Strategy for the Improvement of Prodigiosin Production by a Serratia marcescens Mutant through Fed-Batch Fermentation

A Serratia marcescens mutant for prodigiosin production was obtained by u.v. mutation with rational screening methods and a two-step feeding strategy was used to increase its productivity. In flasks, the mutant strain B6 gave a 2.8-fold higher prodigiosin production than that of the parent strain with glycerol as a carbon source. In a 5-l bioreactor, with a two-step feeding strategy in which glucose was selected as the initial carbon source in the fermentation media and glycerol was fed as a ‘prodigiosin inducer’, it gave a 7.8 times higher prodigiosin production (583 mg/l) than the parent stain with the original cultivation mode.     

Improved trehalose production from biodiesel waste using parent and osmotically sensitive mutant of Propionibacterium freudenreichii subsp. shermanii under aerobic conditions

Trehalose is an important nutraceutical of wide commercial interest in the food processing industry. Recently, crude glycerol was reported to be suitable for the production of trehalose using a food microbe, Propionibacterium freudenreichii subsp. shermanii, under static flask conditions. Similarly, enhanced trehalose yield was reported in an osmotically sensitive mutant of the same strain under anaerobic conditions. In the present study, an effort was made to achieve higher production of trehalose, propionic acid, and lactic acid using the parent and an osmotically sensitive mutant of P. freudenreichii subsp. shermanii under aeration conditions. Under aeration conditions (200 rpm in shake flasks and 30 % air saturation in a batch reactor), biomass was increased and approximately 98 % of crude glycerol was consumed. In the parent strain, a trehalose titre of 361 mg/l was achieved, whereas in the mutant strain a trehalose titre of 1.3 g/l was produced in shake flask conditions (200 rpm). In the mutant strain, propionic and lactic acid yields of 0.53 and 0.21 g/g of substrate were also achieved with crude glycerol. Similarly, in controlled batch reactor culturing conditions a final trehalose titre of approximately 1.56 g/l was achieved with the mutant strain using crude glycerol as the substrate. Enhanced production of trehalose using P. freudenreichii subsp. shermanii from waste under aeration conditions is reported here. Higher production of trehalose was not due to a higher yield of trehalose but to a higher final biomass concentration.     

Culture Conditions for the Production of Alkaline Protease from n-Paraffins by a Kabicidin Resistant Mutant No. 5–128B

A novel process for the microbial production of alkaline protease on an industrial scale was successfully established by using a kabicidin resistant mutant, No. 5–128B, derived from Fusarium sp. S–19–5. The most suitable carbon source for producing alkaline protease was n-paraffins (C₁₀~C₁₄) and the effective nitrogen source was dried-yeast cells containing no nucleic acid, the optimum concentrations being 12.5% (w/v) and 7.0% (w/v), respectively. The optimal temperature and initial pH for protease production were 24°C and 6.0, respectively. Under the optimal conditions using a shaker flask mutant No. 5–128B produced 41000 PU/ml of alkaline protease, which corresponded to about 10 times the amount produced by the parent strain. The relation between the high ability to produce alkaline protease and the resistance to kabicidin, a polyene antibiotic, is discussed.     

Production of acidic lipase by a mutant of Aspergillus niger NCIM 1207 in submerged fermentation

Mutants of Aspergillus niger NCIM 1207, isolated by subjecting conidia to UV-irradiation, were tested for the production of lipase (glycerol ester hydrolase EC 3.1.1.3). Mutants UV-10 and ANCR-1 showed seven fold and five fold enhanced productivity of enzyme, respectively, over the wild strain in shake flask culture when grown in SOB medium containing 1% olive oil. Maximum lipase activity (41 IU/ml) was obtained in the culture broth when UV-10 was grown in medium supplemented with 0.5% Triton X-100. A higher concentration of oil in the medium did not help lipase production in the case of mutant UV-10. Similarly no increase in enzyme levels was observed when mutant UV-10 was grown in medium supplemented with glucose. However, the addition of glucose in the medium resulted in increased levels of lipase production by wild strain, Aspergillus niger NCIM 1207.     

A <Emphasis Type="Italic">Candida guilliermondii</Emphasis> lysine hyperproducer capable of elevated citric acid production

A mutant of the yeast Candida guilliermondii ATCC 9058 exhibiting elevated citric acid production was isolated based upon its ability to overproduce lysine. This method involved the use of a solid medium containing a combination of lysine analogues to identify a mutant that produced a several-fold higher lysine level compared to its parent strain using glucose or glycerol as a carbon source. The mutant strain was also capable of producing more than a fivefold higher citric acid level on glycerol as a carbon source compared to its parent strain. It was concluded that the screening of yeast lysine hyperproducer strains could provide a rapid approach to isolate yeast citric acid hyperproducer strains.     

Crude glycerol from biodiesel as a carbon source for production of a recombinant highly thermostable β-mannanase by <Emphasis Type="Italic">Pichia pastoris</Emphasis>

Objective

To explore an efficient use of crude glycerol for the production of a highly thermostable β-mannanase (ReTMan26) by Pichia pastoris X33.

Results

Cell growth was significantly inhibited by 4 and 6% (w/v) crude glycerol in 250 ml shake-flasks and in 5 l bioreactor batch cultures, respectively, but not affected by pure glycerol at the same concentrations. For further study, the impact of various impurities in crude glycerol on the cell growth of, and ReTMan26 production by, Pichia pastoris was investigated. Salts and methanol did not exert an inhibitory effect, but ≥ 0.2% and 0.3% (w/v) soap in shake-flask and bioreactor cultures, respectively, inhibited fermentation. Under identical conditions, the biomass and ReTMan26 activity produced by high-cell-density fermentation using 5% crude glycerol (glycerol at 80%, w/w) were slightly higher than those using 4% (w/v) pure glycerol.

Conclusions

Non-pretreated ≤ 5% (w/v) crude glycerol could be effectively utilized for industrial production of ReTMan26, and the total production costs using crude glycerol were ~ 4.2% lower than those using pure glycerol.

     

High-throughput screening of high <Emphasis Type="Italic">Monascus</Emphasis> pigment-producing strain based on digital image processing

This work proposed a new method which applied image processing and support vector machine (SVM) for screening of mold strains. Taking Monascus as example, morphological characteristics of Monascus colony were quantified by image processing. And the association between the characteristics and pigment production capability was determined by SVM. On this basis, a highly automated screening strategy was achieved. The accuracy of the proposed strategy is 80.6 %, which is compatible with the existing methods (81.1 % for microplate and 85.4 % for flask). Meanwhile, the screening of 500 colonies only takes 20–30 min, which is the highest rate among all published results. By applying this automated method, 13 strains with high-predicted production were obtained and the best one produced as 2.8-fold (226 U/mL) of pigment and 1.9-fold (51 mg/L) of lovastatin compared with the parent strain. The current study provides us with an effective and promising method for strain improvement.     

Production of tylosin in solid-state fermentation by Streptomyces fradiae NRRL-2702 and its gamma-irradiated mutant (γ-1)

Aims:  To develop solid-state fermentation system (SSF) for hyper production of tylosin from a mutant γ-1 of Streptomyces fradiae NRRL-2702 and its parent strain.
Methods and Results:  Various agro-industrial wastes were screened to study their effect on tylosin production in SSF. Wheat bran as solid substrate gave the highest production of 2500 μg of tylosin g⁻¹ substrate by mutant γ-1 against parent strain (300 μg tylosin g⁻¹ substrate). The tylosin yield was further improved to 4500 μg g⁻¹ substrate [70% moisture, 10% inoculum (v/w), pH 9·2, 30°C, supplemental lactose and sodium glutamate on day 9]. Wild-type strain displayed less production of tylosin (655 μg of tylosin g⁻¹ substrate) in SSF even after optimization of process parameters.
Conclusion:  The study has shown that solid-state fermentation system significantly enhanced the tylosin yield by mutant γ-1.
Significance and Impact of the Study:  This study proved to be very useful and resulted in 6·87 ± 0·30-fold increase in tylosin yield by this mutant when compared to that of wild-type strain.     

Improved glycerol to ethanol conversion by <Emphasis Type="Italic">E. coli</Emphasis> using a metagenomic fragment isolated from an anaerobic reactor

Crude glycerol obtained as a by-product of biodiesel production is a reliable feedstock with the potential to be converted into reduced chemicals with high yields. It has been previously shown that ethanol is the primary product of glycerol fermentation by Escherichia coli. However, few efforts were made to enhance this conversion by means of the expression of heterologous genes with the potential to improve glycerol transport or metabolism. In this study, a fosmid-based metagenomic library constructed from an anaerobic reactor purge sludge was screened for genetic elements that promote the use and fermentation of crude glycerol by E. coli. One clone was selected based on its improved growth rate on this feedstock. The corresponding fosmid, named G1, was fully sequenced (41 kbp long) and the gene responsible for the observed phenotype was pinpointed by in vitro insertion mutagenesis. Ethanol production from both pure and crude glycerol was evaluated using the parental G1 clone harboring the ethanologenic plasmid pLOI297 or the industrial strain LY180 complemented with G1. In mineral salts media containing 50 % (v/v) pure glycerol, ethanol concentrations increased two-fold on average when G1 was present in the cells reaching up to 20 g/L after 24 h fermentation. Similar fermentation experiments were done using crude instead of pure glycerol. With an initial OD₆₂₀ of 8.0, final ethanol concentrations after 24 h were much higher reaching 67 and 75 g/L with LY180 cells carrying the control fosmid or the G1 fosmid, respectively. This translates into a specific ethanol production rate of 0.39 g h^?1 OD^?1 L^?1.     

The production of poly(3-hydroxybutyrate) [P(3HB)] by a newly isolated Bacillus sp. ST1C using liquid waste from biodiesel production

A newly isolated poly(3-hydroxybutyrate) [P(3HB)] producing strain, ST1C, was identified as Bacillus aryabhattai based on its morphological, biochemical and molecular characteristics. It synthesized and accumulated relatively high amounts of P(3HB). The aim of this work was to establish if it could convert an inexpensive liquid waste product from the production of biodiesel, biodiesel liquid waste (BLW), to P(3HB). Using a mineral salt medium (MSM) containing 2.0 % (v/v) glycerol present in the BLW and both normal batch and a draw and fill culture method, B. aryabhattai ST1C produced a maximum P(3HB) content and biomass concentration of 72.31 % dry cell weight (DCW) and 7.24 g/L, respectively, over a 24 h cultivation period in the draw and fill cultivation method. From 24 h to the end of cultivation at 72 h both the P(3HB) content and the biomass concentrations continuously reduced. Concentrations of glycerol in the BLW in this MSM above 3.0 % (v/v) or from pure glycerol (PG) or with an added NaCl concentration of greater than 3.0 % significantly reduced both the maximum P(3HB) content and the biomass concentrations.     

Femtosecond laser-based mutagenesis strategy for micronomicin production enhancement of Micromonospora sagamiensis ATCC 21826

In this work, a mutant MX3004 with improved micronomicin (MCR) production was derived from Micromonospora sagamiensis ATCC21826, which was treated with femtosecond laser under the optimized irradiation conditions of 75 mW and 180 s, with a maximum of positive mutation rate of 17.8 % and the mortality rate of 69.2 %. A novel high-throughput method was established using microplate reader by quantifying the concentration of MCR for efficient screening of positive mutant from large numbers of mutants. Consequently, MX3004 displayed the highest MCR production capacity of 126 U/ml and a stable heredity (ten generations). Moreover, under the optimal fermentation conditions in a 7.5 l fermenter, the MCR production of MX3004 reached the maximum of 263 U/ml, which was increased by 484 % compared with the parent strain. The results suggest that femtosecond laser is a suitable method for the MCR production improvement and the screening method has a great potential application for aminoglycoside antibiotic production.     

SCREENING OF IRON- AND ZINC-ENRICHED YEAST STRAIN AND OPTIMIZATION OF CULTIVATION CONDITIONS

Saccharomyces cerevisiae LN-17 was selected from 26 kinds of primary yeast strains that belong to different genera and species. The iron- and zinc-enriched capability of strain LN-17 was higher than the others. The highest iron and zinc contents of the strain were obtained when the strain grew up under the following conditions: The strain was incubated (5%, v/v) in 50 mL wort medium (pH 6.0) with 100 mg/L Fe ion and 120 mg/L Zn ion. The medium was loaded into a 250-mL Erlenmeyer flask and shaken in a rotary shaker (200 rpm) at 30°C for 60 h. Ferrous sulfate and zinc sulfate were chosen as the source of Fe and Zn. The Fe and Zn contents of the dry cells were determined by atomic absorption spectrum analysis. Under the optimized cultivation conditions, the Fe and Zn contents reached 7.854 mg/g dry cells and 4.976 mg/g dry cells.     

Selective production of two diastereomers of disaccharide sugar alcohol, mannosylerythritol by Pseudozyma yeasts

Mannosylerythritol (ME) is the hydrophilic backbone of mannosylerythritol lipids as the most promising biosurfactants produced by different Pseudozyma yeasts, and has been receiving attention as a new sugar alcohol. Different Pseudozyma yeasts were examined for the sugar alcohol production using glucose as the sole carbon source. P. hubeiensis KM-59 highly produced a conventional type of ME, i.e., 4-O-β-d-mannopyranosyl-d-erythritol (4-ME). Interestingly, P. tsukubaensis KM-160 produced a diastereomer of 4-ME, i.e., 1-O-β-d-mannopyranosyl-d-erythritol (1-ME). In shake flask culture with 200 g/l of glucose, strain KM-59 produced 4-ME at a yield of 33.2 g/l (2.2 g/l/day of the productivity), while strain KM-160 produced 1-ME at 30.0 g/l (2.0 g/l/day). Moreover, the two strains were found to produce ME from glycerol; the maximum yields of 4-ME and 1-ME from 200 g/l of glycerol were 16.1 g/l (1.1 g/l/day) and 15.8 g/l (1.1 g/l/day), respectively. The production of 1-ME as the new diastereomer was further investigated in fed batch culture using a 5-l jar-fermenter. Compared to the flask culture, strain KM-160 gave three times higher productivity of 1-ME at 38.0 g/l (6.3 g/l/day) from glucose and at 31.1 g/l (3.5 g/l/day) from glycerol, respectively. This is the first report on the selective production of two diastereomers of ME, and should thus facilitate the functional development and application of the disaccharide sugar alcohol in the food and relative industries.     

Preparation of Mutants Resistant to Catabolite Repression of Trichoderma reesei

The development of agar plate screening techniques has allowed the isolation of mutants of Trichoderma reesei capable of synthesizing cellulase under the conditions of a high concentration of glucose. Mutants resistant to catabolite repression by glycerol or glucose were isolated on Walseth’s cellulose (WC) agar plates containing 5% glycerol or 5% glucose, respectively. Mutants resistant to catabolite repression by glycerol were not derepressed enough for the production of cellulase on WC agar plates containing 5% glucose or in flask cultures with a mixture of 1% Avicel and 3% glucose. On the contrary, two mutant strains resistant to catabolite repression by glucose (KDD-10 and DGD-16) produced large clearing zones on WC agar plates containing 5% glucose. Both strains could begin to produce CMCase even in the presence of residual glucose and finally produced 1.5 times the CMCase activity, in flask cultures on 1% Avicel and 3% glucose, than that with 1% Avicel alone. These results suggest that KDD-10 and DGD-16 are comparatively derepressed by glucose for cellulase production.     

Enterotoxin A production in Staphylococcus aureus: inhibition by glucose

In this study, we investigated the relationship between carbohydrate metabolism and repression of staphylococcus enterotoxin A (SEA) in Staphylococcus aureus 196E and a pleiotrophic mutant derived from strain 196E. The mutant, designated at strain 196E-MA, lacked a functional phosphoenolpyruvate phosphotransferase system (PTS). The mutant produced acid, under aerobic conditions, from only glucose and glycerol. The parent strain contained an active PTS, and aerobically produced acid from a large number of carbohydrates. Prior growth in glucose led to repression of SEA synthesis in the parent strain; addition to the casamino acids enterotoxin production medium (CAS) led to more severe repression of toxin synthesis. The repression was not related to pH decreases produced by glucose metabolism. When S. aureus 196E was grown in the absence of glucose, there was inhibition of toxin production as glucose level was increased in CAS. The inhibition was related to pH decrease and was unlike the repression observed with glucose-grown strain 196E. The inhibition of SEA synthesis in mutant strain 196E-MA was approximately the same in cells grown with or without glucose and was pH related. Repression of SEA synthesis similar to that seen with glucose-grown S. aureus 196E could not be demonstrated in the mutant. In addition, glucose-grown S. aureus 196E neither synthesized -galactosidase nor showed respiratory activity with certain tricarboxylic acid (TCA) cycle compounds. Glucose-grown strain 196E-MA, however, did not show supressed respiration of TCA cycle compounds; -galactosidase was not synthesized because the mutant lacked a functional PTS. Cyclic adenosine-3, 5-monophosphate did not reverse the repression by glucose of SEA or -galactosidase synthesis in glucose-grown S. aureus 196E. An active PTS appears to be necessary to demonstrate glucose (catabolite) repression in S. aureus.Abbreviations SEA staphylococcal enterotoxin A - SEB staphylococcal enterotoxin B - SEC staphylococcal enterotoxin C - PTS phosphoenolpyruvate phosphotransferase system - CAS casamino acids salts medium - TCA tricarboxylic acid cycle     

Improvement of Aspergillus oryzae NRRL 3484 by mutagenesis and optimization of culture conditions in solid-state fermentation for the hyper-production of extracellular cellulase

Spore suspensions of Aspergillus oryzae NRRL 3484 were subjected to mutagenesis using ultraviolet-irradiation followed by chemical treatments to improve the biosynthesis of cellulase. Ten mutant strains namely UEAC7, UEAR5, UNAC4, UNAC16, UNAR19, UNBC7, UNBR3, UNBR10, UNBR23 and UNBR25 were selected and their extracellular cellulase activities were assayed. Mutant UNAC4 gave the highest cellulase production [2,455 ± 28 U/g-dry substrate (ds) for filter paper-ase (FP-ase)] in a yield 4-fold exceeding that of the wild type strain (578 ± 5.0 U/g-ds for FP-ase). Rice straw (RS) was used as a sole carbon source for the enzyme production at a concentration of 10 % (w/v). Maximum cellulase production was achieved at initial medium pH 5.5, initial moisture content 77 % and an incubation temperature 28 °C on the fifth day of growth. NH₄Cl proved to be the suitable added nitrogen source for maximum enzyme production followed by peptone. These results clearly indicate the cost-effectiveness of solid state fermentation technology in the economic production of extracellular cellulase. The hyper-production of cellulase by mutant strain UNAC4 has potential for industrial processes that convert lignocellulosic material (e.g. RS) into products of commercial value such as glucose and biofuels.     

Optimization of Non-Nutritional Factors for a Cost-Effective Enhancement of Nisin Production Using Orthogonal Array Method

In order to increase nisin production in a cost-effective manner, non-nutritional factors as well as nutritional parameters must be optimized. In this study, optimization of the most important non-nutritional factors for nisin production using orthogonal array method was performed. Optimization of temperature, agitation, age and size of inoculum, medium initial pH value and flask volume/medium volume ratio in de Man, Rogosa and Sharpe (MRS) medium in batch fermentation was accomplished. Nisin was produced by Lactococcus lactis subsp. lactis PTCC 1336 and measured by bioassay method using Micrococcus luteus PTCC 1169 as the nisin-sensitive strain. The optimum levels of non-nutritional factors for maximum nisin production and productivity were obtained as: flask volume/medium volume ratio: 5.00, medium initial pH value: 8.00, inoculum size: 1%, inoculum age: 24 h old (A = 1.7), agitation: 100 rpm and temperature: 27 °C. Under the optimized conditions, maximum nisin production and maximum nisin productivity were 599.70 IU/mL and 37.48 IU/mL/h, respectively.     

Investigating the cryopreservation of nodal explants of Lithodora rosmarinifolia (Ten.) Johnst., a rare, endemic Mediterranean species

In this study, we investigated the possibility of using the droplet-vitrification technique for cryopreserving nodal segments of in vitro plantlets of the endangered plant species Lithodora rosmarinifolia. Among the three vitrification solutions tested, only solutions B1, containing (w/v) 50 % glycerol and 50 % sucrose, and B3, containing 40 % glycerol and 40 % sucrose, were able to induce cryotolerance in nodal explants, resulting in intermediate survival and recovery after cryopreservation. A three-step vitrification protocol, including an additional dehydration treatment with half-strength vitrification solution for 30 min before the treatment with full-strength vitrification solution, did not lead to any improvement in survival and recovery compared with the two-step protocol. The optimal protocol was the following: preculture of nodal segments in liquid medium with 0.3 M sucrose for 16 h and 0.7 M sucrose for 5 h, treatment for 20 min in loading solution containing 1.9 M glycerol + 0.5 M sucrose, dehydration with vitrification solution B1 (glycerol 50.0 %, sucrose 50.0 %, w/v) for 60 min at room temperature, rapid cooling in minute droplets of vitrification solution, and rapid rewarming by immersion of nodal segments for 20 min in unloading solution containing 1.2 M sucrose. Under these conditions, 33 % recovery of cryopreserved nodal explants was achieved. Regrowth of cryopreserved samples was rapid and direct. These results indicate that long-term storage of L. rosmarinifolia by means of cryopreservation of nodal segments is possible, thereby contributing to securing the diversity of this rare and endangered plant species.     

Enhancement of β-galactosidase productivity of Aspergillus niger NCIM-616

A series of mutations was carried out with Aspergillus niger NCIM-616 as the parent strain. A mutant strain NG-4 with 28% increased β-galactosidase productivity was produced with N -methyl- N -nitro- N -nitrosoguanidine (NTG) at 1500µg ml^-1 concentration and exposure timeof 60 min. This mutant yielded a third generation u.v.-treated strain, UV—5 with a 117·6% increase in β-galactosidase productivity with respect to the parent strain.