Enhanced 2,3-Butanediol Production by Optimizing Fermentation Conditions and Engineering Klebsiella oxytoca M1 through Overexpression of Acetoin Reductase

Microbial production of 2,3-butanediol (2,3-BDO) has been attracting increasing interest because of its high value and various industrial applications. In this study, high production of 2,3-BDO using a previously isolated bacterium Klebsiella oxytoca M1 was carried out by optimizing fermentation conditions and overexpressing acetoin reductase (AR). Supplying complex nitrogen sources and using NaOH as a neutralizing agent were found to enhance specific production and yield of 2,3-BDO. In fed-batch fermentations, 2,3-BDO production increased with the agitation speed (109.6 g/L at 300 rpm vs. 118.5 g/L at 400 rpm) along with significantly reduced formation of by-product, but the yield at 400 rpm was lower than that at 300 rpm (0.40 g/g vs. 0.34 g/g) due to acetoin accumulation at 400 rpm. Because AR catalyzing both acetoin reduction and 2,3-BDO oxidation in K. oxytoca M1 revealed more than 8-fold higher reduction activity than oxidation activity, the engineered K. oxytoca M1 overexpressing the budC encoding AR was used in fed-batch fermentation. Finally, acetoin accumulation was significantly reduced by 43% and enhancement of 2,3-BDO concentration (142.5 g/L), yield (0.42 g/g) and productivity (1.47 g/L/h) was achieved compared to performance with the parent strain. This is by far the highest titer of 2,3-BDO achieved by K. oxytoca strains. This notable result could be obtained by finding favorable fermentation conditions for 2,3-BDO production as well as by utilizing the distinct characteristic of AR in K. oxytoca M1 revealing the nature of reductase.     

Enhancement of pyruvate production by Torulopsis glabrata using a two-stage oxygen supply control strategy

The effect of agitation speeds on the performance of producing pyruvate by a multi-vitamin auxotrophic yeast, Torulopsis glabrata, was investigated in batch fermentation. High pyruvate yield on glucose (0.797 g g(-1)) was achieved under high agitation speed (700 rpm), but the glucose consumption rate was rather low (1.14 g l(-1) h(-1)). Glucose consumption was enhanced under low agitation speed (500 rpm), but the pyruvate yield on glucose decreased to 0.483 g g(-1). Glycerol production was observed under low agitation speed and decreased with increasing agitation speed. Based on process analysis and carbon flux distribution calculation, a two-stage oxygen supply control strategy was proposed, in which the agitation speed was controlled at 700 rpm in the first 16 h and then switched to 500 rpm. This was experimentally proven to be successful. Relatively high concentration of pyruvate (69.4 g l(-1)), high pyruvate yield on glucose (0.636 g g(-1)), and high glucose consumption rate (1.95 g l(-1)h(-1)) were achieved by applying this strategy. The productivity (1.24 g l(-1) h(-1)) was improved by 36%, 23% and 31%, respectively, compared with fermentations in which agitation speeds were kept constant at 700 rpm, 600 rpm, and 500 rpm. Experimental results indicate that the difference between the performances for producing pyruvate under a favorable state of oxygen supply (dissolved oxygen concentration >50%) was caused by the different regeneration pathways of NADH generated from glycolysis.     

In silico aided metabolic engineering of Klebsiella oxytoca and fermentation optimization for enhanced 2,3-butanediol production

Klebsiella oxytoca naturally produces a large amount of 2,3-butanediol (2,3-BD), a promising bulk chemical with wide industrial applications, along with various byproducts. In this study, the in silico gene knockout simulation of K. oxytoca was carried out for 2,3-BD overproduction by inhibiting the formation of byproducts. The knockouts of ldhA and pflB genes were targeted with the criteria of maximization of 2,3-BD production and minimization of byproducts formation. The constructed K. oxytoca ΔldhA ΔpflB strain showed higher 2,3-BD yields and higher final concentrations than those obtained from the wild-type and ΔldhA strains. However, the simultaneous deletion of both genes caused about a 50 % reduction in 2,3-BD productivity compared with K. oxytoca ΔldhA strain. Based on previous studies and in silico investigation that the agitation speed during 2,3-BD fermentation strongly affected cell growth and 2,3-BD synthesis, the effect of agitation speed on 2,3-BD production was investigated from 150 to 450 rpm in 5-L bioreactors containing 3-L culture media. The highest 2,3-BD productivity (2.7 g/L/h) was obtained at 450 rpm in batch fermentation. Considering the inhibition of acetoin for 2,3-BD production, fed-batch fermentations were performed using K. oxytoca ΔldhA ΔpflB strain to enhance 2,3-BD production. Altering the agitation speed from 450 to 350 rpm at nearly 10 g/L of acetoin during the fed-batch fermentation allowed for the production of 113 g/L 2,3-BD, with a yield of 0.45 g/g, and for the production of 2.1 g/L/h of 2,3-BD.     

枯草芽孢杆菌(Bacillus subtilis)发酵生产乙偶姻的pH调控策略

【目的】为了提高Bacillus subtilis CCTCC M 208157发酵生产乙偶姻的效率。【方法】在7 L发酵罐水平上考察不同pH条件对菌株生长及乙偶姻合成的影响。【结果】pH对菌株合成乙偶姻有显著影响,pH 4.5有利于细胞合成乙偶姻,但是延迟期较长;pH 5.5时菌株生长较快,但乙偶姻的产量偏低。因此提出了两阶段pH控制策略:发酵前期(0 16 h),控制pH 5.5;发酵中后期(16 72 h),控制pH 4.5。【结论】通过此策略,菌株合成乙偶姻的能力得到进一步提高,乙偶姻的产量、产率和生产强度分别为32.7 g/L、0.41 g/g和0.91 g/(L.h),分别比初始发酵条件下提高了41%、42%和69%。     

Enhancement of ribitol production during fermentation of <Emphasis Type="Italic">Trichosporonoides oedocephalis</Emphasis> ATCC 16958 by optimizing the medium and altering agitation strategies

To maximize the productivity of ribitol, which is an important starting material for the production of one expensive rare sugar, L-ribose, the effects of culture medium and agitation speed on cell growth as well as on the productivity of ribitol were thoroughly investigated in a 7 L fermentor. The maximum volumetric productivity, 0.322 g/L/h of ribitol, were obtained at an initial glucose concentration of 200 g/L in a batch culture. Based on the optimum glucose concentration, the ribitol yield conversed from glucose was up to 0.193 g/g when 1% yeast extract was used as a nitrogen source. When the agitation speed was maintained at 200 rpm, the ribitol concentration of 38.60 g/L was collected after 120 h of cultivation time. Additionally, the scheme of two-phase agitation and glucose infusion was employed. To begin, in the first 24 h of fermentation, a high agitation rate at 350 rpm and the initial glucose concentration of 50 g/L were applied, and the biomass concentration of 25.50 g/L was achieved at 36 h of incubation; whereas this value was observed until 60 h in the former batch fermentation methods. Then, in the second phase, with the agitation speed reduced to 150 rpm and the infusion amount of glucose controlled at 150 g/L, the yield of ribitol reached to 65.00 g/L in two-phase agitation fermentation and was 1.68 fold of that obtained in one-stage batch fermentation. To our knowledge, this study first demonstrates its significant effectiveness in improving ribitol production with the application of Trichosporonoides oedocephalis ATCC 16958.     

Comparative study on the influence of dissolved oxygen control approaches on the microbial hyaluronic acid production of <Emphasis Type="Italic">Streptococcus zooepidemicus</Emphasis>

Three different dissolved oxygen (DO) control approaches were proposed to improve hyaluronic acid (HA) production: a three-stage agitation speed control approach, a two-stage DO control approach, and an oxygen vector perfluorodecalin (PFC) applied approach. In the three-stage agitation speed control approach, agitation speed was 200 rpm during 0–8 h, 400 rpm during 8–12 h, and 600 rpm during 12–20 h. In the two-stage DO control strategy, DO was controlled at above 10% during 0–8 h and at 5% during 8–20 h. In the PFC applied approach, PFC (3% v/v) was added at 8 h. HA production reached 5.5 g/L in the three-stage agitation speed control culture model, and 6.3 g/L in two-stage DO control culture model, and 6.6 g/L in the PFC applied culture model. Compared with the other two DO control approaches, the PFC applied approach had a lower shear stress and thus a higher HA production was achieved.     

Improvement of poly(γ-glutamic acid) biosynthesis and quantitative metabolic flux analysis of a two-stage strategy for agitation speed control in the culture of <Emphasis Type="Italic">Bacillus subtilis</Emphasis> NX-2

In this study, the production of poly(γ-glutamic acid) by Bacillus subtilis NX-2 (PGA) at different agitation speeds was investigated. Based on the analysis of specific cell growth rate (μ) and specific PGA formation rate (q _p ), a two-stage strategy for agitation speed control was proposed. During the first 24 h, an agitation speed of 600 rpm was used to maintain a high μ for better cell growth, which then reduced to 400 rpm after 24 h to maintain a high q _p to enhance PGA production. Using this method, the maximum concentration of PGA reached 40.5 ± 0.91 g/L and the PGA productivity was 0.56 ± 0.012 g/L/h, which was 17.7 and 9.8% higher, respectively, than the best results obtained when a constant agitation speed was used. The flux distributions and the related enzymes of 2-oxoglutarate could be affected by this two-stage strategy for agitation speed. The activity of isocitrate dehydrogenase and glutamate dehydrogenase at the key node of 2-oxoglutarate increased, and more flux distribution was directed to glutamate. The flux distribution from extracellular to intracellular glutamate also increased and improved PGA production as the glutamate uptake rates increased using the agitation-shift control method.     

Increase of xylitol production rate by controlling redox potential in Candida parapsilosis

The effect of redox potential on xylitol production by Candida parapsilosis was investigated. The redox potential was found to be useful for monitoring the dissolved oxygen (DO) level in culture media, especially when the DO level was low. An increase in the agitation speed in a 5 L fermentor resulted in an increased culture redox potential as well as enhanced cell growth. Production of xylitol was maximized at a redox potential of 100 mV. As the initial cell concentration increased from 8 g/L to 30 g/L, the volumetric productivity of xylitol increased from 1.38 g/L. h to 4.62 g/L. h. A two-stage xylitol production strategy was devised, with stage 1 involving rapid production of cells under well-aerated conditions, and stage 2 involving cultivation with reduced aeration such that the culture redox potential was 100 mV. Using this technique, a final xylitol concentration of 180 g/L was obtained from a culture medium totally containing 254.5 g/L xylose in a 3,000 L pilot scale fermentor after 77 h fermentation. The volumetric productivity of xylitol during the fermentation was 2.34 g/L. h.     

Statistical optimization for production of carboxymethylcellulase of <Emphasis Type="Italic">Bacillus amyloliquefaciens</Emphasis> DL-3 by a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/DL-3 from rice bran using response surface method

The optimal conditions for production of carboxymethylcellulase (CMCase) of Bacillus amyloliquefaciens DL-3 by a recombinant Escherichia coli JM109/DL-3 were established at a flask scale using the response surface method (RSM). The optimal conditions of rice bran, tryptone, and initial pH of the medium for cell growth extracted by Design Expert Software were 66.1 g/L, 6.2 g/L, and 7.2, respectively, whereas those for production of CMCase were 58.0 g/L, 5.0 g/L, and 7.1. The analysis of variance (ANOVA) of results from central composite design (CCD) indicated that significant factor (“probe > F” less than 0.0500) for cell growth was rice bran, whereas those for production of CMCase were rice bran and initial pH of the medium. The optimal temperatures for cell growth and the production of CMCase by E. coli JM109/DL-3 were found to be 37°C. The optimal agitation speed and aeration rate of 7 L bioreactors for cell growth were 498 rpm and 1.4 vvm, whereas those for production of CMCase were 395 rpm and 1.1 vvm. The ANOVA of results indicated that the aeration rate was more significant factor (“probe > F” less than 0.0001) than the agitation speed for cell growth and production of CMCase. The optimal inner pressure for cell growth was 0.08 MPa, whereas that for the production of CMCase was 0.06 MPa. The maximal production of CMCase by E. coli JM109/DL-3 under optimized conditions was 871.0 U/mL, which was 3.0 times higher than the initial production of CMCase before optimization.     

Dependence of morphology on agitation intensity in fed-batch cultures of Aspergillus oryzae and its implications for recombinant protein production

We previously reported that, although agitation conditions strongly affected mycelial morphology, such changes did not lead to different levels of recombinant protein production in chemostat cultures of Aspergillus oryzae (Amanullah et al., 1999). To extend this finding to another set of operating conditions, fed-batch fermentations of A. oryzae were conducted at biomass concentrations up to 34 g dry cell weight/L and three agitation speeds (525, 675, and 825 rpm) to give specific power inputs between 1 and 5 kWm(-3). Gas blending was used to control the dissolved oxygen level at 50% of air saturation except at the lowest speed where it fell below 40% after 60-65 h. The effects of agitation intensity on growth, mycelial morphology, hyphal tip activity, and recombinant protein (amyloglucosidase) production in fed-batch cultures were investigated. In the batch phase of the fermentations, biomass concentration, and AMG secretion increased with increasing agitation intensity. If in a run, dissolved oxygen fell below approximately 40% because of inadequate oxygen transfer associated with enhanced viscosity, AMG production ceased. As with the chemostat cultures, even though mycelial morphology was significantly affected by changes in agitation intensity, enzyme titers (AGU/L) under conditions of substrate limited growth and controlled dissolved oxygen of >50% did not follow these changes. Although the measurement of active tips within mycelial clumps was not considered, a dependency of the specific AMG productivity (AGU/g biomass/h) on the percentage of extending tips was found, suggesting that protein secretion may be a bottle-neck in this strain during fed-batch fermentations.     

The improvement of cephalosporin C production by fed-batch culture ofCephalosporium acremonium M25 using rice oil

The objective of this study is to improve cephalosporin C (CPC) production by optimization of medium and culture conditions. A statistical method was introduced to optimize the main culture medium. The main medium for CPC production was optimized using a statistical method. Glucose and corn steep liquor (CSL) were found to be the most effective factors for CPC production. Glucose and CSL were optimized to 2.84 and 6.68%, respectively. CPC production was improved 50% by feeding of 5% rice oil at day 3rd and 5th day during the shake flask culture ofC. acremonium M25. The effect of agitation speeds on CPC production in a 2.5-L bioreactor was also investigated with fed-batch mode. The maximum cell mass (54.5 g/L) was obtained at 600 rpm. However, the maximum CPC production (0.98 g/L) was obtained at 500 rpm. At this condition, the maximum CPC production was improved about 132% compared to the result with batch flask culture.     

Production of chum salmon cystatin from the recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> optimized using response surface methodology

Chum salmon cystatin was overexpressed on Saccharomyces cerevisiae YPH 499. At first, the culture condition for the production of recombinant chum salmon cystatin (RC) by S. cerevisiae YPH 499 was optimized in a shake flask using response surface methodology. Three independent variables; medium pH, inducing time, and the amount of inducing assistant, were analyzed to get the optimal condition for the production of RC. The results were fitted to a second-order polynomial equation, in which the determination coefficient (R ²) was 0.904. The highest RC production in a shake flask, 0.57 U/mL was obtained at 5.7 of medium pH, 6.7 h of inducing time, and 5.6 g/L of inducing assistant. Based on the results of shake flask, the effects of agitation and aeration rates on the production of RC by S. cerevisiae YPH 499 were determined for scaleup in a fermentor. The highest production of RC in a fermentor, 0.56 U/mL was obtained at 350 rpm of agitation rate and 1.0 vvm of aeration rate. RC at 100 μg/g showed the highest inhibitory activity against the autolysis of Alaska pollock surimi based on the analysis of TCA-soluble peptides.     

多粘类芽胞杆菌利用生物柴油副产物粗甘油生产乙偶姻

研究多粘类芽胞杆菌利用廉价底物生物柴油副产物粗甘油批次发酵生产乙偶姻,考察不同pH条件、不同转速下乙偶姻、2,3-丁二醇和乙酸3种主要产物的产量,根据发酵结果设计一种三阶段溶氧调节的方法,结果表明:经76h批次发酵,乙偶姻产量为14.62 g/L,副产物2,3-丁二醇和乙酸分别为1.24和2.93 g/L;副产物量低,且易于分离,可以有效减少后期分离提取产物的成本。     

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.     

Enhanced Production of carboxymethylcellulase by a marine bacterium,Bacillus velezensis A-68, by using rice hulls in pilot-scale bioreactor under optimized conditions for dissolved oxygen

The optimal conditions for the production of carboxymethylcellulase (CMCase) by Bacillus velezensis A-68 at a flask scale have been previously reported. In this study, the parameters involved in dissolved oxygen in 7 and 100 L bioreactors were optimized for the pilot-scale production of CMCase. The optimal agitation speed and aeration rate for cell growth of B. velezensis A-68 were 323 rpm and 1.46 vvm in a 7 L bioreactor, whereas those for the production of CMCase were 380 rpm and 0.54 vvm, respectively. The analysis of variance (ANOVA) implied that the highly significant factor for cell growth was the aeration rate, whereas that for the production of CMCase was the agitation speed. The optimal inner pressures for cell growth and the production of CMCase by B. velezensis A-68 in a 100 L bioreactor were 0.00 and 0.04 MPa, respectively. The maximal production of CMCase in a 100 L bioreactor under optimized conditions using rice hulls was 108.1 U/ml, which was 1.8 times higher than that at a flask scale under previously optimized conditions.     

乙酸合成途径阻断及NADH氧化酶表达对于谷氨酸棒杆菌生产乙偶姻的影响

【目的】研究乙酸合成途径阻断及NADH氧化酶表达对于谷氨酸棒杆菌生产乙偶姻的影响。【方法】在谷氨酸棒杆菌CGF2中异源表达als SD操纵子构建乙偶姻生产菌株CGT1,考察敲除乙酸生成途径cat和pqo对乙偶姻的影响。然后引入短乳杆菌的NADH氧化酶,在优化的溶氧条件下研究其对乙偶姻产量的影响。【结果】CGT1在摇瓶发酵中可积累6.27 g/L乙偶姻,敲除cat使乙偶姻产量显著提高30.94%,达到8.21 g/L;双敲除cat和pqo没有进一步提高产量。通过优化发酵的溶氧水平,乙偶姻产量达到10.06 g/L。在高溶氧水平下引入NADH氧化酶导致菌株的生长和糖代谢速率提高,但乙偶姻产量略有降低。在分批补料发酵中,重组菌株乙偶姻产量达到40.51 g/L,产率为0.51 g/(L?h)。【结论】在谷氨酸棒杆菌中阻断乙酸合成途径cat能够有效提高乙偶姻产量,NADH氧化酶在高溶氧水平下表达不利于乙偶姻的合成,需要进一步调节表达水平以确定其效果。     

休哈塔假丝酵母HDYXHT-01利用木糖生产乙醇的发酵工艺优化

采用Plackett-Burman (PB) 方法和中心组合设计 (Ccentral composit design,CCD) 对休哈塔假丝酵母Candida shehataeHDYXHT-01利用木糖发酵生产乙醇的工艺进行优化。PB试验设计与分析结果表明：硫酸铵、磷酸二氢钾、酵母粉和接种量是影响木糖乙醇发酵的4个关键因素,以乙醇产量为响应目标,采用CCD和响应面分析法 (Response surface methodology,RSM),确定了木糖乙醇发酵的最佳工艺为：硫酸铵1.73 g/L、磷酸二氢钾3.56 g/L、酵母粉2.62 g/L和接种量5.66％,其他发酵条件为：木糖80 g/L,MgSO4·7H2O 0.1 g/L,pH 5.0,培养温度30 ℃,装液量100 mL/250 mL,摇床转速140 r/min,发酵时间48 h,在该条件下发酵液中乙醇产量可以达到26.18 g/L,比未优化前提高了1.15倍。     

Optimization of culture conditions and medium components for the production of mycelial biomass and exo-polysaccharides with Cordyceps militaris in liquid culture

Both crude exo-biopolymers and mycelial biomass, produced by liquid culture of Cordyceps species, are believed to possess several potential health benefits. As a result of its known biological activities, Cordyceps militaris has been extensively characterized in regards to potential medicinal applications. However, optimized liquid culture conditions for enhanced polysaccharide productivity have yet to be developed, which is a necessary step for industrial applications. Therefore, in this study, the liquid culture conditions were optimized for maximal production of mycelial biomass and exo-polysaccharide (EPS) by C. militaris. The effects of medium composition, environmental factors, and C/N ratio were investigated. Among these variables 80 g, glucose; 10 g, yeast extract; 0.5 g, MgSO₄·7H₂O; and 0.5 g, KH₂PO₄ in 1 L distilled water were found to be the most suitable carbon, nitrogen, and mineral sources, respectively. The optimal temperature, initial pH, agitation, and aeration were determined to be 24°C, uncontrolled pH, 200 rpm, and 1.5 vvm, respectively. Under these optimal conditions, mycelial growth in shake flask cultures and 5 L jar bioreactors was 29.43 and 40.60 g/L, respectively, and polysaccharide production in shake flask cultures and 5 L jar bioreactors was 2.53 and 6.74 g/L, respectively.     

发酵法生产L-异亮氨酸的溶氧控制策略

研究了溶氧对Brewibacterium lactofermentation分批发酵生产L-异亮氨酸（Ile）的影响,提出了前10h恒700d/min以维持溶氧在35％以上,10h后调至600r／min以维持溶氧在15％～20％的两阶段供氧控制模式。与对照相比,获得了较高的产率（0．094g／g）和糖耗速度（4．76/L·h）,在较短时间内（52h）获得较高的Ile产量（23．3g／L）,比结果最好的单一搅拌转速（600r/min）提高11．6％。生产强度（0．448d/L·h）比恒定搅拌转速（500、600、700、800r/min）控制下的过程分别提高了83．6％、28．7％、44．9％、35．7％。最后采用代谢通量分析对该结果产生的原因进行了定量解释。     

过氧化氢酶发酵生产条件优化及在染整清洁生产中的应用研究

在以嗜热子囊菌生产过氧化氢酶的摇瓶发酵研究中,获得了适合工业化生产的碳源,即以26g/L的糊化玉米淀粉和1%(v/v)乙醇为混合碳源,过氧化氢酶的酶活达到了1996 u/mL,比优化前提高了25%。在此基础上,重点研究了发酵罐上的主要影响因素溶解氧对发酵的影响,通过分段控制搅拌转速,在52h将搅拌转速从200r/min提高到350r/min,过氧化氢酶最高酶活达到4505 u/mL,与不使用控制溶氧水平策略相比,酶活力提高了2.4倍。此外,还考察了该酶去除过氧化氢的效率,并在实际纺织生产中进行了应用实验,取得了良好的效果。