5% (w/v) soybean flour, 0.1% (v/v) Tween-80 and other trace nutrients; b) optimized physical parameters of production, such as an inoculum containing a homogeneous suspension of 6×10⁷ conidia per 1,28±1°C, pH 4.0±0.5, 300±20 rpm, 11000±1000 l/h aeration, and 170–220 h duration; c) optimal recovery through a filter press (450 l/h rate of filtration) followed by precipitation with 2.5–3.0 volumes of acetone (15°C and basket centrifugation (27°C, 1700 rpm)); and d) vacuum drying (35°C, 4–6 h). This afforded 70% recovery of cellulase in the form of white fluffy powder containing 20000±2000 carboxy methyl cellulase and 1000±50 units filter paperase per g activities, with raw material cost of US$ 8–10 per million carboxy methyl cellulase units. During storage for 18 months at 4°C, ambient temperature and 37°C, the cellulase preparation was found to retain 100, 75 and 60% of its initial activity, respectively.     

Production and Chemical Characterization of Antifungal Metabolites From Micromonosporasp. M39 Isolated From Mangrove Rhizosphere Soil

Micromonospora sp. M39 was selected as a producer of antifungal substances. Cell mass and antifungal activity of the organism was dependent on the carbon and nitrogen sources used. A combination of glucose, starch and glycerol as carbon sources at 1%(w/v) and corn steep powder as a nitrogen source at 0.25%(w/v) concentration in basal medium gave a maximum growth of 17.2 PCV/50 ml and in vitro an antifungal activity of 19.0 mm against the rice blast pathogen Pyricularia oryzaeMPO 293. In the selected production medium, optimum antifungal activity of the crude extract of the strain M39 was on day 16 of fermentation at 28 ± 2 °C. The crude extract of the strain M39 was analyzed and characterized by HPLC-DAD-UV–visible spectra. The peaks with a retention time of 4.88 min had a u.v. spectrum identical to that of 2,3-dihydroxybenzoic acid. The peak with a retention time of 6.08 min was confirmed by an automated spectral library search as phenylacetic acid. Two other peaks in the chromatogram were identified as cervinomycin A1 with a retention time at 12.78 min and cervinomycin A2 with a retention time at 13.46 min.     

Production of bacterial cellulose from <Emphasis Type="Italic">Enterobacter amnigenus</Emphasis> GH-1 isolated from rotten apple

Bacterial cellulose finds novel applications in biomedical, biosensor, food, textile and other industries. The optimum fermentation conditions for the production of cellulose by newly isolated Enterobacter amnigenus GH-1 were investigated. The strain was able to produce cellulose at temperature 25–35°C with a maximum at 28°C. Cellulose production occurred at pH 4.0–7.0 with a maximum at 6.5. After 14 days of incubation, the strain produced 2.5 g cellulose/l in standard medium whereas cellulose yield in the improved medium was found to be 4.1 g/l. The improved medium consisted of 4% (w/v) fructose, 0.6% (w/v) casein hydrolysate, 0.5% (w/v) yeast extract, 0.4% (w/v) disodium phosphate, and 0.115% (w/v) citrate. Addition of metal ions like zinc, magnesium, and calcium and solvents like methanol and ethanol were found to be stimulatory for cellulose production by the strain. The strain used natural carbon sources like molasses, starch hydrolysate, sugar cane juice, coconut water, coconut milk, pineapple juice, orange juice, and pomegranate juice for growth and cellulose production. Fruit juices can play important role in commercial exploitation of bacterial cellulose by lowering the cost of the production medium.     

Cultural conditions for production of glucoamylase from Lactobacillus amylovorus ATCC 33621

Lactobacillus amylovorus ATCC 33621 is an actively amylolytic bacterial strain which produces a cell-bound glucoamylase (EC 3.2.1.3). Conditions of growth and glucoamylase production were investigated using dextrose-free de Man-Rogosa-Sharpe (MRS) medium in a 1.5 I fermenter, with varying dextrin concentration (0.1–1.5% (w/v)), pH (4.5–6.5) and temperature (25–55°C). Cell extracts were prepared by subjecting cells to treatment with a French Pressure cell in order to release intracellular proteins. Glucoamylase activity was then assayed. The effects of pH (4.0–9.0), temperature (15–85°C) and substrate (dextrin and starch, 0–2% w/v) concentration on crude enzyme activity were investigated. Optimal growth was obtained in MRS medium containing 1% (w/v) dextrin, at pH 5.5 and 37°C. Glucoamylase production was maximal at the late logarithmic phase of growth, during 16–18 h. Crude enzyme had a pH optimum of 6.0 and temperature optimum of 60°C. With starch as the substrate, maximal activity was obtained at a concentration of 1.5% (w/v). The effects of ions and inhibitors on glucoamylase activity were also investigated. Enzyme activity was not significantly influenced by Ca²⁺ and EDTA at 1 mmol 1⁻¹ concentration; however Pb²⁺ and Co²⁺ were found to inhibit the activity at concentrations of 1 mmol 1⁻¹. The crude enzyme was found to be thermolabile when glucoamylase activity decreased after about 10 min exposure at 60°C. This property can be exploited in the brewing of low calorie beers where only mild pasteurization treatments are used to inactivate enzymes. The elimination of residual enzyme effect would prevent further maltodextrin degradation and sweetening during long-term storage, thus helping to stabilize the flavour of beer.     

Development of fermentation process for PLA-degrading enzyme production by a new thermophilic Actinomadura sp. T16-1

The fermentation process for a poly (L-lactide) (PLA)-degrading enzyme production by a newly isolate of thermophilic PLA-degrading Actinomadura sp. T16-1 was investigated. The strain produced 33.9 U/mL of enzyme activity after cultivation at 50°C under shaking of 150 rpm for 96 h in a medium consisting of (w/v) 0.05% PLA film, 0.2% gelatin, 0.4% (NH₄)₂SO₄, 0.4% K₂HPO₄, 0.2 % KH₂PO₄, and 0.02% MgSO₄ · 7H₂O. The optimal concentration of PLA film and gelatin obtained by response surface methodology (RSM) for the highest production of PLA-degrading enzyme was 0.035% (w/v) and 0.238% (w/v), respectively. Under these conditions, the model predicted 40.4 U/mL of PLA-degrading activity and the verification of the optimization showed 44.6 U/mL of PLA-degrading enzymatic activity in the flasks experiment. The maximum PLA-degrading activity reached 150 U/mL within 72 h cultivation in the 3-L airlift fermenter.     

Intergeneric protoplast fusion between Kluyveromyces and Saccharomyces cerevisiae – to produce sorbitol from Jerusalem artichokes

The construction of inulin-assimilating and sorbitol-producing fusants was achieved by intergeneric protoplast fusion between Kluyveromyces sp. Y-85 and Saccharomyces cerevisiae E-15. The cells of parental strains were pretreated with 0.1% EDTA (w/v) and 2-mercaptoethanol (0.1%, v/v) and then exposed to 2.0% (w/v) Zymolase at 30 °C for 30–40 min. The optimized fusion condition demonstrated that with the presence of 30% (w/v) polyethylene glycol 6000 (PEG-6000) and 10 mM CaCl₂ for 30 min, the fusion frequency reached 2.64 fusants/10⁶ parental cells. The fusants were screened by different characters between two parental strains and further identified by DNA contents, inulinase activity and sorbitol productivity. One of the genetically stable fusants, Strain F27, reached a maximal sorbitol production of 4.87 g/100 ml under optimal fermentation condition.     

Rosmarinic acid production by <Emphasis Type="Italic">Coleus forskohlii</Emphasis>hairy root cultures

Coleus forskohlii hairy root cultures were found to produce forskolin and rosmarinic acid (RA) as the main metabolites. The growth and RA production by C. forskohlii hairy root cultures in various liquid media were examined. The hairy root cultures showed good growth in hormone-free Murashige and Skoog medium containing 3% (w/v) sucrose (MS medium), and Gamborg B5 medium containing 2% (w/v) sucrose (B5 medium). RA yield reached 4.0 mg (MS medium) and 4.4 mg (B5 medium) after 5 weeks of culture in a 100 ml flask containing 20 ml of each medium. Hairy root growth and RA were also investigated after treatment with various concentrations of yeast extract (YE), salicylic acid (SA) and methyl jasmonic acid (MJA). RA production in a 100 ml flask containing 20 ml B5 medium reached 5.4 mg (1.9 times more than control) with treatment of 0.01 or 1% (w/v) YE, 5.5 mg (2.0 times more than control) with treatment of 0.1 mM SA, and the maximum RA content with 9.5 mg per flask (3.4 times more than control) was obtained in the hairy roots treated with 0.1 mM MJA. These results suggest that MJA is an effective elicitor for production of RA in C. forskohlii hairy root cultures.     

Improved production of curdlan with concentrated cells ofAgrobacterium sp.

The addition of a limited concentration of yeast extract to a minimal salt medium (MSM) enhanced cell growth and increased the production of curdlan whereas nitrogenlimitation was found to be essential for the higher production of curdlan byAgrobacterium sp. ATCC 31749. As the amount of the inoculum increased, the cell growth as well as the production of curdlan also increased in the MSM without a nitrogen source. The cell growth and production of curdlan increased as the initial pH of the medium decreased as low as 5.0. The conversion rate and concentration of curdlan from 2% (w/v) glucose in the MSM with concentrated cells under nitrogen deletion was 67% and 13.4 g/L, respectively. The highest conversion rate of curdlan under the conditions optimized in this study was 71% when the glucose concentration was 1% (w/v).     

Medium optimization for the production of glucose isomerase from thermophilic Streptomyces thermonitrificans

A thermophilic strain of Streptomyces thermonitrificans produced a high activity of intracellular glucose isomerase (12 U/ml) when grown in a medium containing 1% (w/v) xylose, supplemented with 2% (w/v) sorbitol as the second carbon source, at 50°C for 16 h. Addition of Mg²⁺ enhanced enzyme production but the organism could grow and produce the enzyme in the absence of Co²⁺.The authors are with the Division of Biochemical Sciences, National Chemical Laboratory, Pune 411 008, IndiaNCL Communication No. 5813     

Cell surface structure enhancing uptake of polyvinyl alcohol (PVA) is induced by PVA in the PVA-utilizing <Emphasis Type="Italic">Sphingopyxis</Emphasis> sp. strain 113P3

Polyvinyl alcohol (PVA)-utilizing Sphingopyxis sp. 113P3 (reidentified from Sphingomonas sp. 113P3) removed almost 0.5% PVA from culture supernatants in 4 days. Faster degradation of 0.5% PVA was performed by the periplasmic fraction. The average molecular size of PVA in the culture supernatant or cell-bound PVA was gradually shifted higher, suggesting that lower molecular size molecules are degraded faster. Depolymerized products were found in neither the culture supernatant nor the cell-bound fraction; however they were recovered from the periplasmic fraction. As extracellular or cell-associated PVA oxidase activity was almost undetectable in strain 113P3, degradation of PVA must be performed by periplasmic PVA dehydrogenase after uptake into the periplasm. Following the consumption of PVA, a dent appeared on the cell surface on day 2 and increased in size and depth for 4 days and was maintained for 8 days. Ultrastructural change on the cell surface was only observed in PVA medium, but not in nutrient broth (NB), suggesting that the change is induced by PVA. Fluorescein-4-isothiocyanate-labeled PVA was bound more to cells grown in PVA than to cells grown in NB. No binding was found with PVA-grown cells treated with formaldehyde. Thus, a dent on the cell surface seems to be related to the uptake of PVA.     

Determination of the Chemical Form of Fluorine in Tea Infusions by 19F-NMR

A novel marine ice-nucleating bacterium, KUIN-5, was isolated from a marine algae, Monostroma latissum. Strain KUIN-5 was identified as a Pseudomonas sp. from its characteristics and taxonomies; the optimum temperature and pH for its growth were 25°C and 6.0, respectively. When strain KUIN-5 was aerobically cultured in Carlucci-Pramer medium (pH 6.0) for 50 h at 25°C, the highest ice-nucleating activity of the cells among the media for marine bacteria was obtained, and the ice-nucleating temperature, T₅₀, was indicated to be ? 3.2°C. Also, the optimum concentration of NaCl for the growth in this medium, which was prepared with distilled water instead of seawater, was 2.0% (w/v) and then the ice-nucleating activity was inversely proportional to the NaCl concentration. Moreover, when strain KUIN-5 was cultured in Davis medium under optimum conditions, it produced insoluble polysaccharide (IPS) in the culture. The maximum amount of IPS production by strain KUIN-5 was 84.5 mg/ml of medium under optimum conditions. Therefore, this IPS was isolated and could be identified as cellulose, based on TLC or HPLC of the acid hydrolysate, and GC-MS of the acetylated polyalcohol prepared by periodate oxidation and Smith degradation of this polysaccharide. This is the first report of cellulose production by a marine ice-nucleating bacterium.     

Lipase from marine Aspergillus awamori BTMFW032: production, partial purification and application in oil effluent treatment

Marine fungus BTMFW032, isolated from seawater and identified as Aspergillus awamori, was observed to produce an extracellular lipase, which could reduce 92% fat and oil content in the effluent laden with oil. In this study, medium for lipase production under submerged fermentation was optimized statistically employing response surface method toward maximal enzyme production. Medium with soyabean meal-0.77% (w/v); (NH(4))(2)SO(4)-0.1m; KH(2)PO(4)-0.05 m; rice bran oil-2% (v/v); CaCl(2)-0.05 m; PEG 6000-0.05% (w/v); NaCl-1% (w/v); inoculum-1% (v/v); pH 3.0; incubation temperature 35°C and incubation period-five days were identified as optimal conditions for maximal lipase production. The time course experiment under optimized condition, after statistical modeling, indicated that enzyme production commenced after 36 hours of incubation and reached a maximum after 96 hours (495.0 U/ml), whereas maximal specific activity of enzyme was recorded at 108 hours (1164.63 U/mg protein). After optimization an overall 4.6-fold increase in lipase production was achieved. Partial purification by (NH(4))(2)SO(4) precipitation and ion exchange chromatography resulted in 33.7% final yield. The lipase was noted to have a molecular mass of 90 kDa and optimal activity at pH 7 and 40°C. Results indicated the scope for potential application of this marine fungal lipase in bioremediation.     

Inulinase production by the marine yeast Cryptococcus aureus G7a and inulin hydrolysis by the crude inulinase

The marine yeast strain G7a isolated from sediment of China South Sea was found to secrete a large amount of inulinase into the medium. This marine yeast strain was identified to be a strain of Cryptococcus aureus according to the results of routine yeast identification and molecular methods. The crude inulinase produced by this marine yeast showed the highest activity at pH 5.0 and 50 °C. The optimal medium for inulinase production was artificial seawater containing inulin 4.0% (w/v), K₂HPO₄ 0.3% (w/v), yeast extract 0.5% (w/v), KCl 0.5% (w/v), CaCl₂ 0.12% (w/v), NaCl 4.0% (w/v) and MgCl₂·6H₂O 0.6% (w/v), while the optimal cultivation conditions for inulinase production were pH 5.0, a temperature of 28 °C and a shaking speed of 170 rpm. Under the optimal conditions, over 85.0 U/ml of inulinase activity was produced within 42 h of fermentation at shake flask level. This is very high level of inulinase activity produced by yeasts. A large amount of monosaccharides and oligosaccharides were detected after inulin hydrolysis by the crude inulinase.