响应面法优化褐藻胶降解菌Cobetia sp.20发酵培养基

为了提高褐藻胶降解菌株Cobetia sp.20产褐藻胶裂解酶的能力,利用响应面法优化其发酵产褐藻胶裂解酶的培养基。首先利用单因素法分别对发酵培养基中的不同碳源、碳源添加量、不同氮源、氮源添加量以及氯化钠添加量、磷酸二氢钾添加量、硫酸镁添加量和pH进行探究,研究各因素对产酶的影响。在单因素实验的基础上,通过Plackett-Burman试验确定Cobetia sp.20发酵培养基中影响产酶的主要因素。通过响应面试验建立回归方程。研究结果表明,Cobetia sp.20最优发酵培养基配方为褐藻胶15.00 g/L、硫酸铵7.50 g/L、氯化钠15.00 g/L、硫酸镁0.50 g/L、磷酸二氢钾5.30 g/L、硫酸亚铁0.01 g/L、pH值7.58。优化后酶活为142.79 U/mL,比优化前提高了26.36%。褐藻胶裂解酶活的提高,为褐藻胶裂解酶的工业化生产提供了参考。     

产双功能褐藻胶裂解酶菌株的筛选与初步研究

目的：双功能褐藻胶裂解酶既能降解聚β-D-甘露糖醛酸,又能降解聚α-L-古罗糖醛酸,可以用一种酶来制备不同结构的褐藻胶寡糖。本文的目的是筛选能产生双功能褐藻胶裂解酶的菌株,对其产酶曲线和降解产物作初步研究。方法：利用唯一碳源培养基筛选产生褐藻胶裂解酶的菌株,通过16SrDNA序列比对进行菌种鉴定,通过在凝胶上检测褐藻胶裂解酶活性来判断发酵上清液中褐藻胶裂解酶的数量及分子量,利用薄层层析确定降解褐藻胶的终产物组成。结果：从褐藻上筛选到一株海洋细菌QY107,鉴定为弧菌属细菌。发酵120h时褐藻胶裂解酶产量为12．32U／mL,其发酵液上清中只含有一种褐藻胶裂解酶,分子量在28kDa左右,并且对聚β—D-甘露糖醛酸和聚α-L-古罗糖醛酸都能降解,降解褐藻胶的终产物主要为三糖。结论：本文筛选到一株弧菌QY107,其发酵液上清中只有一种双功能褐藻胶裂解酶,可用于大量制备褐藻胶三糖。推测该酶具有特殊的催化腔结构,对其结构与功能相互关系的研究可能会发现新的底物结合与催化机制。酶解制备褐藻胶寡糖因其环保高效而越来越受到人们的重视,因此该菌株能促进海洋寡糖类生物制品的开发,在医药、食品、农业、生物燃料等领域具有广阔的应用前景。     

响应面法优化类芽胞杆菌HB172198产褐藻胶裂解酶发酵培养基

为了提高类芽胞杆菌新种HB172198产褐藻胶裂解酶活力,本研究采用响应面法对该菌株液体发酵培养基进行了优化实验。在单因素实验和Plackett-Burman试验筛选出海藻酸钠、胰蛋白胨、NaCl、MgSO4·7H2O等4个显著影响产酶因素的基础上,通过Box-Behnken设计及响应面法进行回归分析,得出产褐藻胶裂解酶最佳发酵培养基,其成分为:海藻酸钠7.50 g/L、胰蛋白胨13.57 g/L、NaCl 29.75 g/L、MgSO4·7H2O 0.08 g/L。优化条件下该菌株最大酶活性达14.60 U/mL,是优化前的1.87倍。本研究为菌株HB172198产褐藻胶裂解酶的大规模生产和工业应用提供了重要的理论依据。     

Production of pectinolytic enzymes pectinase and pectin lyase by <Emphasis Type="Italic">Bacillus subtilis</Emphasis> SAV-21 in solid state fermentation

Pectin-degrading enzymes (pectinase and pectin lyase) were produced in solid state fermentation by Bacillus subtilis SAV-21 isolated from fruit and vegetable market waste soil of Yamuna Nagar, Haryana, India, and identified by 16S rDNA sequencing. Under optimized conditions, maximum production of pectinase (3315 U/gds) and pectin lyase (10.5 U/gds) was recorded in the presence of a combination of orange peel and coconut fiber (4:1), with a moisture content of 60% at 35 °C and pH 4.0 after 4 days and 8 days of incubation, respectively. Pectinase yield was enhanced upon supplementation with galactose and yeast extract, whereas pectin lyase production was unaffected by adding carbon and nitrogen source to the basal medium. Thus, B. subtilis SAV-21 can be exploited for cost-effective production of pectinase and pectin lyase using agro-residues.     

Screening of Ganoderma strains with high polysaccharides and ganoderic acid contents and optimization of the fermentation medium by statistical methods

Polysaccharides and ganoderic acids (GAs) are the major bioactive constituents of Ganoderma species. However, the commercialization of their production was limited by low yield in the submerged culture of Ganoderma despite improvement made in recent years. In this work, twelve Ganoderma strains were screened to efficiently produce polysaccharides and GAs, and Ganoderma lucidum 5.26 (GL 5.26) that had been never reported in fermentation process was found to be most efficient among the tested stains. Then, the fermentation medium was optimized for GL 5.26 by statistical method. Firstly, glucose and yeast extract were found to be the optimum carbon source and nitrogen source according to the single-factor tests. Ferric sulfate was found to have significant effect on GL 5.26 biomass production according to the results of Plackett–Burman design. The concentrations of glucose, yeast extract and ferric sulfate were further optimized by response surface methodology. The optimum medium composition was 55 g/L of glucose, 14 g/L of yeast extract, 0.3 g/L of ferric acid, with other medium components unchanged. The optimized medium was testified in the 10-L bioreactor, and the production of biomass, IPS, total GAs and GA-T enhanced by 85, 27, 49 and 93 %, respectively, compared to the initial medium. The fermentation process was scaled up to 300-L bioreactor; it showed good IPS (3.6 g/L) and GAs (670 mg/L) production. The biomass was 23.9 g/L in 300-L bioreactor, which was the highest biomass production in pilot scale. According to this study, the strain GL 5.26 showed good fermentation property by optimizing the medium. It might be a candidate industrial strain by further process optimization and scale-up study.     

The Surface Display of the Alginate Lyase on the Cells of Yarrowia lipolytica for Hydrolysis of Alginate

The alginate lyase structural gene (AlyVI gene) was amplified from plasmid pET24-ALYVI carrying the alginate lyase gene from the marine bacterium Vibrio sp. QY101 which is a pathogen of Laminaria sp. When the gene was cloned into the multiple cloning site of the surface display vector pINA1317-YlCWP110 and expressed in cells of Yarrowia lipolytica, the cells displaying the alginate lyase could form clear zone on the plate containing sodium alginate, indicating that they had high alginate lyase activity. The cells displaying alginate lyase can be used to hydrolyze poly-β-d-mannuronate (M) and poly-α-l-guluronate (G) and sodium alginate to produce different lengths of oligosaccharides (more than pentasaccharides). This is the first report that the yeast cells displaying alginate lyase were used to produce different lengths of oligosaccharides from alginate.     

Nutrition and bioprocess development for efficient biosynthesis of an antitumor compound from marine-derived fungus

An integrated nutrition and bioprocess strategy was developed for improving the biosynthesis of an antitumor compound, 1403C, by a marine-derived fungus, Halorosellinia sp. (no. 1403). First, statistical design strategies were synthetically applied to optimize the nutritional composition. The resulting 1403C production reached 2.07 g/l, which was 143.5 % higher than the original production. However, it only produced 0.44 g/l of 1403C in 5-l bioreactor fermentation. Thus, the operating parameters including culture pH, dissolved oxygen, agitation speed, impeller type and inoculum level were considered to improve the fermentation process, and an effective control strategy for 1403C production by Halorosellinia sp. submerged in a 5-l bioreactor was established. When inoculating 0.22 g/l dry biomass, controlling dissolved oxygen not lower than 30 % during the growth phase but ranging between 30 and 40 % during the stationary phase, using a double-layer six-flat-blade Rushton disc turbine agitated at 400 rpm, keeping short-term low pH and rapid-rising pH with glucose starvation, the highest 1403C production was finally obtained at 1.32 g/l, which was promoted by 200 % compared to before optimization. Fermentation scale-up was finally performed in a 500-l bioreactor, and 1403C production of 1.09 g/l was obtained.     

Biochemical characterization and high-level production of oxidized polyvinyl alcohol hydrolase from Sphingopyxis sp. 113P3 expressed in methylotrophic Pichia pastoris

The Sphingopyxis sp. 113P3 gene oph, encoding oxidized polyvinyl alcohol hydrolase (OPH), was optimized with the preferred codons of Pichia pastoris and ligated into the pPIC9K vector behind the α-factor signal sequence. The vector was then transfected into P. pastoris GS115 and genomic integration was confirmed. Large-scale production of recombinant protein was performed by induction with 14.4 g/L methanol at 22 °C in a 3-L bioreactor. The maximal OPH activity obtained was 68.4 U/mL, which is the highest activity reported. The optimal pH and temperature of recombinant OPH were 8.0 and 45 °C, respectively. OPH activity was stable over a pH range of 5.0–8.5, and at a maximal temperature of 45 °C. The K _cat /K _m of recombinant OPH was 598 mM^?1 s^?1, which was 4.27-fold higher than that of recombinant OPH derived from Escherichia coli. The improved catalytic efficiency of OPH expressed in recombinant P. pastoris makes it favorable for industrial applications.     

Effective conversion of industrial starch waste to L-Lactic acid by Lactococcus lactis in a dialysis sac bioreactor

We describe here a simple technological process based on the direct fermentation of potato starch waste (PSW), an inexpensive agro-processing industrial waste, by a potential probiotic strain, Lactococcus lactis subsp. lactis, for enhancing L-lactic acid production. To maximize bioconversion and increase cell stability, we designed and tested a novel dialysis sac-based bioreactor. Shake flask fermentation (SFF) and fed batch fermentation in the dialysis sac bioreactor were compared for L-lactic acid production efficiency. The results showed that the starch (20 g/L) in the PSW-containing medium was completely consumed within 24 h in the dialysis sac bioreactor, compared with 48 h in the SFF. The maximum lactic acid concentration (18.9 g/L) and lactic acid productivity (0.79 g/L·h) obtained was 1.2- and 2.4-fold higher in the bioreactor than by SFF, respectively. Simultaneous saccharification and fermentation was effected at pH 5.5 and 30 °C. L. lactis cells were viable for up to four cycles in the fed batch fermentation compared to only one cycle in the SFF.     

Production of alginate by Azotobacter vinelandii grown at two bioreactor scales under oxygen-limited conditions

The oxygen transfer rate (OTR) was evaluated as a scale-up criterion for alginate production in 3- and 14-L stirred fermentors. Batch cultures were performed at different agitation rates (200, 300, and 600 rpm) and airflow rates (0.25, 0.5, and 1 vvm), resulting in different maximum OTR levels (OTR_max). Although the two reactors had a similar OTR_max (19 mmol L^?1 h^?1) and produced the same alginate concentration (3.8 g L^?1), during the cell growth period the maximum molecular weight of the alginate was 1,250 kDa in the 3-L stirred fermentor and 590 kDa in 14-L stirred fermentor. The results showed for the first time the evolution of the molecular weight of alginate and OTR profiles for two different scales of stirred fermentors. There was a different maximum specific oxygen uptake rate between the two fermenters, reaching 8.3 mmol g^?1 h^?1 in 3-L bioreactor and 10.6 mmol g^?1 h^?1 in 14-L bioreactor, which could explain the different molecular weights observed. These findings open the possibility of using $ q_{{{\text{O}}_{ 2} }} $ instead of OTR_max as a scaling criterion to produce polymers with similar molecular weights during fermentation.     

Detection of the key enzyme of alginate biosynthesis in <Emphasis Type="Italic">Vibrio</Emphasis> sp. QY102

Alginate is an important component of biofilms of many pathogens, but its presence in Vibrio has not been reported. The GDP-mannose dehydrogenase gene (algD), which is the kinetic control point in alginate biosynthesis, was cloned for the first time from Vibrio species using degenerated PCR and inverse PCR. Sequence analysis showed that algD was also localized in an alginate biosynthesis cluster, as it is in Pseudomonas aeruginosa. In addition, the existence of mannuronic acid, a component of alginate, was supported by the NMR spectrum of Vibrio sp. QY102 exopolysaccharide.     

Enhanced expression of the codon-optimized exo-inulinase gene from the yeast Meyerozyma guilliermondii in Saccharomyces sp. W0 and bioethanol production from inulin

In the present study, after the exo-inulinase gene INU1 from Meyerozyma guilliermondii was optimized according to the codon usage bias of Saccharomyces cerevisiae, both the optimized gene INU1Y and the native gene INU1 were ligated into the homologous integration expression vector pMIRSC11 and expressed in Saccharomyces sp. W0. It was determined that the inulinase activity of the recombinant yeast Y13 with the optimized gene INU1Y was 43.84 U/mL, which was obviously higher than that (31.39 U/mL) produced by the recombinant yeast EX3 with the native gene INU1. Moreover, it was indicated that the recombinant yeast Y13 could produce 126.30 mg/mL ethanol from 300.0 g/L inulin while the recombinant yeast EX3 and Saccharomyces sp. W0 produced 122.75 mg/mL and 114.15 mg/mL ethanol, respectively, under the same conditions. In addition, the ethanol productivity of the recombinant yeast Y13 was 2.25 mg/mL/h within 48 h of the fermentation, which was obviously higher than that of the recombinant yeast EX3 (1.97 mg/mL/h) and Saccharomyces sp. W0 (1.77 mg/mL/h) within the same period. The results demonstrated that the recombinant yeast Y13 had higher ethanol production and productivity than the recombinant yeast EX3 and Saccharomyces sp. W0. Therefore, it was concluded that the codon optimization of the exo-inulinase gene from M. guilliermondii effectively enhanced inulinase activity and improved ethanol production from inulin by Saccharomyces sp. W0 carrying the optimized inulinase gene.     

Medium Optimization for Improved Production of Dihydrolipohyl Dehydrogenase from <Emphasis Type="Italic">Bacillus sphaericus</Emphasis> PAD-91 in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Dihydrolipohyl dehydrogenase (DLD) is a FAD-dependent enzyme that catalyzes the reversible oxidation of dihydrolipoamide. Herein, we report medium optimization for the production of a recombinant DLD with NADH-dependent diaphorase activity from a strain of Bacillus sphaericus PAD-91. The DLD gene that consisted of 1413 bp was expressed in Escherichia coli BL21 (DE3), and its enzymatic properties were studied. The composition of production medium was optimized using one-variable-at-a-time method followed by response surface methodology (RSM). B. sphaericus DLD catalyzed the reduction of lipoamide by NAD⁺ and exhibited diaphorase activity. The molecular weight of enzyme was about 50 kDa and determined to be a monomeric protein. Recombinant diaphorase showed its optimal activity at temperature of 30 °C and pH 8.5. K _m and V _max values with NADH were estimated to be 0.025 mM and 275.8 U/mL, respectively. Recombinant enzyme was optimally produced in fermentation medium containing 10 g/L sucrose, 25 g/L yeast extract, 5 g/L NaCl and 0.25 g/L MgSO₄. At these concentrations, the actual diaphorase activity was calculated to be 345.0 ± 4.1 U/mL. By scaling up fermentation from flask to bioreactor, enzyme activity was increased to 486.3 ± 5.5 U/mL. Briefly, a DLD with diaphorase activity from a newly isolated B. sphaericus PAD-91 was characterized and the production of recombinant enzyme was optimized using RSM technique.     

Purification and Characterization of an Alginate Lyase from Marine Bacterium Vibrio sp. Mutant Strain 510-64

Marine Vibrio sp. 510 was chosen as a parent strain for screening high producers of alginate lyase using the complex mutagenesis of Ethyl Methanesulphonate and UV radiation treatments. The mutant strain Vibrio sp. 510-64 was selected and its alginate lyase activity was increased by 3.87-fold (reaching 46.12 EU/mg) over that of the parent strain. An extracellular alginate lyase was purified from Vibrio sp. 510-64 cultural supernatant by successive fractionation on DEAE Sepharose FF and two steps of Superdex 75. The purified enzyme yielded a single band on SDS-PAGE with the molecular weight of 34.6 kDa. Data of the N-terminal amino acid sequence indicated that this protein might be a novel alginate lyase. The substrate specificity results demonstrated that the alginate lyase had the specificity for poly G block.     

Bioprocess optimization for pectinase production using <Emphasis Type="Italic">Aspergillus niger</Emphasis> in a submerged cultivation system

Background

Pectinase enzymes present a high priced category of microbial enzymes with many potential applications in various food and oil industries and an estimated market share of $ 41.4 billion by 2020.

Results

The production medium was first optimized using a statistical optimization approach to increase pectinase production. A maximal enzyme concentration of 76.35 U/mL (a 2.8-fold increase compared with the initial medium) was produced in a medium composed of (g/L): pectin, 32.22; (NH₄)₂SO₄, 4.33; K₂HPO₄, 1.36; MgSO₄.5H₂O, 0.05; KCl, 0.05; and FeSO₄.5H₂O, 0.10. The cultivations were then carried out in a 16-L stirred tank bioreactor in both batch and fed-batch modes to improve enzyme production, which is an important step for bioprocess industrialization. Controlling the pH at 5.5 during cultivation yielded a pectinase production of 109.63 U/mL, which was about 10% higher than the uncontrolled pH culture. Furthermore, fed-batch cultivation using sucrose as a feeding substrate with a rate of 2 g/L/h increased the enzyme production up to 450 U/mL after 126 h.

Conclusions

Statistical medium optimization improved volumetric pectinase productivity by about 2.8 folds. Scaling-up the production process in 16-L semi-industrial stirred tank bioreactor under controlled pH further enhanced pectinase production by about 4-folds. Finally, bioreactor fed-batch cultivation using constant carbon source feeding increased maximal volumetric enzyme production by about 16.5-folds from the initial starting conditions.

     

Cloning and Sequencing of Alginate Lyase Genes from Deep-Sea Strains of Vibrio and Agarivorans and Characterization of a New Vibrio Enzyme

Four alginate lyase genes were cloned and sequenced from the genomic DNAs of deep-sea bacteria, namely members of Vibrio and Agarivorans. Three of them were from Vibrio sp. JAM-A9m, which encoded alginate lyases, A9mT, A9mC, and A9mL. A9mT was composed of 286 amino acids and 57% homologous to AlxM of Photobacterium sp. A9mC (221 amino acids) and A9mL (522 amino acids) had the highest degree of similarity to two individual alginate lyases of Vibrio splendidus with 74% and 84% identity, respectively. The other gene for alginate lyase, A1mU, was shotgun cloned from Agarivorans sp. JAM-A1m. A1mU (286 amino acids) showed the highest homology to AlyVOA of Vibrio sp. with 76% identity. All alginate lyases belong to polysaccharide lyase family 7, although, they do not show significant similarity to one another with 14% to 58% identity. Among the above lyases, the recombinant A9mT was purified to homogeneity and characterized. The molecular mass of A9mT was around 28 kDa. The enzyme was remarkably salt activated and showed the highest thermal stability in the presence of NaCl. A9mT favorably degraded mannuronate polymer in alginate. We discussed substrate specificities of family 7 alginate lyases based on their conserved amino acid sequences.     

Characterization of a new alginate lyase from newly isolated Flavobacterium sp. S20

Alginate lyase is a promising biocatalyst because of its application in saccharification of alginate for the production of biochemicals and renewable biofuels. This study described the isolation of a new alginate metabolizing bacterium, Flavobacterium sp. S20, from sludge samples and the characterization of its alginate lyase Alg2A. The alginate lyase gene, alg2A, was obtained by constructing and screening the genomic library of the strain S20 and overexpressed in Escherichia coli. Substrate specificity assays indicated Alg2A preferred poly-α-l-guluronate as a substrate over poly-β-d-mannuronate. In the saccharification process of a high content (10 %, w/v) of sodium alginate, the recombinant alginate lyase Alg2A yielded 152 of mM the reducing sugars after 69 h of reaction, and the amounts of oligosaccharides with a different degree of polymerization (DP) generated by Alg2A gradually accumulated without significant variation in the distribution of oligosaccharide compositions. These results indicated that Alg2A possessed high enzymatic capability for saccharifying the alginate, which could be used in saccharifying the alginate biomass prior to the main fermentation process for biofuels. In addition, Alg2A had a different endolytic reaction mode from both the two commercial alginate lyases and other alginate lyases from polysaccharide lyase family 7 owing to high yields of penta-, hex-, and hepta-saccharides in the hydrolysis products of Alg2A. Thus, Alg2A could be a good tool for the large-scale preparation of alginate oligosaccharides with high DP.     

从海洋中分离的弧菌QY102褐藻胶裂解酶的纯化和性质研究

从马尾藻(Sargassum)表面分离到一株产生高效胞外褐藻胶裂解酶的海洋弧菌（Vibrio sp.） QY102。以褐藻胶为唯一碳源发酵培养后,发酵液上清通过0.22μm滤膜过滤、DEAESepharose离子交换和Superdex75凝胶过滤得到电泳纯的褐藻胶裂解酶。酶的性质研究表明：其分子量约为28.5kD（SDSPAGE）,反应最适温度为40℃,最适pH为7.1,Ca2+、Mg2+对酶活有促进作用,而Ni2+、Al3+、Zn2+、Ba2+对酶活有抑制作用。该酶的活性明显高于已报道的褐藻胶裂解酶,pH稳定范围广（5～10）,并且对聚甘露糖醛酸的活性高于对聚古罗糖醛酸的活性。     

Purification and characterization of a Na+/K+ dependent alginate lyase from turban shell gut Vibrio sp. YKW-34

An alginate lyase with high specific enzyme activity was purified from Vibrio sp. YKW-34, which was newly isolated from turban shell gut. The alginate lyase was purified by in order of ion exchange, hydrophobic and gel filtration chromatographies to homogeneity with a recovery of 7% and a fold of 25. This alginate lyase was composed of a single polypeptide chain with molecular mass of 60 kDa and isoelectric point of 5.5–5.7. The optimal pH and temperature for alginate lyase activity were pH 7.0 and 40 °C, respectively. The alginate lyase was stable over pH 7.0–10.0 and at temperature below 50 °C. The alginate lyase had substrate specificity for both poly-guluronate and poly-mannuronate units. The k_cat/K_m value for alginate (heterotype) was 1.7 × 10⁶ s⁻¹ M⁻¹. The enzyme activity was completely lost by dialysis and restored by addition of Na⁺ or K⁺. The optimal activity exhibited in 0.1 M of Na⁺ or K⁺. This enzyme was resistant to denaturing reagents (SDS and urea), reducing reagents (β-mercaptoethanol and DTT) and chelating reagents (EGTA and EDTA).     

Efficient extracellular expression of <Emphasis Type="Italic">Bacillus deramificans</Emphasis> pullulanase in <Emphasis Type="Italic">Brevibacillus choshinensis</Emphasis>

In this study, the pullulanase gene from Bacillus deramificans was efficiently expressed in Brevibacillus choshinensis. The optimal medium for protein expression was determined through a combination of single-factor experiments and response surface methodology. The initial pH of the medium and the culture temperature were optimized. The pullulanase yield increased 10.8-fold through medium and condition optimization at the shake-flask level. From the results of these experiments, the dissolved oxygen level was optimized in a 3-L fermentor. Under these optimized conditions, the pullulanase activity and the specific pullulanase productivity reached 1005.8 U/mL and 110.5 × 10³ U/g dry cell weight, respectively, with negligible intracellular expression. The Brevibacillus choshinensis expression system has proven to be valuable for the extracellular production of pullulanase.