Efficient production of l-lactic acid from hydrolysate of Jerusalem artichoke with immobilized cells of Lactococcus lactis in fibrous bed bioreactors

Hydrolysate of Jerusalem artichoke was applied for the production of l-lactic acid by immobilized Lactococcus lactis cells in a fibrous bed bioreactor system. Preliminary experiments had indicated that the high quality hydrolysate, which was derived from the 40min acid treatment at 95°C and pH 1.8, was sufficient to support the cell growth and synthesis of l-lactic acid. With the addition of 5g/l yeast extract, the fermentative performance of free cell system was evidently improved. After the basal settlement of hydrolysate based fermentation, the batch mode and the fed-batch mode fermentation were carried out in the free cell system and the fibrous bed bioreactor system, respectively. In all cases the immobilized cells presented the superior ability to produce l-lactic acid. The comparison of batch mode and fed-batch mode also indicated that the growth-limiting feeding strategy could reduce the lag phase of fermentation process and enhance the production of l-lactic acid. The achieved maximum concentration of l-lactic acid was 142g/l in the fed-batch mode. Subsequent repeated-batch fermentation of the fibrous bed bioreactor system had further exhibited the persistence and stability of this system for the high production of l-lactic acid in a long term. Our work suggested the great potential of the fibrous bed bioreactor system and hydrolysate of J. artichoke in the economical production of l-lactic acid at industrial scale.     

Enhanced fed-batch production of pyrroloquinoline quinine in <Emphasis Type="Italic">Methylobacillus</Emphasis> sp. CCTCC M2016079 with a two-stage pH control strategy

The effects of pH control strategy and fermentative operation modes on the biosynthesis of pyrroloquinoline quinine (PQQ) were investigated systematically with Methylobacillus sp. CCTCC M2016079 in the present work. Firstly, the shake-flask cultivations and benchtop fermentations at various pH values ranging from 5.3 to 7.8 were studied. Following a kinetic analysis of specific cell growth rate (μ _x ) and specific PQQ formation rate (μ _p ), the discrepancy in optimal pH values between cell growth and PQQ biosynthesis was observed, which stimulated us to develop a novel two-stage pH control strategy. During this pH-shifted process, the pH in the broth was controlled at 6.8 to promote the cell growth for the first 48 h and then shifted to 5.8 to enhance the PQQ synthesis until the end of fermentation. By applying this pH-shifted control strategy, the maximum PQQ production was improved to 158.61 mg/L in the benchtop fermenter, about 44.9% higher than that under the most suitable constant pH fermentation. Further fed-batch study showed that PQQ production could be improved from 183.38 to 272.21 mg/L by feeding of methanol at the rate of 11.5 mL/h in this two-stage pH process. Meanwhile, the productivity was also increased from 2.02 to 2.84 mg/L/h. In order to support cell growth during the shifted pH stage, the combined feeding of methanol and yeast extract was carried out, which brought about the highest concentration (353.28 mg/L) and productivity (3.27 mg/L/h) of PQQ. This work has revealed the potential of our developed simple and economical strategy for the large-scale production of PQQ.     

Efficient chemoenzymatic synthesis of uridine 5′-diphosphate N-acetylglucosamine and uridine 5′-diphosphate N-trifluoacetyl glucosamine with three recombinant enzymes

Uridine 5′-diphosphate N-acetylglucosamine (UDP-GlcNAc) is a natural UDP-monosaccharide donor for bacterial glycosyltransferases, while uridine 5′-diphosphate N-trifluoacetyl glucosamine (UDP-GlcNTFA) is its synthetic mimic. The chemoenzymatic synthesis of UDP-GlcNAc and UDP-GlcNTFA was attempted by three recombinant enzymes. Recombinant N-acetylhexosamine 1-kinase was used to produce GlcNAc/GlcNTFA-1-phosphate from GlcNAc/GlcNTFA. N-acetylglucosamine-1-phosphate uridyltransferase from Escherichia coli K12 MG1655 was used to produce UDP-GlcNAc/GlcNTFA from GlcNAc/GlcNTFA-1-phosphate. Inorganic pyrophosphatase from E. coli K12 MG1655 was used to hydrolyze pyrophosphate to accelerate the reaction. The above enzymes were expressed in E. coli BL21 (DE3) and purified, respectively, and finally mixed in one-pot bioreactor. The effects of reaction conditions on the production of UDP-GlcNAc and UDP-GlcNTFA were characterized. To avoid the substrate inhibition effect on the production of UDP-GlcNAc and UDP-GlcNTFA, the reaction was performed with fed batch of substrate. Under the optimized conditions, high production of UDP-GlcNAc (59.51?g/L) and UDP-GlcNTFA (46.54?g/L) were achieved in this three-enzyme one-pot system. The present work is promising to develop an efficient scalable process for the supply of UDP-monosaccharide donors for oligosaccharide synthesis.     

Efficient expression and purification of recombinant alcohol oxidase in Pichia pastoris

In order to improve the production of alcohol oxidase (AOX), a recombinant Pichia pastoris (P. pastoris) system was constructed by transformation of the plasmid pPIC9K-AOX into P. pastoris GS115. The effects of different expression conditions on alcohol oxidase activity in the culture supernatant were investigated in the shake flask scale. The results showed that the highest extracellular activity (562 U/L) of alcohol oxidase was obtained after 56 h induction with 4% methanol at OD₆₀₀ 1.0 in the medium containing 50 g/L maltose, which is about 4.2 folds higher than previously reported. High-purity functional recombinant AOX (>90%) was purified from the culture with the Ni-NTA affinity column and Sephadex G-100 chromatographical methods, with a total recovery rate of 68.9%. Further studies showed that the purified rAOX had similar enzymatic characteristics as the native enzyme, except that the thermal stability and resistance to H₂O₂ inhibition of rAOX were significantly greater compared to the previous report. The purified rAOX was well tolerant to various water-miscible organic solvents. This efficient expression and purification process will be promising for large-scale production of rAOX as an important diagnostic enzyme for alcohol detection in many areas.     

Generation of high-yield rapamycin-producing strains through protoplasts-related techniques

Rapamycin is a 31-member ring macrolide produced by Streptomyces hygroscopicus and has many applications in clinical medicine. In the present work, several protoplasts-related techniques including protoplasts mutation, intraspecies and interspecies protoplasts fusion were tried to improve the rapamycin productivity in S. hygroscopicus. Although mutation and fusion of different protoplasts of S. hygroscopicus did not improve the productivity of rapamycin significantly, the interspecies fusion of protoplasts of S. hygroscopicus D7-804 and Streptomyces erythreus ZJU325 could have brought about one high-yield (345 mg/L) rapamycin producer with 23.6% higher than that of the parental strain. Then, with seven mutants of S. hygroscopicus with different features and rapamycin productivities as the parental strains, only one-round genome shuffling has generated a high-yield rapamycin-producing strain with an outstanding yield of 445 mg/L. The systematic research of protoplast-related techniques has established an applicable way to generate high-yield strains from original microorganisms which can only produce low amount of expected natural products, without information of target gene clusters and gene sequences.     

EFFICIENT PRODUCTION OF URIDINE 5′-DIPHOSPHO-N-ACETYLGLUCOSAMINE BY THE COMBINATION OF THREE RECOMBINANT ENZYMES AND YEAST CELLS

Uridine 5′-diphospho N-acetylglucosamine (UDP-GlcNAc) is an important nucleotide sugar in the biochemistry of all living organisms, and it is an important substrate in the synthesis of oligosaccharides. In the present work, three bioactive enzymes, namely, glucokinase (YqgR), GlcNAc-phosphate mutase (Agm1), and N-acetylglucosamine-1-phosphate uridyltransferase (GlmU), were produced effectively as soluble form in recombinant Escherichia coli. These three enzymes and dried yeast together were used to construct a multistep enzymatic system, which could produce UDP-GlcNAc efficiently with N-acetylglucosamine (GlcNAc) as the substrate. After the optimization of various reaction conditions, 31.5 mMUDP-GlcNAc was produced from 50 mMGlcNAc and 50 mMUMP.     

High‐level production of soluble pyrroloquinoline quinone‐dependent glucose dehydrogenase in Escherichia coli

Pyrroloquinoline quinone‐dependent glucose dehydrogenase (EC1.1.5.2, PQQGDH) has attracted progressive attention due to its application in glucose detection in clinic diagnosis and industrial bioprocess controls. To satisfy its increasing demand, improvement of PQQGDH production derived from Acinetobacter calcoaceticus L.M.D. 79.41 in recombinant Escherichia coli is necessary and is therefore the focus of the current study. Different carbon sources as well as induction conditions were investigated for overexpression of soluble PQQGDH. The results indicate that the target protein was optimally produced with 20 g/L glucose as the substrate. Moreover, the highest expression level (1530 kU/L) was achieved by a novel two‐temperature cultivation strategy in the 10‐L fermentor. This presents a sixfold improvement over previously reported values. After Ni‐NTA affinity chromatography purification, high‐purity enzyme with the specific activity of 5811 U/mg was obtained with a purification yield of 55%. The purified recombinant PQQGDH showed thermal stability and substrate specificity as the native enzyme. In summary, this work provides an alternative production process to overexpress PQQGDH and shows high applicability for large‐scale production of this important glucose dehydrogenase.     

Novel and efficient screening of PQQ high-yielding strains and subsequent cultivation optimization

A novel and efficient screening method for pyrroloquinoline quinone (PQQ) high-yielding methylotrophic strains was developed by using glucose dehydrogenase apoenzyme (GDHA) which depended on PQQ as the cofactor. Using this high-throughput method, PQQ high-yielding strains were rapidly screened out from thousands of methylotrophic colonies at a time. The comprehensive phylogenetic analysis revealed that the highest PQQ-producing strain zju323 (CCTCC M 2016079) could be assigned to a novel species in the genus Methylobacillus of the Betaproteobacteria. After systematic optimization of different medium components and cultivation conditions, about 33.4 mg/L of PQQ was obtained after 48 h of cultivation with Methylobacillus sp. zju323 at the shake flask scale. Further cultivations of Methylobacillus sp. zju323 were carried out to investigate the biosynthesis of PQQ in 10-L bench-top fermenters. In the batch operation, the PQQ accumulation reached 78 mg/L in the broth after 53 h of cultivation. By adopting methanol feeding strategy, the highest PQQ concentration was improved up to 162.2 mg/L after 75 h of cultivation. This work developed a high-throughput strategy of screening PQQ-producing strains from soil samples and also demonstrated one potential bioprocess for large-scale PQQ production with the isolated PQQ strain.     

The biosynthesis and bioactivity evaluation of the cytosine-substituted mildiomycin analogue (MIL-C) for controlling powder mildew

Powdery mildew is one of the most destructive plant diseases and causes dramatic yield losses in agricultural production. Mildiomycin (MIL) is an effective nucleoside antibiotics used to against such a devastating disease. In order to further improve the bioactivity of MIL, a cytosine-substituted mildiomycin analogue (MIL-C) was biosynthesized by supplementing 0.9 g/L cytosine into the fermentation medium as the precursor. The bioactivity of MIL-C against powdery mildew disease in vivo and in vitro were examined systematically, and compared to MIL and triadimefon. The minimum inhibitory concentration (MIC) of MIL-C in vitro was 78.8 mg/L, which was only half of that of MIL. Furthermore, in the greenhouse trials, the EC₉₀ value of MIL-C (52.89 mg/L) was much lower than that of either MIL (153.22 mg/L) or triadimefon (288.90 mg/L). In the field trials, the efficiency of MIL-C against powdery mildew of cucumber or pumpkin was better than that of MIL or triadimefon. Further acute toxicological and Ames tests proved that MIL-C was a potent bio-pesticide with good bio-compatibility and low toxicity, and its usage can be proposed to popularize for controlling the powdery mildew in the future.