Effect of variation in growth conditions on the activity of dextranase inhibitor in continuous cultures of Streptococcus sobrinus

The activity of free extracellular dextranase inhibitor was determined in strains of Streptococcus sobrinus which were grown in a chemostat under a variety of defined conditions. Maximum release of dextranase inhibitor occurred at low growth rate in glucose-limited medium at pH 6.5. Free inhibitor could not be detected when the strains were grown at high growth rate or in batch culture.     

Production,characterization and (co-)immobilization of dextranase from <Emphasis Type="Italic">Penicillium aculeatum</Emphasis>

Fermentation kinetics of Penicillium aculeatum ATCC 10409 demonstrated that fungal growth and dextranase release are decoupled. Inoculation by conidia or mycelia resulted in identical kinetics. Two new isoenzymes of the dextranase were characterized regarding their kinetic constants, pI, MW, activation energy and stabilities. The larger enzyme was 3-fold more active (turnover number: 2,230 ± 97 s⁻¹). Pre-treatment of bentonite with H₂O₂ did not affect adsorption characteristics of dextranase. Enzyme to bentonite ratios above 0.5:1 (w/w) resulted in a high conservation of activity upon adsorption. Furthermore, dextranase could be used in co-immobilizates for the direct conversion of sucrose into isomalto-oligosaccharides (e.g. isomaltose). Yields of co-immobilizates were 2–20 times that of basic immobilizates, which consist of dextransucrase without dextranase.     

Dextranase production from Penicillium funiculosum

Twenty-eight Penicillium cultures were screened for dextranase activity. Dextranase yield of about 2000 DU/ml was obtained with Penicillium funiculosum SH-5. Maximum dextranase concentration was attained only when cell mass decreased. The kinetics of the dextranase production was correlated with the cell mass by a two-parameter model. The optimum pH and temperature for dextranase were 5.0-5.5 and 55°C, respectively. Crude dextranase preparation was inhibitory to insoluble glucan formation by streptococcus mutans 6715 in vitro.     

Expression, purification and characterization of a recombinant Lipomyces starkey dextranase in Pichia pastoris

The DEX gene encoding an extracellular dextranase from Lipomyces starkeyi was cloned into vector pPIC9k-His6 and was expressed in Pichia pastoris GS115 strain under the control of AOX1 promoter. After 107 h of the 5L-scaled fermentation, wet cells weight of the recombinant P. pastoris Mut(+) strain reached to 588.6g/L, and the concentration of dextranase and enzyme activity in the supernatant were 0.46 g/L and 83900 U/L, respectively. The activity of dextranase was improved 17.56-fold by cation-exchange chromatography only with a final yield of 71.61% and the specific activity of the purified enzyme was 181.96 U/mg. The purified dextranase, analyzed by SDS-PAGE and Western blotting, showed only one homogeneous band. Then the factors affecting the dextranase activity were evaluated. The optimal temperature and pH was 30 degrees C and pH 4.5, respectively. Metal ions Al(3+), Cu(2+), Fe(3+), and SDS could completely inhibit the enzyme activity, whereas Mg(2+) enhanced 145% of the enzyme activity. These characters are much different from what was previously reported for the L. starkeyi dextranase that was either expressed in S. cerevisiae or purified from natural L. starkeyi.     

Dextranase production by recombinant Pichia pastoris under operational volumetric mass transfer coefficient (kLa) and volumetric gassed power input (Pg/V) attainable at commercial large scale

Abstract

Most of the reported bioprocesses carried out by the methylotrophic yeast Pichia pastoris have been performed at laboratory scale using high power inputs and pure oxygen, such conditions are not feasible for industrial large-scale processes. In this study, volumetric mass transfer (k_La) and volumetric gassed power input (Pg/V) were evaluated within values attainable in large-scale production as scale-up criteria for recombinant dextranase production by Mut^S P. pastoris strain. Cultures were oxygen limited when the volumetric gassed power supply was limited to 2?kW m^?3. Specific growth rate, and then dextranase production, increased as k_La and Pg/V did. Meanwhile, specific production and methanol consumption rates were constant, due to the limited methanol condition also achieved at 2?L bioprocesses. The specific dextranase production rate was two times higher than the values previously reported for a Mut⁺ strain. After a scale-up process, at constant k_La, the specific growth rate was kept at 30?L bioprocess, whereas dextranase production decreased, due to the effect of methanol accumulation. Results obtained at 30?L bioprocesses suggest that even under oxygen-limited conditions, methanol saturated conditions are not adequate to express dextranase with the promoter alcohol oxidase. Bioprocesses developed within feasible and scalable operational conditions are of high interest for the commercial production of recombinant proteins from Pichia pastoris.     

Improving arachidonic acid fermentation by Mortierella alpina through multistage temperature and aeration rate control in bioreactor

Effective production of arachidonic acid (ARA) using Mortierella alpina was conducted in a 30-L airlift bioreactor. Varying the aeration rate and temperature significantly influenced cell morphology, cell growth, and ARA production, while the optimal aeration rate and temperature for cell growth and product formation were quite different. As a result, a two-stage aeration rate control strategy was constructed based on monitoring of cell morphology and ARA production under various aeration rate control levels (0.6–1.8 vvm). Using this strategy, ARA yield reached 4.7 g/L, an increase of 38.2% compared with the control (constant aeration rate control at 1.0 vvm). Dynamic temperature-control strategy was implemented based on the fermentation performance at various temperatures (13–28°C), with ARA level in total cellular lipid increased by 37.1% comparing to a constant-temperature control (25°C). On that basis, the combinatorial fermentation strategy of two-stage aeration rate control and dynamic temperature control was applied and ARA production achieved the highest level of 5.8 g/L.     

Engineering a novel secretion signal for cross-host recombinant protein expression

Protein secretion is conferred by a hydrophobic secretion signal usually located at the N-terminal of the polypeptide. We report here, the identification of a novel secretion signal (SS) that is capable of directing the secretion of recombinant proteins from both prokaryotes and eukaryotes. Secretion of fusion reporter proteins was demonstrated in Escherichia coli, Saccharomyces cerevisiae and six different eukaryotic cells. Estrogen-inducibility and secretion of fusion reporter protein was demonstrated in six common eukaryotic cell lines. The rate of protein secretion is rapid and its expression profile closely reflects its intracellular concentration of mRNA. In bacteria and yeast, protein secretion directed by SS is dependent on the growth culture condition and rate of induction. This secretion signal allows a flexible strategy for the production and secretion of recombinant proteins in numerous hosts, and to conveniently and rapidly study protein expression.     

Use of the weighted jackknife method to calculate the variance in cellular-specific protein secretion rate: application to monoclonal antibody secretion rate kinetics in response to osmotic stress

The specific secretion rate (q, mug protein secreted/viable cell-h) and its variance are very useful to compare the capability of cell lines for protein secretion. An assessment of specific secretion rate variability is also beneficial and important when the specific secretion rate is to be used as an on-line process parameter to monitor culture production behavior or for in-process decisionmaking. Experimental errors in mammalian cell culture (e.g., protein concentration measurement and cell counting) and estimation error in the method of calculating q contribute to the total variance of the specific secretion rate. Although the variance of q is essential for comparing the differences between cell lines and the response of the same cell line to different nutrient or environmental conditions, few methods for calculating the variance of the specific secretion rate have been reported. As a model system, we have used the weighted jackknife method and the delta method to calculate the variance in the specific secretion rate of a murine monoclonal antibody (q(mAb)) determined by a differential method. These methods were applied to calculate q(mAb) and its standard deviation to determine the change in q(mAb) kinetics during batch culture of the 9.2.27 hybridoma in response to growth in hyperosmotic media or osmotic stress. Without osmotic stress, during exponential growth in DMEM + 5% FBS spinner culture, the estimate of q(mAb) decreases at least threefold. Results indicate that the 9.2.27 hybridoma responds to hyperosmotic media (400 mOsm, 470 mOsm) by significantly reducing the degree of q(mAb) decrease in the exponential phase, thus maintaining a higher q(mAb) through the stationary phase. The trend of q(mAb) during the batch cultures studied is further confirmed by t-test. Osmotic stress is statistically shown to be able to alter significantly the hybridoma-specific mAb secretion kinetics during batch culture. Determination of the variance of specific secretion rate using the weighted jackknife method offers a powerful approach for establishing the confidence limits of specific protein secretion rate between cell cultures in different nutritional or osmotic environments. (c) 1996 John Wiley & Sons, Inc.     

Some properties of an endodextranase inhibitor from continuous cultures of Streptococcus sobrinus.

Cell-free filtrates of Streptococcus sobrinus, cultured at low growth rate in the chemostat, contain a dextranase inhibitor that can completely inhibit the activity of S. sobrinus endodextranase. The range of conditions under which inhibition occurs, and the situations in which enzyme activity can reappear, have been examined in continuous cultures of strain 6715-13WT and the dextranase-deficient mutant 6715-13-201. A purified preparation of the inhibitor was specific for S. sobrinus dextranase, having no action on dextranases from other oral streptococci. The percentage inhibition of S. sobrinus dextranase varied with the enzyme concentration, and the complete inhibition of low amounts of enzyme indicated a very tight bond between the inhibitor and the enzyme.     

3-羟基丙酸分批发酵过程中的pH控制策略研究

本文利用重组大肠杆菌以甘油为底物发酵合成3．羟基丙酸,考察了不同pH对3．羟基丙酸产量及菌体生长的影响,发现在pH6．5条件下,细胞比生长速率达到最大值,延迟期也相对较短;而pH7．0有利于3-羟基丙酸的合成,控制pH7．0可以使3-羟基丙酸产量达到7．39g／L。基于不同pH条件下对细胞比生长速率和3-羟基丙酸比生成速率的分析,提出3．羟基丙酸分批发酵过程中的pH控制策略,即在发酵过程前5h将pH控制在6．5,5h～15h控制pH为7．0,此时有利于细胞生长;而后在15h-25h控制pH为7．5,25h后控制pH为7．0,从而使细胞具有较高的3．羟基丙酸比合成速率。在此控制策略下经过34h发酵3-羟基丙酸的终产量达到8．76g／L,比pH7．0条件下的3-羟基丙酸产量提高了18．54％。     

Enhanced hyaluronic acid production by a two-stage culture strategy based on the modeling of batch and fed-batch cultivation of Streptococcus zooepidemicus

This study aimed to enhance hyaluronic acid (HA) production by a two-stage culture strategy based on the modeling of batch and fed-batch culture of Streptococcus zooepidemicus. Batch culture had higher specific HA synthesis rate while fed-batch culture had higher specific cell growth rate. The lower specific HA synthesis rate in fed-batch culture resulted from the competition of cell growth for the common precursors at a low substrate concentration. Based on the modeling of batch and fed-batch culture of S. zooepidemicus, a two-stage culture strategy was proposed to enhance HA production. S. zooepidemicus were cultured in a fed-batch mode with sucrose concentration maintained at 1.0+/-0.2g/L during 0-8h and then batch culture was performed during 8-20h with an initial sucrose concentration of 15g/L. With the proposed two-stage culture strategy, HA production was increased to 6.6g/L compared with 5.0g/L in batch culture with the same total sucrose. The enhanced HA production by the proposed two-stage culture strategy resulted from the decreased inhibition of cell growth and the increased transformation rate of sucrose to HA.     

Food-Grade Expression and Characterization of a Dextranase from Chaetomium gracile Suitable for Sugarcane Juice Clarification

The microbial production of dextranase using cheap carbon sources is beneficial to solve the economic loss caused by the accumulation of dextran in syrup. A food-grade microbial cell factory was constructed by introducing the dextranase encoding gene DEX from Chaetomium gracile to the chromosome of Bacillus subtilis, and the antibiotic resistance marker gene was subsequently deleted via the Cre/loxP strategy. The dual-promoter system with a sequentially arranged constitutive P43 promoter resulted in an 85 % increase in DEX expression. Under the optimal fermentation conditions of 10 g/L maltose, 15 g/L casein, 1 g/L Na₂HPO₄, 1 g/L FeSO₄ and 8 g/L NaCl, DEX activity was increased from 2.625 to 64.34 U/mL. Recombinant DEX was purified 5.98-fold with a recovery ratio of 26.67 % and specific activity of 3935.02 U/mg. Enzyme activity was optimal at 55 °C and pH 5.0 and remained 80.34 % and 71.36 % of the initial activity at 55 °C and pH 4.0 after 60 min, respectively. The enzyme possessed high activity in the presence of Co²⁺, while Ag⁺ showed the strongest inhibition ability. The optimal substrate was 20 g/L dextran T-2000. The findings could facilitate the low-cost, large-scale production of food-grade DEX for use in the sugar industry.     

Effects of passage number on growth and productivity of hybridoma secreting MRSA anti-PBP2a monoclonal antibodies

Monoclonal antibodies (mAb) are high added value glycoproteins recommended for immunotherapy, diagnosis, and also for the treatment of bacterial infections resistant to multiple drugs such as Methicillin Resistant Staphylococcus aureus (MRSA). In addition to environmental conditions related to cell cultures, the intrinsic characteristics of hybridoma cells, like the secretion stability of monoclonal antibodies by the cells through successive subcultures, are relevant for the characterization of cell lines related to the productivity of mAb. The rate of mAb production differs significantly between different cell lines and different passage numbers, and it is an important variable in characterization of cell lines. In order to find a more robust, faster-growing, and higher-productivity cell line of hybridoma, cultivations in 24-well plates were performed in different subculture periods, or cell passages (P), of hybridoma cells producing MRSA anti-PBP2a monoclonal antibodies [MRSA-antiPBP2a (mAb)]. The objective of this study was to study the effects of cell growth and production of MRSA-antiPBP2a mAb secreted by murine hybridoma cells grown in different passages as well as determine the which passages the hybridomas can be cultivated without harming their growth and productivity. So, cell growth profiles of hybridomas secreting MRSA-antiPBP2a (mAb) and the production of MRSA-antiPBP2a mAb in different subculture periods or cell passages (P) were studied. Cell growth tests, monoclonal antibody productivity, and metabolite characteristics revealed substantial differences in those cells kept between P10 and P50. Similarities in the secretion of monoclonal antibody, growth, and metabolic profiles, were noted in the MRSA-antiPBP2a mAb producing hybridoma cells kept between P10 and P20. Also, glucose consumption (g/L) and lactate production (g/L) in the latter cell cultures were monitored daily through biochemical analyzer. As of P30, it was observed a 4.4 times reduction in productivity, a 13 % reduction in metabolic yield, and a significant change in cell growth. Secretion of MRSA-antiPBP2a mAb should be obtained through the culture of hybridomas up to P20 in order to keep its stability.     

Purification and characterization of Streptococcus sobrinus dextranase produced in recombinant Escherichia coli and sequence analysis of the dextranase gene.

The plasmid (pYA902) with the dextranase (dex) gene of Streptococcus sobrinus UAB66 (serotype g) produces a C-terminal truncated dextranase enzyme (Dex) with a multicomplex mass form which ranges from 80 to 130 kDa. The Escherichia coli-produced enzyme was purified and characterized, and antibodies were raised in rabbits. Purified dextranase has a native-form molecular mass of 160 to 260 kDa and specific activity of 4,000 U/mg of protein. Potential immunological cross-reactivity between dextranase and the SpaA protein specified by various recombinant clones was studied by using various antisera and Western blot (immunoblot) analysis. No cross-reactivity was observed. Optimal pH (5.3) and temperature (39 degrees C) and the isoelectric points (3.56, 3.6, and 3.7) were determined and found to be similar to those for dextranase purified from S. sobrinus. The dex DNA restriction map was determined, and several subclones were obtained. The nucleotide sequence of the dex gene was determined by using subclones pYA993 and pYA3009 and UAB66 chromosomal DNA. The open reading frame for dex was 4,011 bp, ending with a stop codon TAA. A ribosome-binding site and putative promoter preceding the start codon were identified. The deduced amino acid sequence of Dex revealed the presence of a signal peptide of 30 amino acids. The cleavage site for the signal sequence was determined by N-terminal amino acid sequence analysis for Dex produced in E. coli chi 2831(pYA902). The C terminus consists of a serine- and threonine-rich region followed by the peptide LPKTGD, 3 charged amino acids, 19 amino acids with a strongly hydrophobic character, and a charged pentapeptide tail, which are proposed to correspond to the cell wall-spanning region, the LPXTGX consensus sequence, and the membrane-anchoring domains of surface-associated proteins of gram-positive cocci.     

Enhancement of Candida rugosa lipase production by using different control fed-batch operational strategies

Simulation studies have predicted that maximum lipase activity is reached with fed-batch operation strategies. In this work, two different fed-batch operational strategies have been studied: constant substrate feeding rate and specific growth rate control. A constant substrate feeding rate strategy showed that maximum aqueous lipolytic activity (55 U/mL) was reached at low substrate feeding rates, whereas lipase tends to accumulate inside the cell at higher rates of substrate addition. In the second fed-batch strategy studied, a feedback control strategy has been developed based on the estimation of state variables (X and mu) from the measurement of indirect variables such as CER by means of mass spectrometry techniques. An on-off controller was then used to maintain the specific growth rate at the desired value by adjusting the substrate feeding rate. A constant specific growth rate strategy gave higher final levels of aqueous lipolytic activity (117 U/mL) at low specific growth rates. At higher specific growth rates the enzyme remained accumulated inside the cell, as was observed with a constant feeding fed-batch strategy. With a constant specific growth rate strategy, lipase production by Candida rugosa was enhanced 10-fold compared to a batch operation. Purification studies have demonstrated that lipolytic and esterasic specific activity ratios of Candida rugosa isoenzymes can be modified by using different operational conditions. These studies have also showed that the isoenzymes obtained in a controlled growth rate strategy are around three- to four-fold more active than those obtained in a constant feeding rate strategy.     

Characterization of a yeast D-mannan with an alpha-D-glucosyl phosphate residue as an important immunochemical determinant

Conditions for the reaction of concanavalin A and dextranase with glutaraldehyde have been established to give a soluble, intermolecularly cross-linked conjugate possessing both dextranase and concanavalin activities. Evidence is presented that the dextranase and concanavalin molecules are linked to each other in the conjugate. The conjugate gives a different pattern of hydrolysis products on incubation with dextran than does dextranase.     

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%。     

表达血管生长抑制素的重组毕赤酵母在诱导阶段混合碳源的流加

为进行高密度发酵并实现外源基因的高表达,在表型为Mut^S的重组毕赤酵母（Pichia pastoris）表达人血管生长抑制素的诱导阶段,采用了甘油甲醇混合补料的培养方式。以溶氧水平作为甘油代谢指针来控制甘油限制性流加既可维持一定菌体生长,又不会发生发酵液中残余甘油及有害代谢产物（乙醇）阻遏蛋白表达。当表达阶段的菌体平均比生长速率控制于0.012h^-1,菌体浓度达150 g/L,血管生长抑制素浓度最高达到108 mg/L,血管生长抑制素的平均比生产速率为0.02 mg/(g·h),菌体关于甘油的表观得率为0.69 g/g,菌体关于甲醇的表观得率为0.93g/g,较没有采用甘油限制性流加时都有所提高。     

Stoichiometric interpretation of Escherichia coli glucose catabolism under various oxygenation rates.

Metabolic by-product secretion is commonly observed in oxygen-limited cultures. Oxygen limitations occur because of limits in the capacity of the respiratory system or because of the oxygenation limits of the cultivation method used. The latter restriction is of considerable practical importance since it results in a critical cell concentration above which oxygenation is insufficient, leading to by-product secretion. In this study we used a flux balance approach to determine optimal metabolic performance of Escherichia coli under variable oxygen limitations. This method uses linear optimization to find optimal metabolic flux patterns with respect to cell growth. Cell growth was defined as precursor requirements on the basis of a composition analysis. A growth-associated maintenance requirement of 23 mmol of ATP per g of biomass and a non-growth-associated maintenance value of 5.87 mmol at ATP per g (dry weight)-h were incorporated on the basis of a comparison with experimental data. From computations of optimal growth increased oxygen limitations were found to result in the secretion of acetate, formate, and ethanol in that order. Consistent with the experimental data in the literature, by-product secretion rates increased linearly with the growth rate. The computed optimal growth under increasing oxygen limitation revealed four critical growth rates at which changes in the by-product secretion pattern were observed. Concomitant with by-product secretion under oxygen limitations were changes in metabolic pathway utilization. The shifts in metabolism were characterized by changes in the metabolic values (computed as shadow prices) of the various redox carriers. The redox potential was thus identified as a likely trigger that leads to metabolic shifts.2+ ă     

Improvement of specific growth rate of <Emphasis Type="BoldItalic">Pichia pastoris</Emphasis> for effective porcine interferon-α production with an on-line model-based glycerol feeding strategy

Effective expression of porcine interferon-α (pIFN-α) with recombinant Pichia pastoris was conducted in a bench-scale fermentor. The influence of the glycerol feeding strategy on the specific growth rate and protein production was investigated. The traditional DO-stat feeding strategy led to very low cell growth rate resulting in low dry cell weight (DCW) of about 90 g/L during the subsequent induction phase. The previously reported Artificial Neural Network Pattern Recognition (ANNPR) model-based glycerol feeding strategy improved the cell density to 120 g DCW/L, while the specific growth rate decreased from 0.15 to 0.18 to 0.03–0.08 h⁻¹ during the last 10 h of the glycerol feeding stage leading to a variation of the porcine interferon-α production, as the glycerol feeding scheme had a significant effect on the induction phase. This problem was resolved by an improved ANNPR model-based feeding strategy to maintain the specific growth rate above 0.11 h⁻¹. With this feeding strategy, the pIFN-α concentration reached a level of 1.43 g/L, more than 1.5-fold higher than that obtained with the previously adopted feeding strategy. Our results showed that increasing the specific growth rate favored the target protein production and the glycerol feeding methods directly influenced the induction stage. Consequently, higher cell density and specific growth rate as well as effective porcine interferon-α production have been achieved by our novel glycerol feeding strategy.