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.     

Sugarcane molasses and yeast powder used in the Fructooligosaccharides production by Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611

Different concentrations of sucrose (3–25% w/v) and peptone (2–5% w/v) were studied in the formulation of media during the cultivation of Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611. Moreover, cane molasses (3.5–17.5% w/v total sugar) and yeast powder (1.5–5% w/v) were used as alternative nutrients for both strains’ cultivation. These media were formulated for analysis of cellular growth, β-Fructosyltransferase and Fructooligosaccharides (FOS) production. Transfructosylating activity (U _t ) and FOS production were analyzed by HPLC. The highest enzyme production by both the strains was 3% (w/v) sucrose and 3% (w/v) peptone, or 3.5% (w/v) total sugars present in cane molasses and 1.5% (w/v) yeast powder. Cane molasses and yeast powder were as good as sucrose and peptone in the enzyme and FOS (around 60% w/w) production by studied strains.     

Production of extracellular emulsifying agent byPseudomonas aeruginosa UG1

Summary Twenty-three bacterial strains were isolated from oil-contaminated soil samples. Of these, 20 displayed some ability to effect oil dispersion and they were screened quantitatively for the ability to emulsify 0.5% (v/v) reference oil. One strain, identified asPseudomonas aeruginosa UG1, produced extracellular material that emulsified reference oil, hexadecane and 2-methylnaphthalene at concentrations as high as 6% (v/v) in nutrient broth. Emulsification activity increased during a 10 day incubation period at 30°C. The activity was not influenced by pH over the range 5 to 9. The emulsifying agent was precipitated by cold ethanol. The highest emulsifying activity was detected in the extracellular fraction precipitated between 30 and 50% (v/v) ethanol. A linear relationship was observed between emulsifier concentration (mg/ml) and emulsifying activity. Genetic analysis showed that thePseudomonas aeruginosa UG1 strain did not carry extrachromosomal plasmids, suggesting that the gene(s) coding for emulsifying activity was carried on the chromosome.     

Production of a Thermostable Lipase by Humicola lanuginosa Grown on Sorbitol-Corn Steep Liquor Medium

For thermostable lipase production by Humicola lanuginosa No. 3, a simple optimized medium consisting of (%, w/v): sorbitol, 1.0; corn steep liquor, 1.0; NaCl, 0.5; CaCl₂–2H₂0, 0.01; Silicone Km-70 (antifoamer), 0.2; and whale oil or castor oil as a lipase inducer, 0.3, was used. The yield of the lipase was about 80 — 120U/ml after 25 hr aerobic cultivation at 45°C when the pH was maintained at 7 to 8. The acetone powder preparation of the enzyme was most active at pH 7.0 and 45°C. The enzyme retained 100% activity on incubation for 20 hr at 60°C. The enzyme was able to hydrolyze almost all forms of natural fats tested (14 kinds), coconut oil being the most rapidly hydrolyzed.     

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.     

Production of Bacteriocin ST33LD, Produced by Leuconostoc mesenteroides subsp. mesenteroides, as Recorded in the Presence of Different Medium Components

Summary Bacteriocin ST33LD, produced by Leuconostoc mesenteroides subsp. mesenteroides, is approximately 2.7 kDa in size and inhibits Enterococcus faecalis, Escherichia coli, Lactobacillus casei and Pseudomonas aeruginosa. Good growth was recorded in the presence of 10% (w/v) soy milk or 10% (w/v) molasses, but there was no bacteriocin production. Growth in MRS broth adjusted to pH 4.5 yielded low bacteriocin levels (800 AU/ml). However, the same medium adjusted to pH 5.0, 5.5 and 6.5, respectively, yielded 3200 AU/ml. Tween 80 decreased bacteriocin production by more than 50%. Growth in the presence of tryptone yielded maximal activity (12,800 AU/ml), whereas different combinations of tryptone, meat extract and yeast extract produced activity levels of 1600 AU/ml and less. Growth in the presence of 2.0% (w/v) sucrose, or maltose, yielded much higher levels of bacteriocin activity (12,800 AU/ml) compared to growth in the presence of 2.0% (w/v) glucose or lactose (6400 AU/ml). Lower yields were also recorded in the presence of fructose and mannose. KH₂PO₄ at 10.0% (w/v) stimulated bacteriocin production. Glycerol concentrations of 0.5% (w/v) and higher (up to 5.0%, w/v) repressed bacteriocin production by 50%. The addition of cyanocobalamin, thiamine and L-ascorbic acid to MRS broth (1.0 ppm) yielded 12,800 AU/ml bacteriocin, whereas the addition of DL-6,8-thioctic acid yielded only 6 400 AU/ml.     

Efficiency of the EPS emulsifier produced by <Emphasis Type="Italic">Ochrobactrum anthropi</Emphasis> in different hydrocarbon bioremediation assays

Ochrobactrum anthropi strain AD2 was isolated from the waste water treatment plant of an oil refinery and was identified by analysis of the sequence of the gene encoding 16S rDNA. This bacterium produced exopolysaccharides in glucose nutrient broth media supplemented with various hydrocarbons (n-octane, mineral light and heavy oils and crude oils). The exopolysaccharide AD2 (EPS emulsifier) synthesized showed a wide range of emulsifying activity but none of them had surfactant activity. Yield production varied from 0.47 to 0.94 g of EPS l⁻¹ depending on the hydrocarbon added. In the same way, chemical composition and emulsification activity of EPS emulsifier varied with the culture conditions. Efficiency of the EPS emulsifier as biostimulating agent was assayed in soil microcosms and experimental biopiles. The AD2 biopolymer was added alone or combined with commercial products frequently used in oil bioremediation such as inorganic NPK fertilizer and oleophilic fertilizer (S200 C). Also, its efficiency was tested in mixture with activated sludge from an oil refinery. In soil microcosms supplemented with S200 C + EPS emulsifier as combined treatment, indigenous microbial populations as well as hydrocarbon degradation was enhanced when compared with microcosms treated with NPK fertilizer or EPS emulsifier alone. In the same way EPS emulsifier stimulated the bioremediation effect of S200 C product, increasing the number of bacteria and decreasing the amount of hydrocarbon remained. Finally, similar effects were obtained in biopile assays amended with EPS emulsifier plus activated sludge. Our results suggest that the bioemulsifier EPS emulsifier has interesting properties for its application in environment polluted with oil hydrocarbon compounds and may be useful for bioremediation purposes.     

Factorial designs: an efficient approach to choosing the main factors influencing growth and hydrolase production by <Emphasis Type="Italic">Tetrahymena thermophila</Emphasis>

A fractional factorial design with eight trials was applied to select and model the effects of major factors, individually and in combination, on improving Tetrahymena thermophila growth and enzyme production. Regulated pH at 6.8 and olive oil at 0.5% (v/v) showed positive effects on fermentation, and increased cell growth parameters including generation time and maximal population formation. Lipase and protease production were also improved by these factors and were favoured by cultivation of Tetrahymena in darkness. This statistical experiment offers a beneficial and rapid screening procedure to select the most effective combination of factors influencing fermentation processes.     

Extraction of fucoxanthin and polyphenol from <Emphasis Type="Italic">Undaria pinnatifida</Emphasis> using supercritical carbon dioxide with co-solvent

Extraction of brown seaweed (Undaria pinnatifida) oil was carried out by using supercritical carbon dioxide (SCO₂) and ethanol as co-solvent. The flow rate of ethanol was 3.0% (v/v) as compared to that of SCO₂. Experiments were performed in a semi-batch flow apparatus on dried samples at temperatures from 303 to 333 K and pressures from 80 to 300 bar. Fucoxanthin and polyphenol were quantitatively analyzed by using HPLC and UV-spectrometer. The highest yields of fucoxanthin and polyphenol were shown at 200 bar, 323 K and 250 bar, 333 K, respectively. The solubility of fucoxanthin in SCO₂ agreed well with the Chrastil model.     

Extracellular lipase of <Emphasis Type="Italic">Aspergillus niger</Emphasis> NRRL3; production,partial purification and properties

Four strains of Aspergillus niger were screened for lipase production. Each was cultivated on four different media differing in their contents of mineral components and sources of carbon and nitrogen. Aspergillus niger NRRL3 produced maximal activity (325U/ml) when grown in 3% peptone, 0.05% MgSO₄.7H₂O, 0.05% KCl, 0.2% K₂HPO₄ and 1% olive oil:glucose (0.5:0.5). A. niger NRRL3 lipase was partially purified by ammonium sulphate precipitation. The majority of lipase activity (48%) was located in fraction IV precipitated at 50–60% of saturation with a 18-fold enzyme purification. The optimal pH of the partial purified lipase preparation for the hydrolysis of emulsified olive oil was 7.2 and the optimum temperature was 60°C. At 70°C, the enzyme retained more than 90% of its activity. Enzyme activity was inhibited by Hg²⁺ and K⁺, whereas Ca²⁺ and Mn²⁺ greatly stimulated its activity. Additionally, the formed lipase was stored for one month without any loss in the activity.     

Production of bioethanol by direct bioconversion of oil-palm industrial effluent in a stirred-tank bioreactor

The purpose of this study was to evaluate the feasibility of producing bioethanol from palm-oil mill effluent generated by the oil-palm industries through direct bioconversion process. The bioethanol production was carried out through the treatment of compatible mixed cultures such as Thrichoderma harzianum, Phanerochaete chrysosporium, Mucor hiemalis, and yeast, Saccharomyces cerevisiae. Simultaneous inoculation of T. harzianum and S. cerevisiae was found to be the mixed culture that yielded the highest ethanol production (4% v/v or 31.6 g/l). Statistical optimization was carried out to determine the operating conditions of the stirred-tank bioreactor for maximum bioethanol production by a two-level fractional factorial design with a single central point. The factors involved were oxygen saturation level (pO₂%), temperature, and pH. A polynomial regression model was developed using the experimental data including the linear, quadratic, and interaction effects. Statistical analysis showed that the maximum ethanol production of 4.6% (v/v) or 36.3 g/l was achieved at a temperature of 32°C, pH of 6, and pO₂ of 30%. The results of the model validation test under the developed optimum process conditions indicated that the maximum production was increased from 4.6% (v/v) to 6.5% (v/v) or 51.3 g/l with 89.1% chemical-oxygen-demand removal.     

Influence of dissolved oxygen and shear conditions on clavulanic acid production by Streptomyces clavuligerus

Clavulanic acid (CA), a potent β-lactamase inhibitor, is produced by a filamentous bacterium. Here, the effect of DO and shear, expressed as impeller tip velocity, on CA production was examined. Cultivations were performed in a 4 L fermentor with speeds of 600, 800 and 1,000 rpm and a fixed air flow rate (0.5 vvm). Also, cultivation with automatic control of dissolved oxygen, at 50% air saturation, by varying stirrer speed and using a mixture of air and O₂ (10% v/v) in the inlet gas, and a cultivation with fixed stirrer speed of 800 rpm and air flow rate of 0.5 vvm, enriched with 10% v/v O₂, were performed. Significant variations in CA titer, CA production rate and O₂ uptake-rate were observed. It was also found that the DO level has no remarkable effect on CA production once a critical level is surpassed. The most significant improvement in CA production was related to high stirrer speeds.     

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.     

Tetradecane 1,14-Dicarboxylic Acid Production from n-Hexadecane by Candida cloacae

The better condition of cultivation for tetradecane 1,14-dicarboxylic acid (DC-16) production from n-hexadecane (n-C₁₆) by Candida cloacae MR-12 was investigated by using acetic acid as carbon source for the growth. In general, the condition suitable for the growth was also favorable for the production of DC-16. The change of pH during cultivation, the use of NaOH solution as pH controlling agent after pH-change and the addition of antifoam stimulated the production of DC-16.

Under the optimum conditions where the culture medium contained 15% (v/v) n-C₁₆, 1.4% (w/v) acetic acid, inorganic salts and growth factors, and pH was changed from 6.5 to 7.75 at 16 hr after the inoculation, the highest level of DC-16 production was attained after about 72 hr cultivation and the amount of the product accumulated was 61.5 g per liter of the medium.

When a mixture of various n-alkanes was used as starting material, DCs corresponding to the respective n-alkanes were produced as mixture.     

Production of extracellular alkaline proteases by <Emphasis Type="Italic">Aspergillus clavatus</Emphasis>

Summary The production of extracellular alkaline proteases from Aspergillus clavatus was evaluated in a culture filtrate medium, with different carbon and nitrogen sources. The fungus was cultivated at three different temperatures during 10 days. The proteolytic activity was determined on casein pH 9.5 at 37 °C. The highest alkaline proteolytic activity (38 U/ml) was verified for culture medium containing glucose and casein at 1% (w/v) as substrates, obtained from cultures developed at 25 °C for 6 days. Cultures developed in Vogel medium with glucose at 2% (w/v) and 0.2% (w/v) NH₄NO₃ showed higher proteolytic activity (27 U/ml) when compared to the cultures with 1% of the same sugar. Optimum temperature was 40 °C and the half-lives at 40, 45 and 50 °C were 90, 25 and 18 min, respectively. Optimum pH of enzymatic activity was 9.5 and the enzyme was stable from pH 6.0 to 12.0.     

Production of biomass and recombinant human-like collagen in <Emphasis Type="Italic">Escherichia coli</Emphasis> processes with different CO<Subscript>2</Subscript> pulses

The evolution of CO₂ in a fed-batch culture of recombinant Escherichia coli containing human-like collagen (HLC) cDNA was determined with an O₂-enriched air supply (40%, v/v) in a 12.8 l fermentor; a maximum CO₂ concentration of 12.7% in the effluent gas was detected. The CO₂ pulse injection experiments showed that: (1) a 20% CO₂ pulse introduced in the batch cultivation phases inhibited cell growth but if introduced in the fed-batch cultivation phases slightly stimulated growth; and (2) CO₂ inhibited HLC expression only in the expression phase, where the final HLC concentration decreased by 34% under a 3 h 20% CO₂ pulse. The higher the CO₂ concentration and/or the longer the duration of the CO₂ pulse, the stronger the stimulatory or inhibitory effects. An erratum to this article can be found at     

The influence of sucrose and an elevated CO2 concentration on photosynthesis of photoautotrophic peanut (Arachis hypogaea L.) cell cultures

Using photoautotrophic cells ofArachis hypogaea (L.) growing at ambient CO₂, it was shown that exogenous sucrose supplied to the liquid medium reduced¹⁴CO₂ fixation (supplied as NaH¹⁴CO₃). This was mostly due to a reduced labelling in P-esters, and to a lesser extent, in the serine/glycine moiety. However, radioactivity in the neutral sugar fraction was increased upon supplement of exogenous sucrose. The reduced labelling of P-esters and serine/glycine agrees with a lower concentration and specific activity of Rubisco in the sucrose supplied treatments as compared to the control. Following a transfer into a sugar free nutrient medium the concentration and activity of Rubisco is increased. The concentration of PEPCase was not influenced by sucrose application, although its specific activity was increased.At elevated CO₂ concentration (2.34% v/v) the Rubisco concentration and specific activity was at the same level as in the control (0.03% v/v CO₂). However, the concentration and the specific activity of PEPCase was increased and dry weight increase was about 8–9-fold higher than at ambient CO₂.     

Optimization for producing cell-bound lipase from <Emphasis Type="Italic">Geotrichum</Emphasis> sp. and synthesis of methyl oleate in microaqueous solvent

An integrated optimization strategy involving a combination of different designs was employed to optimize producing conditions of cell-bound lipase (CBL) from Geotrichum sp. Firstly, it was obtained by a single factorial design that the most suitable carbon source was a mixture of olive oil and citric acid and the most suitable nitrogen source was a mixture of corn steep liquor and NH₄NO₃. Then, the Plackett–Burman design was used to evaluate the effects of 13 variables related to CBL production, and three statistically significant variables namely, temperature, olive oil concentration, and NH₄NO₃ concentration, were selected. Subsequently, the levels of the three variables for maximum CBL production were determined by response surface analysis as follows: 1.64% (v/v) olive oil, 1.49% (w/v) NH₄NO₃, and temperature 33.00°C. Such optimization resulted in a high yield of CBL at 23.15 U/ml, an enhanced 4.45-fold increase relative to the initial result (5.2 U/ml) in shake flasks. The dried CBL was used to synthesize methyl oleate in microaqueous hexane, resulting in 94% conversion after 24 h, and showed reusability with 70% residual activity and 69% conversion after eight cycles of batch operation, which indicating that CBL, as a novel and natural form of immobilized enzyme, can be effectively applied in repeated synthesis of methyl oleate in a microaqueous solvent.     

Production and partial characterization of biosurfactant produced by Streptomyces sp. R1

The present study focused on developing a wild-type actinomycete isolate as a model for a non-pathogenic filamentous producer of biosurfactants. A total of 33 actinomycetes isolates were screened and their extracellular biosurfactants production was evaluated using olive oil as the main substrate. Out of 33 isolates, 32 showed positive results in the oil spreading technique (OST). All isolates showed good emulsification activity (E₂₄) ranging from 84.1 to 95.8%. Based on OST and E₂₄ values, isolate R1 was selected for further investigation in biosurfactant production in an agitated submerged fermentation. Phenotypic and genotypic analyses tentatively identified isolate R1 as a member of the Streptomyces genus. A submerged cultivation of Streptomyces sp. R1 was carried out in a 3-L stirred-tank bioreactor. The influence of impeller tip speed on volumetric oxygen transfer coefficient (k _L a), growth, cell morphology and biosurfactant production was observed. It was found that the maximum biosurfactant production, indicated by the lowest surface tension measurement (40.5 ± 0.05 dynes/cm) was obtained at highest k _L a value (50.94 h⁻¹) regardless of agitation speed. The partially purified biosurfactant was obtained at a concentration of 7.19 g L⁻¹, characterized as a lipopeptide biosurfactant and was found to be stable over a wide range of temperature (20–121 °C), pH (2–12) and salinity [5–20% (w/v) of NaCl].

     

Production of α-amylase fromHalobacterium halobium

Maximum production of extracellular -amylase activity inHalobacterium halobium was at 40°C in a medium containing 25% (w/v) NaCl, 1% (w/v) soluble starch and 1% (w/v) peptone, in presence of 0.1mm ZnSO₄ after 5 days in shaking cultures. The amylase had optimal activity at pH 6.5 in the presence of 1 to 3% (w/v) NaCl at 53°C.S. Patel, N. Jain and D. Madamwar are with the Post Graduate Department of Biosciences, Sadar Patel University, Vallabh Vidyanagar-388120, India.