Optimization of the cryopreservation of African clawed frog (Xenopus laevis) sperm

Cryopreservation of testicular sperm in the African clawed frog, Xenopus laevis, was tested using three penetrating cryoprotectants (DMSO, methanol, and glycerol) and three semen diluents (300 mmol/L glucose, 300 mmol/L sucrose, and a motility inhibiting saline [MIS] solution [150 mmol/L NaCl, 3 mmol/L KCL, 1 mmol/L Mg₂SO₄, 1 mmol/L CaCl₂, and 20 mmol/L Tris, pH 8.0]). Three freezing rates and four thawing rates were also tested, and the best freezing/thawing conditions have been determined. The responses of sperm motility, viability, and fertility were assessed. Incubation of the sperm macerates with penetrating cryoprotectants showed that DMSO was the least toxic and methanol the most toxic. Semen in cryodiluents frozen 10 cm above the surface of liquid nitrogen (freezing rate of 20 to 25 °C/min) and thawed at room temperature for 40 sec had significantly higher percentages of motile and viable sperm than that of semen frozen 5 cm or 8 cm above the surface of liquid nitrogen and thawed at 5, 25, or 30 °C for 10, 15, or 60 sec, respectively. Sperm frozen in MIS containing 5% DMSO had a higher hatching rate than that of sperm frozen in sucrose and glucose diluents containing 5% or 10% DMSO and in MIS containing 10% DMSO. Addition of 73 mmol/L sucrose to the sperm extender MIS + 5% DMSO could improve the postthaw sperm motility and fertility. In conclusion, dilution of collected sperm in MIS solution (to have a final concentration of 6.5 × 10⁶ to 8 × 10⁶/mL) containing 5% DMSO and 73 mmol/L sucrose, freezing in a vapor of liquid nitrogen at 10 cm above the surface, and thawing at room temperature for 40 sec was the best cryopreservation protocol. This protocol gave 70% hatching rate, 80% motility rate, and 75% viability rate of fresh hormonally induced sperm.     

An improved bioprocess for synthesis of acetohydroxamic acid using DTT (dithiothreitol) treated resting cells of Bacillus sp. APB-6

Acyltransferase activity of amidase from Bacillus sp. APB-6 was enhanced (24 U) by multiple feedings of N-methylacetamide (70 mM) into the production medium. Hyperinduced whole resting cells of Bacillus sp. APB-6 corresponding to 4 g/L (dry cell weight), when treated with 10 mM DTT (dithiothreitol) resulted in 93% molar conversion of acetamide (300 mM) to acetohydroxamic acid in presence of hydroxylamine-HCl (800 mM) after 30 min at 45 °C in a 1 L reaction mixture. After lyophilization, a 62 g powder containing 34% (wt wt⁻¹) acetohydroxamic acid was recovered. This is the first report where DTT has been used to enhance acyltransfer reaction and such high molar conversion (%) of amide to hydroxamates was recorded at 1 L scale.     

Biotransformation of glycerol to 3-hydroxypropionaldehyde: Improved production by in situ complexation with bisulfite in a fed-batch mode and separation on anion exchanger

3-Hydroxypropionaldehyde (3HPA) is an important C3 chemical that can be produced from renewable glycerol by resting whole cells of Lactobacillus reuteri. However the process efficiency is limited due to substrate inhibition, product-mediated loss of enzyme activity and cell viability, and also formation of by-products. Complex formation of 3HPA with sodium bisulfite and subsequent binding to Amberlite IRA-400 was investigated as a means of in situ product recovery and for overcoming inhibition. The adsorption capacity and -isotherm of the resin were evaluated using the Langmuir model. The resin exhibited maximum capacity of 2.92 mmol complex/g when equilibrated with 45 mL solution containing an equilibrium mixture of 2.74 mmol 3HPA-bisulfite complex and 2.01 mmol free 3HPA. The dynamic binding capacity based on the breakthrough curve of 3HPA and its complex on passing a solution with 2.49 mmol complex and 1.65 mmol free 3HPA was 2.01 mmol/g resin. The bound 3HPA was desorbed from the resin using 0.20 M NaCl with a high purity as a mixture of complexed- and free 3HPA at a ratio of 0.77 mol/mol. Fed-batch biotransformation of glycerol (818.85 mmol) with in situ 3HPA complexation and separation on the bisulfite-functionalized resin resulted in an improved process with consumption of 481.36 mmol glycerol yielding 325.54 mmol 3HPA at a rate of 17.13 mmol/h and a yield of 68 mol%. Also, the cell activity was maintained for at least 28 h.     

Use of glycerol for producing 1,3-dihydroxyacetone by Gluconobacter oxydans in an airlift bioreactor

1,3-Dihydroxyacetone can be produced by biotransformation of glycerol with glycerol dehydrogenase from Gluconobacter oxydans cells. Firstly, improvement the activity of glycerol dehydrogenase was carried out by medium optimization. The optimal medium for cell cultivation was composed of 5.6 g/l yeast extract, 4.7 g/l glycerol, 42.1 g/l mannitol, 0.5 g/l K₂HPO₄, 0.5 g/l KH₂PO₄, 0.1 g/l MgSO₄·7H₂O, and 2.0 g/l CaCO₃ with the initial pH of 4.9. Secondly, an internal loop airlift bioreactor was applied for DHA production from glycerol by resting cells of G. oxydans ZJB09113. Furthermore, the effects of pH, aeration rate and cell content on DHA production and glycerol feeding strategy were investigated. 156.3 ± 7.8 g/l of maximal DHA concentration with 89.8 ± 2.4% of conversion rate of glycerol to DHA was achieved after 72 h of biotransformation using 10 g/l resting cells at 30 °C, pH 5.0 and 1.5 vvm of aeration rate.     

Hydrogen production by immobilized R. faecalis RLD-53 using soluble metabolites from ethanol fermentation bacteria E. harbinense B49

In order to increase the hydrogen yield from glucose, hydrogen production by immobilized Rhodopseudomonas faecalis RLD-53 using soluble metabolites from ethanol fermentation bacteria Ethanoligenens harbinense B49 was investigated. The soluble metabolites from dark-fermentation mainly were ethanol and acetate, which could be further utilized for photo-hydrogen production. Hydrogen production by B49 was noticeably affected by the glucose and phosphate buffer concentration. The maximum hydrogen yield (1.83 mol H₂/mol glucose) was obtained at 9 g/l glucose. In addition, we found that the ratio of acetate/ethanol (A/E) increased with increasing phosphate buffer concentration, which is favorable to further photo-hydrogen production. The total hydrogen yield during dark- and photo-fermentation reached its maximum value (6.32 mol H₂/mol glucose) using 9 g/l glucose, 30 mmol/l phosphate buffers and immobilized R. faecalis RLD-53. Results demonstrated that the combination of dark- and photo- fermentation was an effective and efficient process to improve hydrogen yield from a single substrate.     

Continuous culture of the microalgae Schizochytrium limacinum on biodiesel-derived crude glycerol for producing docosahexaenoic acid

Crude glycerol is a major byproduct of the biodiesel industry; previous research has proved the feasibility of producing docosahexaenoic acid (DHA, 22:6 n − 3) through fermentation of the algae Schizochytrium limacinum on crude glycerol. The objective of this work is to investigate the cell growth kinetics, substrate utilization efficiency, and DHA production of the algae through a continuous culture. Steady-state biomass yield, biomass productivity, growth yield on glycerol, specific glycerol consumption rate, and fatty acid composition were investigated within the range of dilution rate (D) from 0.2 to 0.6 day⁻¹, and the range of feed crude glycerol concentration (S₀) from 15 to 120 g/L. The maximum specific growth rate was determined as 0.692 day⁻¹. The cells had a true growth yield of 0.283 g/g but with a relatively high maintenance coefficient (0.2216 day⁻¹). The highest biomass productivity of 3.88 g/L-day was obtained at D = 0.3 day⁻¹ and S₀ = 60 g/L, while the highest DHA productivity (0.52 g/L-day) was obtained at D = 0.3 day⁻¹ and S₀ = 90 g/L due to the higher DHA content at S₀ = 90 g/L. The biomass and DHA productivity of the continuous culture was comparable to those of batch culture, while lower than the fed-batch culture, mainly because of the lower DHA content obtained by the continuous culture. Overall, the results show that continuous culture is a powerful tool to investigate the cell growth kinetics and physiological behaviors of the algae growing on biodiesel-derived crude glycerol.     

Kinetics of an extracellular exo-inulinase production from a 5-flourocytosine resistant mutant of Geotrichum candidum using two-factorial design

In the present study, eight different strains of Geotrichum candidum were isolated and screened for an extracellular exo-inulinase production using chemically enriched sucrose–mineral media. The isolate (Zool-3i) with a better enzyme activity (1.38 IU/ml) was subjected to induced mutagenesis using methyl methane sulphonate (MMS) and a mutant with an enzyme activity of 32.06 IU/ml was obtained. Further exposure to ethyl methane sulphonate (EMS) and ultraviolet (UV) radiations yielded a mutant exhibiting an improved activity of 39.34 IU/ml. The potential mutant was cultured overnight and plated on 5fc–YPR agar medium and thus made resistant against 5-flourocytocine. Over 50-fold enhancement in enzyme production (71.85 IU/ml) was achieved when the process parameters including incubation period (48 h), sucrose concentration (5.0 g/L), pH (6.0), inoculum size (2.0%, 16 h old) and urea (0.2%) were identified using Plackett–Burman design. On the basis of kinetic variables, notably Q_p (0.723 U/g/h), Y_p/s (2.036 U/g) and q_p (0.091 U/g cells/h), the mutant MEU-5fc-6 was found to be a hyper producer of exo-inulinase (HS, LSD 0.045, p ? 0.05).     

Biological hydrogen production by the algal biomass Chlorella vulgaris MSU 01 strain isolated from pond sediment

Chlorella vulgaris MSU 01 strain isolated from the sediment of the pond is able to produce molecular hydrogen in a clean way. To relate the dynamic coupling between the cultural conditions and biological responses, an original lab scale set up has been developed for hydrogen production. Different sources like mannitol, glucose, alanine, citric acid, aspartic acid, l-alanine, l-cysteine, sodium succinate and sodium pyruvate were used for algal media optimization. Corn stalk, from 1 to 5 g/L was tested for the effective algal growth and hydrogen production. The cell concentration of 1.6-19 g/L dry cell weight (DCW) was found at the 10th day. The kinetic parameters involved in the hydrogen production at 4 g/L corn stalk using the algal inoculum (50 mL) in the bioreactor volume (500 mL) was found to be with the hydrogen production potential (P_s) of 7.784 mL and production yield of (P_r) 5.534 mL respectively. The growth profile of the algal biomass at the above mentioned condition expressed the logistic model with R² 0.9988. The final pH of the broth was increased from 7.0 to 8.5-8.7. The anaerobic fermentation by C. vulgaris MSU 01 strain involved in the conversion process of complex carbon source has increased the H₂ evolution rate and higher butyrate concentration in the fermentate.     

Production of medium-chain-length polyhydroxyalkanoates by activated sludge enriched under periodic feeding with nonanoic acid

The potential use of activated sludge for the production of medium-chain-length polyhydroxyalkanoates (MCL-PHAs) was investigated. The enrichment of bacterial populations capable of producing MCL-PHAs was achieved by periodic feeding with nonanoic acid in a sequencing batch reactor (SBR). Denaturing gradient gel electrophoresis analysis revealed Pseudomonas aeruginosa strains to be predominant in the bacterial community during the SBR process. The composition of PHA synthesized by the enriched biomass from nonanoic acid consisted of a large concentration (>89 mol%) of MCL monomer units and a small amount of short-chain-length monomer units. Under fed-batch fermentation with continuous feeding of nonanoic acid at a flow rate of 0.225 g/L/h and a C/N ratio of 40, a maximum PHA content of 48.6% dry cell weight and a conversion yield (Y_p/s) of 0.94 g/g were achieved. These results indicate that MCL-PHA production by activated sludge is a promising alternative to typical pure culture approaches.     

Sequential production of two biopolymers-levan and poly-ε-lysine by microbial fermentation

Sequential fermentation for the production of two invaluable biopolymers, levan and poly-ε-lysine (ε-PL), has been successfully developed. It involves fermentation of Bacillus subtilis (natto) Takahashi in sucrose medium to produce levan, separation of levan product from small remaining sugar molecules by ultrafiltration and fermentation of the remnant from levan production by Streptomyces albulus to produce ε-PL. In the process, 50-60 g/L of levan was produced (100% recovery after precipitation by ethanol). The remnant from levan production with glucose adjusted to 30 g/L and with combined use of yeast extract (10 g/L), (NH₄)₂SO₄ (2 g/L) and basal salts was proven to be suitable for ε-PL production. 4.37 g/L of ε-PL accumulation (85% recovery after purification) was reached in 72 h using two-stage fermentation with control of pH. The process of using remnant (waste) from levan fermentation for the second biopolymer (ε-PL) production is unprecedented and the products obtained are environmental-friendly.     

Biohydrogen production by immobilized Chlorella sp. using cycles of oxygenic photosynthesis and anaerobiosis

Hydrogen production was studied using immobilized green alga Chlorella sp. through a two-stage cyclic process where immobilized cells were first incubated in oxygenic photosynthesis followed by anaerobic incubation for H₂ production in the absence of sulfur. Chlorella sp. used in this study was capable of generating H₂ under immobilized state in agar. The externally added glucose enhanced H₂ production rates and total produced volume while shortened the lag time required for cell adaptation prior to H₂ evolution. The rate of hydrogen evolution was increased as temperature increased, and the maximum evolution rate under 30 mM glucose was 183 mL/h/L and 238 mL/h/L at 37 °C and 40 °C, respectively. In order to continue repeated cycles of H₂ production, at least two days of photosynthesis stage should be allowed for cells to recover H₂ production potential and cell viability before returning to H₂ production stage again.     

Process development of succinic acid production by Escherichia coli NZN111 using acetate as an aerobic carbon source

Escherichia coli strain NZN111 could convert glucose to succinic acid efficiently in anaerobic conditions after the induction of gluconeogenic carbon sources in aerobic conditions. Acetate shows a strong effect on both yield and productivity of succinic acid. In this study, the fed-batch process of succinic acid production by NZN111 using acetate in a chemically defined medium in the aerobic stage was investigated and developed. Increasing cell density could increase succinic acid with a productivity of 3.97 g/(L h) in the first 8 h of the anaerobic phase with an overall yield of 1.42 mol/mol glucose in a 5 L fermentor. However, there was strong repression from succinic acid in the later anaerobic stage. When succinic acid exceeded 30 g/L, the glucose consumption rate began to drop sharply along with the succinic acid production rate. Supplementation with glucose from 30 to 70 g/L in the anaerobic stage showed little effect on succinic acid production. Acetic acid and pyruvic acid accumulated had no effect on succinic acid formation because of their low concentration. With acetate as the sole carbon source for aerobic cultivation in the following scale-up, 60.09 g/L of succinic acid was produced with a yield of 1.37 mol/mol in a 50 L bioreactor.     

Optimisation of exopolysaccharide production by Gomphidius rutilus and its antioxidant activities in vitro

The production conditions of the Gomphidius rutilus exopolysaccharides (GREP) in submerged culture were optimised, and the antioxidant activities of GREP in vitro were evaluated. The optimal culture medium constituents were determined as follows: 30 g/L sucrose, 3.0 g/L soybean meal, 0.25 g/L MgSO₄, 1.5 g/L K₂HPO₄, 0.5 g/L KH₂PO₄, 0.03 g/L ZnSO₄, and 0.01 g/L FeSO₄. The optimum parameters for the liquid fermentation were as follows: temperature, 25 °C; cultivation time, 6 d; initial pH, 8.0; volume of medium, 150 mL; and rotary speed, 180 rpm. GREP content and dry cell weight in optimised conditions were 540.1 ± 15.9 mg/L and 8.2 ± 0.3 g/L, respectively. GREP content under the optimised conditions was 2.5 times than that under the basic culture medium and initial conditions. GREP demonstrated positive antioxidant potential on superoxide anion radical, 1,1-diphenyl-2-picrylhydrazyl, and hydroxyl radical scavenging, and reducing power.     

Production of succinic acid from sucrose and sugarcane molasses by metabolically engineered Escherichia coli

Sucrose-utilizing genes (cscKB and cscA) from Escherichia coli KO11 were cloned and expressed in a metabolically engineered E. coli KJ122 to enhance succinate production from sucrose. KJ122 harboring a recombinant plasmid, pKJSUC, was screened for the efficient sucrose utilization by growth-based selection and adaptation. KJ122-pKJSUC-24T efficiently utilized sucrose in a low-cost medium to produce high succinate concentration with less accumulation of by-products. Succinate concentrations of 51 g/L (productivity equal to 1.05 g/L/h) were produced from sucrose in anaerobic bottles, and concentrations of 47 g/L were produced in 10 L bioreactor within 48 h. Antibiotics had no effect on the succinate production by KJ122-pKJSUC-24T. In addition, succinate concentrations of 62 g/L were produced from sugarcane molasses in anaerobic bottles, and concentrations of 56 g/L in 10 L bioreactor within 72 h. These results demonstrated that KJ122-pKJSUC-24T would be a potential strain for bio-based succinate production from sucrose and sugarcane molasses.     

Simultaneous production of citric acid and invertase by Yarrowia lipolytica SUC+ transformants

Simultaneous production of citric acid (CA) and invertase by Yarrowia lipolytica A-101-B56-5 (SUC⁺ clone) growing from sucrose, mixture of glucose and fructose, glucose or glycerol was investigated. Among the tested substrates the highest concentration of CA was reached from glycerol (57.15 g/L) with high yield (Y_CA/S = 0.6 g/g). When sucrose was used, comparable amount of CA was secreted (45 g/L) with slightly higher yield (Y_CA/S = 0.643 g/g). In all cultures amount of isocitrate (ICA) was below 2% of total citrates. Considering invertase production, the best carbon source appeared to be sucrose (72 380 U/L). The highest yield of CA and invertase biosynthesis calculated for 1 g of biomass was obtained for cells growing from glycerol (9.9 g/g and 4325 U/g, respectively). Concentrates of extra- and intracellular invertase of the highest activity were obtained from sucrose as substrate (0.5 and 1.8 × 10⁶ U/L, respectively).     

Enhanced resistance of Saccharomyces cerevisiae to vanillin by expression of lacA from Trametes sp. AH28-2

Saccharomyces cerevisiae is affected by the presence of certain phenolic compounds such as vanillin during fermentation of pretreated lignocellulosic hydrolysates. Since vanillin can be polymerized in the presence of laccase into compounds with lower toxicity, the laccase gene, lacA, from Trametes sp. AH28-2 was fused to the α-factor signal sequence and transferred into S. cerevisiae CEN.PK strains for secretory expression. Furthermore, the chaperone gene, KAR2, was overexpressed to promote the translocation of laccase. In the presence of 8 mmol/L vanillin, a shorter lag phase was observed in the lacA gene expressing strains. The vanillin-specific conversion rate of the lacA-expressing strain BSJX0A2 was 0.069 g g⁻¹ biomass h⁻¹, while it was 0.065 g g⁻¹ biomass h⁻¹ in the reference strain.     

Microbial production of N-acetylneuraminic acid by genetically engineered Escherichia coli

Previously, we described the production of N-acetylneuraminic acid (NeuAc) from N-acetylglucosamine (GlcNAc) in a system combining recombinant Escherichia coli expressing GlcNAc 2-epimerase (slr1975), E. coli expressing NeuAc synthetase (neuB), and Corynebacterium ammoniagenes. However, this system was unsuitable for large-scale production because of its complexity and low productivity. To overcome these problems, we constructed a recombinant E. coli simultaneously overexpressing slr1975 and neuB. This recombinant E. coli produced 81 mM (25 g/L) NeuAc in 22 h without the addition of C. ammoniagenes cells. For manufacturing on an industrial scale, it is preferable to use unconcentrated culture broth as the source of enzymes, and therefore, a high-density cell culture is required. An acetate-resistant mutant strain of E. coli (HN0074) was selected as the host strain because of its ability to grow to a high cell density. The NeuAc aldolase gene of E. coli HN0074 was disrupted by homologous recombination yielding E. coli N18-14, which cannot degrade NeuAc. After a 22 h reaction with 540 mM (120 g/L) GlcNAc in a 5 L jar fermenter, the culture broth of E. coli N18-14 overexpressing slr1975 and neuB contained 172 mM (53 g/L) NeuAc.     

Isolation,identification and characterization of a novel Rhodococcus sp. strain in biodegradation of tetrahydrofuran and its medium optimization using sequential statistics-based experimental designs

Statistics-based experimental designs were applied to optimize the culture conditions for tetrahydrofuran (THF) degradation by a newly isolated Rhodococcus sp. YYL that tolerates high THF concentrations. Single factor experiments were undertaken for determining the optimum range of each of four factors (initial pH and concentrations of K₂HPO₄ · 3H₂O, NH₄Cl and yeast extract) and these factors were subsequently optimized using the response surface methodology. The Plackett–Burman design was used to identify three trace elements (Mg²⁺, Zn²⁺and Fe²⁺) that significantly increased the THF degradation rate. The optimum conditions were found to be: 1.80 g/L NH₄Cl, 0.81 g/L K₂HPO₄ · 3H₂O, 0.06 g/L yeast extract, 0.40 g/L MgSO₄ · 7H₂O, 0.006 g/L ZnSO₄ · 7H₂O, 0.024 g/L FeSO₄ · 7H₂O, and an initial pH of 8.26. Under these optimized conditions, the maximum THF degradation rate increased to 137.60 mg THF h⁻¹ g dry weight in Rhodococcus sp. YYL, which was nearly five times of that by the previously described THF degrading Rhodococcus strain.     

Evaluation of bioenergy recovery processes treating organic residues from ethanol fermentation process

This study evaluates a two-stage bioprocess for recovering bioenergy in the forms of hydrogen and methane while treating organic residues of ethanol fermentation from tapioca starch. A maximum hydrogen production rate of 0.77 mmol H₂/g VSS/h can be achieved at volumetric loading rate (VLR) of 56 kg COD/m³/day. Batch results indicate that controlling conditions at S₀/X₀ = 12 with X₀ = 4000 mg VSS/L and pH 5.5-6 are important for efficient hydrogen production from fermentation residues. Hydrogen-producing bacteria enriched in the hydrogen bioreactor are likely utilizing lactate and acetate for biohydrogen production from ethanol-fermentation residues. Organic residues remained in the effluent of hydrogen bioreactor can be effectively converted to methane with a rate of 0.37 mmol CH₄/g VSS/h at VLR of 8 kg COD/m³/day. Approximately 90% of COD in ethanol-fermentation residues can be removed and among that 2% and 85.1% of COD can be recovered in the forms of hydrogen and methane, respectively.     

Optimization of lab scale methanol production by <Emphasis Type="Italic">Methylosinus trichosporium</Emphasis> OB3b

Methylosinus trichosporium OB3b is a methanotrophic bacterium containing particulate methane monooxygenase (MMO), which catalyzes the hydroxylation of methane to methanol. The methanol is further oxidized to formaldehyde by methanol dehydrogenase (MDH). We developed a novel compulsory circulation diffusion system for cell cultivation. A methane/air mixture (1:1, v/v) was prepared in a tightly sealed gas reservoir and pumped into a nitrate mineral salt culture medium under optimal conditions (5 μM CuSO₄, pH 7.0, 30°C). Cells were harvested, washed, and resuspended (0.6 mg dry cells/mL) in a 500 mL flask in 100 mL of 10 mM phosphate buffer (pH 7.0) containing 100 mM NaCl and 1 mM EDTA as MDH inhibitors, and 20 mM sodium formate. A single 12 h batch reaction at 25°C yielded a final concentration of 13.2 mM methanol. The use of a repeated batch mode, in which the accumulated methanol was removed after each of three 8 h cycles over a 24 h period, showed a productivity of 2.17 μmol methanol/h/mg dry cell wt. Finally, a lab-scale reaction performed using a 3 L cylindrical reactor with a working volume of 1 L produced 13.7 mM methanol after 16 h. Our results identify a simple process for improving the productivity of biologically derived methanol and, therefore the utility of methane as an energy source.