Effect of galactose feeding on the improved production of hirudin in fed-batch cultures of recombinant Saccharomyces cerevisiae

Different feeding strategies of galactose were employed to improve the production of anticoagulant, hirudin, by fed-batch mode of cultivation from recombinant Saccharomyces cerevisiae. The structural gene coding for hirudin was harboured with GAL10 promoter for controlled expression of hirudin and the MFα 1 signal sequence for secretion into the growth medium. A step-wise feeding of galactose was found as more suitable feeding strategy of galactose which resulted in the final hirudin volumetric productivity of 6,840?μg/l?·?h, than intermittent, continuous and ethanol controlled feeding of galactose. The final volumetric productivity of hirudin obtained by step-wise feeding of galactose was 3.88 fold higher compared with simple batch fermentation.     

Improvement of extracellular recombinant glucose oxidase production in fed-batch culture of Saccharomyces cerevisiae: Effect of different feeding strategies

Out of four different feeding strategies tested for the production of extracellular recombinant glucose oxidase from Saccharomyces cerevisiae, constant feeding of galactose on the exhaustion of initial glucose, gave the highest yield-154 U/ml which was 62% above the yield achieved in batch operation (95 U/ml). © Rapid Science Ltd. 1998     

Enhancement of extracellular glucose oxidase production in pH-stat feed-back controlled fed-batch culture of recombinant Saccharomyces cerevisiae

Glucose oxidase (GOD) from Aspergillus niger was expressed in Saccharomyces cerevisiae under the regime of GAL-10 promoter and GAL-7 terminator of S. cerevisiae and -amylase signal sequence of Aspergillus oryzae. The enhancement of the expression level was achieved in pH-stat feed-back controlled fed-batch culture. The highest titre of extracellular GOD was 199 U/ml which marked two fold improvement over the batch (95 U/ml) and 28% above that of non-feed back controlled fed-batch (154 U/ml) operation. © Rapid Science Ltd. 1998     

Enhancement of glucose oxidase production in batch cultivation of recombinant Saccharomyces cerevisiae: optimization of oxygen transfer condition

AIMS: To obtain an optimal combination of agitation speed and aeration rate for maximization of specific glucose oxidase (GOD) production in recombinant Saccharomyces cerevisiae, and to establish a correlation between kLa vis-à-vis oxygen transfer condition and specific glucose oxidase production. METHODS AND RESULTS: The oxygen transfer condition was manifested indirectly by manipulating the impeller speed and aeration rate in accordance with a Central Composite Rotatory Design (CCRD). The dissolved oxygen concentration and the volumetric oxygen transfer coefficient (kLa) were determined at corresponding combinations of impeller speed and aeration rate. The maximal specific extracellular glucose oxidase production (3.17 U mg-1 dry cell mass) was achieved when the initial dissolved oxygen concentration was 6.83 mg l-1 at the impeller speed of 420 rev min-1 and at the rate of aeration of 0.25 vvm. It was found out that while impeller speed had a direct effect on the production of enzyme, a correlation between kLa and specific GOD production could not be established. CONCLUSION: At the agitation speed of 420 rev min-1 and at 0.25 vvm aeration rate, the degree of turbulence and the dissolved oxygen concentration were thought to be optimal both for cellular growth and production of enzyme. SIGNIFICANCE AND IMPACT OF THE STUDY: The combined effect of agitation and aeration on recombinant glucose oxidase production in batch cultivation has not yet been reported in the literature. Therefore, this study gives an insight into the effect of these two important physical parameters on recombinant protein production. It also suggests that since there is no correlation between kLa and specific production of GOD, kLa should not be used as one of the scale-up parameters.     

Fed-batch culture of recombinant Saccharomyces cerevisiae for glucose 6-phosphate dehydrogenase production

We examined glucose 6-phosphate dehydrogenase (G6PD) production by fed-batch cultivation, using a recombinant strain of Saccharomyces cerevisiae W303-181 overexpressing this enzyme. The cultivations were carried out in a 3 L fermenter at pH 5.7, 30 °C, 2.0 vvm aeration, 200 rpm agitation and an inoculum concentration of 1.0 g/L. The volume of the culture medium in the fed-batch process varied from 1.333 to 2.0 L, due to the addition of 15.0 g/L glucose solution during 5 h. Different feeding rates were studied (exponentially increasing and decreasing feeding rates), and the feeding profile was determined by values of the parameter K (time constant), namely: 0.2, 0.5 and 0.8 h⁻¹. The best enzyme production (847 U/L) was obtained with an exponentially increasing feeding rate and K = 0.2 h⁻¹. The results attained also showed that this process is promising for G6PD production.     

Exploiting the NADPH pool for xylitol production using recombinant Saccharomyces cerevisiae

Xylitol is a five-carbon sugar alcohol that has a variety of uses in the food and pharmaceutical industries. In xylose assimilating yeasts, NAD(P)H-dependent xylose reductase (XR) catalyzes the reduction of xylose to xylitol. In the present study, XR with varying cofactor specificities was overexpressed in Saccharomyces cerevisiae to screen for efficient xylitol production. Xylose consumption and xylitol yields were higher when NADPH-dependent enzymes (Candida tropicalis XR and S. cerevisiae Gre3p aldose reductase) were expressed, indicating that heterologous enzymes can utilize the intracellular NADPH pool more efficiently than the NADH pool, where they may face competition from native enzymes. This was confirmed by overexpression of a NADH-preferring C. tropicalis XR mutant, which led to decreased xylose consumption and lower xylitol yield. To increase intracellular NADPH availability for xylitol production, the promoter of the ZWF1 gene, coding for the first enzyme of the NADPH-generating pentose phosphate pathway, was replaced with the constitutive GPD promoter in a strain expressing C. tropicalis XR. This change led to a ~12% increase in xylitol yield. Deletion of XYL2 and SOR1, whose gene products can use xylitol as substrate, did not further increase xylitol yield. Using wheat stalk hydrolysate as source of xylose, the constructed strain efficiently produced xylitol, demonstrating practical relevance of this approach.     

Xylitol production by immobilized recombinant Saccharomyces cerevisiae in a continuous packed-bed bioreactor

Continuous xylitol production with two different immobilized recombinant Saccharomyces cerevisiae strains (H475 and S641), expressing low and high xylose reductase (XR) activities, was investigated in a lab-scale packed-bed bioreactor. The effect of hydraulic residence time (HRT; 1.3-11.3 h), substrate/cosubstrate ratio (0.5 and 1), recycling ratio (0, 5, and 10), and aeration (anaerobic and oxygen limited conditions) were studied. The cells were immobilized by gel entrapment using Ca-alginate as support and the beads were treated with Al(3+) to improve their mechanical strength. Xylose was converted to xylitol using glucose as cosubstrate for regeneration of NAD(P)H required in xylitol formation and for generation of maintenance energy. The stability of the recombinant strains after 15 days of continuous operation was evaluated by XR activity and plasmid retention analyses. Under anaerobic conditions the volumetric xylitol productivity increased with decreasing HRT with both strains. With a recycling ratio of 10, volumetric productivities as high as 3.44 and 5.80 g/L . h were obtained with the low XR strain at HRT 1.3 h and with the high XR strain at HRT 2.6 h, respectively. However, the highest overall xylitol yields on xylose and on cosubstrate were reached at higher HRTs. Lowering the xylose/cosubstrate ratio from 1 to 0.5 increased the overall yield of xylitol on xylose, but the productivity and the xylitol yield on cosubstrate decreased. Under oxygen limited conditions the effect of the recycling ratio on production parameters was masked by other factors, such as an accumulation of free cells in the bioreactor and severe genetic instability of the high XR strain. Under anaerobic conditions the instability was less severe, causing a decrease in XR activity from 0.15 to 0.10 and from 3.18 to 1.49 U/mg with the low and high XR strains, respectively. At the end of the fermentation, the fraction of plasmid bearing cells in the beads was close to 100% for the low XR strain; however, it was significantly lower for the high XR strain, particularly for cells from the interior of the beads. (c) 1996 John Wiley & Sons, Inc.     

Bioethanol production from Gracilaria verrucosa using Saccharomyces cerevisiae adapted to NaCl or galactose

This study examined the pretreatment, enzymatic saccharification, and fermentation of the red macroalgae Gracilaria verrucosa using adapted saccharomyces cerevisiae to galactose or NaCl for the increase of bioethanol yield. Pretreatment with thermal acid hydrolysis to obtain galactose was carried out with 11.7% (w/v) seaweed slurry and 373 mM H₂SO₄ at 121 °C for 59 min. Glucose was obtained from enzymatic hydrolysis. Enzymatic saccharification was performed with a mixture of 16 U/mL Celluclast 1.5L and Viscozyme L at 45 °C for 48 h. Ethanol fermentation in 11.7% (w/v) seaweed hydrolysate was carried out using Saccharomyces cerevisiae KCTC 1126 adapted or non-adapted to high concentrations of galactose or NaCl. When non-adapted S. cerevisiae KCTC 1126 was used, the ethanol productivity was 0.09 g/(Lh) with an ethanol yield of 0.25. Ethanol productivity of 0.16 and 0.19 g/(Lh) with ethanol yields of 0.43 and 0.48 was obtained using S. cerevisiae KCTC 1126 adapted to high concentrations of galactose and NaCl, respectively. Adaptation of S. cerevisiae KCTC 1126 to galactose or NaCl increased the ethanol yield via adaptive evolution of the yeast.

     

Modeling the growth and proteinase A production in continuous cultures of recombinant Saccharomyces cerevisiae

Overexpression of the homologous protein proteinase A (PrA) in Saccharomyces cerevisiae has been achieved by inserting the PrA gene (PEP4) with its own promoter on a 2mu multicopy plasmid. With this system the specific PrA production rate was found to be described well by a linear function of the oxidative glucose metabolism, the reductive glucose metabolism, and the oxidative ethanol metabolism, with a significant lower yield resulting from the reductive glucose metabolism compared with the oxidative glucose metabolism. To describe the experimental data, a simple mathematical model has been set up. The model is based on an assumption of a limited respiratory capacity as suggested by Sonnleitner and K?ppeli but extended to describe production of an extracellular protein. The model predicts correctly the critical dilution rate to be between 0.15 and 0.16 h(-1), the decrease in the biomass yield above the critical dilution rate, and the production of proteinase A at different dilution rates. Both the experimental data and model simulations suggest that the optimum operating conditions for protein production is just at the critical dilution rate. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 447-454, 1997.     

Production of recombinant hirudin in galactokinase-deficientSaccharomyces cerevisiae by fed-batch fermentation with continuous glucose feeding

The artificial gene coding for anticoagulant hirudin was placed under the control of theGAL10 promoter and expressed in the galactokinase-deficient strain (Δgal1) ofSaccharomyces cereivisiae, which uses galactose only as a gratuitous inducer in order to avoid its consumption. For efficient production of recombinant hirudin, a carbon source other than galactose should be provided in the medium to support growth of the Δgal1 strain. Here we demonstrate the successful use of glucose in the fed-batch fermentation of the Δgal1 strain to achieve efficient production of recombinant hirudin, with a yield of up to 400 mg hirudin/L.     

Cross-reactions between engineered xylose and galactose pathways in recombinant Saccharomyces cerevisiae

Background

Bioethanol can be produced from sugar-rich, starch-rich (first generation; 1G) or lignocellulosic (second generation; 2G) raw materials. Integration of 2G ethanol with 1G could facilitate the introduction of the 2G technology. The capital cost per ton of fuel produced would be diminished and better utilization of the biomass can be achieved. It would, furthermore, decrease the energy demand of 2G ethanol production and also provide both 1G and 2G plants with heat and electricity. In the current study, steam-pretreated wheat straw (SPWS) was mixed with presaccharified wheat meal (PWM) and converted to ethanol in simultaneous saccharification and fermentation (SSF).

Results

Both the ethanol concentration and the ethanol yield increased with increasing amounts of PWM in mixtures with SPWS. The maximum ethanol yield (99% of the theoretical yield, based on the available C6 sugars) was obtained with a mixture of SPWS containing 2.5% water-insoluble solids (WIS) and PWM containing 2.5% WIS, resulting in an ethanol concentration of 56.5 g/L. This yield was higher than those obtained with SSF of either SPWS (68%) or PWM alone (91%).

Conclusions

Mixing wheat straw with wheat meal would be beneficial for both 1G and 2G ethanol production. However, increasing the proportion of WIS as wheat straw and the possibility of consuming the xylose fraction with a pentose-fermenting yeast should be further investigated.     

Population dynamics of a continuous fermentation of recombinant Saccharomyces cerevisiae using flow cytometry

The plasmid instability of genetically modified microorganisms during prolonged bioreactor operations is one of the major problems to be overcome in the production of recombinant proteins. The use of flow cytometry to monitor a fermentation process with recombinant cells in a CSTR is reported here. This technique has been applied to determine the fraction of plasmid-bearing cells (P+) of a recombinant Saccharomyces cerevisiae strain harboring the EXG1 gene in a continuous stirred tank bioreactor with a working volume of 2 L. The different levels in the expression of the EXG1 gene, which encodes the enzyme exo-beta-glucanase, were used to determine the P+ fraction. Other parameters such as viability, cellular protein, cell size and structure were also monitored using flow cytometry. This technique has two main advantages over the conventional method of determining the P+ fraction (plating in selective and non-selective solid media): (a) it takes a very short period of time to obtain a measurement that provides multiple parametric information; and (b) it is more representative of the bioreactor cell population since it can analyze thousands of cells in the same sample. A continuous operation (432 h) with the recombinant strain in a CSTR was carried out to test the application of this technique. Measurements of cellular exo-beta-glucanase activity and cellular protein content closely correlates to the measured fraction of plasmid-containing cells in the population. Moreover, the standard deviation of the fraction of P+ cells determined using this technique was very low (about 2%). Recombinant protein production also increased the size of the yeast cells, whereas the recombinant cells also had a more complex internal structure than the non-recombinant host strain.     

Metabolic flux analysis of xylose metabolism in recombinant Saccharomyces cerevisiae using continuous culture

This study focused on elucidating metabolism of xylose in a Saccharomyces cerevisiae strain that overexpresses xylose reductase and xylitol dehydrogenase from Pichia stipitis, as well as the endogenous xylulokinase. The influence of xylose on overall metabolism was examined supplemented with low glucose levels with emphasis on two potential bottlenecks; cofactor requirements and xylose uptake. Results of metabolic flux analysis in continuous cultivations show changes in central metabolism due to the cofactor imbalance imposed by the two-step oxidoreductase reaction of xylose to xylulose. A comparison between cultivations on 27:3g/L xylose-glucose mixture and 10g/L glucose revealed that the NADPH-generating flux from glucose-6-phosphate to ribulose-5-phosphate was almost tenfold higher on xylose-glucose mixture and due to the loss of carbon in that pathway the total flux to pyruvate was only around 60% of that on glucose. As a consequence also the fluxes in the citric acid cycle were reduced to around 60%. As the glucose level was decreased to 0.1g/L the fluxes to pyruvate and in the citric acid cycle were further reduced to 30% and 20%, respectively. The results from in vitro and in vivo xylose uptake measurements showed that the specific xylose uptake rate was highest at the lowest glucose level, 0.1g/L.     

Effects of temperature and glycerol and methanol‐feeding profiles on the production of recombinant galactose oxidase in Pichia pastoris

Optimization of protein production from methanol‐induced Pichia pastoris cultures is necessary to ensure high productivity rates and high yields of recombinant proteins. We investigated the effects of temperature and different linear or exponential methanol‐feeding rates on the production of recombinant Fusarium graminearum galactose oxidase (EC 1.1.3.9) in a P. pastoris Mut⁺ strain, under regulation of the AOX1 promoter. We found that low exponential methanol feeding led to 1.5‐fold higher volumetric productivity compared to high exponential feeding rates. The duration of glycerol feeding did not affect the subsequent product yield, but longer glycerol feeding led to higher initial biomass concentration, which would reduce the oxygen demand and generate less heat during induction. A linear and a low exponential feeding profile led to productivities in the same range, but the latter was characterized by intense fluctuations in the titers of galactose oxidase and total protein. An exponential feeding profile that has been adapted to the apparent biomass concentration results in more stable cultures, but the concentration of recombinant protein is in the same range as when constant methanol feeding is employed. © 2014 The Authors Biotechnology Progress published by Wiley Periodicals, Inc. on behalf of American Institute of Chemical Engineers Biotechnol. Prog., 30:728–735, 2014     

不同宿主来源的重组酿酒酵母混合糖代谢比较

【目的】研究不同工业酿酒酵母宿主背景对重组酵母木糖利用效率的影响。【方法】将木糖利用途径的木糖还原酶(XR)、木糖醇脱氢酶(XDH)和木酮糖激酶(XK)编码基因串联后分别转入3株不同的工业酿酒酵母中,得到重组酵母ZQ1、ZQ5和ZQ7。分别对3个木糖途径代谢基因的表达水平、酶活和重组菌株的木糖发酵效率进行比较。【结果】重组菌株在木糖代谢基因转录、酶活性和木糖利用性能方面有很大差异,其中ZQ5木糖代谢能力最强,ZQ7其次,ZQ1木糖利用能力最弱。ZQ7在初始木糖浓度为20 g/L时木糖利用速率快于ZQ5,表明木糖浓度对重组菌发酵性能评价具有影响。【结论】不同菌株的遗传背景和木糖浓度对重组菌木糖利用的影响很大,评价重组酵母的木糖利用需考虑宿主的遗传背景和底物浓度的影响。     

酿酒酵母Saccharomyces cerevisiae重组菌株木糖醇发酵的初步研究

木糖还原酶催化木糖为木糖醇的反应,是木糖代谢的第一步。将木糖还原酶的原因ＸＹＬ１引入酿酒酵母中,构建得到儿表达ＸＹＬ１基因的重组酿酒酵母菌株ＨＹＥＸ２,该重组菌株的木糖还原酶比活力为７．４７Ｕ／ｍｇ。研究表明,该菌株获得转化木糖产生木糖醇的能力,当辅助碳源葡萄糖的浓度为２％,并在发酵３０ｈ左右添加木糖,木糖醇的转化率可达到０．９７ｇ／ｇ。     

A comparative summary of expression systems for the recombinant production of galactose oxidase

Background  

The microbes Escherichia coli and Pichia pastoris are convenient prokaryotic and eukaryotic hosts, respectively, for the recombinant production of proteins at laboratory scales. A comparative study was performed to evaluate a range of constructs and process parameters for the heterologous intra- and extracellular expression of genes encoding the industrially relevant enzyme galactose 6-oxidase (EC 1.1.3.9) from the fungus Fusarium graminearum. In particular, the wild-type galox gene from F. graminearum, an optimized variant for E. coli and a codon-optimized gene for P. pastoris were expressed without the native pro-sequence, but with a His-tag either at the N- or the C-terminus of the enzyme.     

High-level production of animal-free recombinant transferrin from Saccharomyces cerevisiae

Background

Microorganisms that are exposed to pollutants in the environment, such as metals/metalloids, have a remarkable ability to fight the metal stress by various mechanisms. These metal-microbe interactions have already found an important role in biotechnological applications. It is only recently that microorganisms have been explored as potential biofactories for synthesis of metal/metalloid nanoparticles. Biosynthesis of selenium (Se⁰) nanospheres in aerobic conditions by a bacterial strain isolated from the coalmine soil is reported in the present study.

Results

The strain CM100B, identified as Bacillus cereus by morphological, biochemical and 16S rRNA gene sequencing [GenBank:GU551935.1] was studied for its ability to generate selenium nanoparticles (SNs) by transformation of toxic selenite (SeO₃ ^2-) anions into red elemental selenium (Se⁰) under aerobic conditions. Also, the ability of the strain to tolerate high levels of toxic selenite ions was studied by challenging the microbe with different concentrations of sodium selenite (0.5 mM-10 mM). ESEM, AFM and SEM studies revealed the spherical Se⁰ nanospheres adhering to bacterial biomass as well as present as free particles. The TEM microscopy showed the accumulation of spherical nanostructures as intracellular and extracellular deposits. The deposits were identified as element selenium by EDX analysis. This is also indicated by the red coloration of the culture broth that starts within 2-3 h of exposure to selenite oxyions. Selenium nanoparticles (SNs) were further characterized by UV-Visible spectroscopy, TEM and zeta potential measurement. The size of nanospheres was in the range of 150-200 nm with high negative charge of -46.86 mV.

Conclusions

This bacterial isolate has the potential to be used as a bionanofactory for the synthesis of stable, nearly monodisperse Se⁰ nanoparticles as well as for detoxification of the toxic selenite anions in the environment. A hypothetical mechanism for the biogenesis of selenium nanoparticles (SNs) involving membrane associated reductase enzyme(s) that reduces selenite (SeO₃ ^2-) to Se⁰ through electron shuttle enzymatic metal reduction process has been proposed.     

补料方式对酵母菌生产谷胱甘肽的影响

比较了酵母菌发酵生产谷胱甘肽（GSH）的几种补料分批培养方式。实验发现补料可以明显地促进酵母菌的生长和谷胱甘肽的合成,同时还发现不同的补料方式对发酵液中的菌体浓度和GSH浓度有不同的影响。采用指数流加方式可获得极高的菌体浓度,但菌体中的GSH浓度较低;而采用恒－pH补料分批培养既可以达到较高菌体浓度,菌体中又含有较高的GSH含量,因此,其总的GSH产量最高,可达到977.8mg/L。