High-cell-density production of poly-β-hydroxybutyrate (PHB) from methanol by Methylobacterium extorquens: production of high-molecular-mass PHB

Methylobacterium extorquens ATCC 55366 was successfully cultivated at very high cell densities in a fed-batch fermentation system using methanol as a sole carbon and energy source and a completely minimal culture medium for the production of poly--hydroxybutyrate (PHB). Cell biomass levels were between 100 g/l and 115 g/l (dry weight) and cells contained between 40% and 46% PHB on a dry-weight basis. PHB with higher molecular mass values than previously reported for methylotrophic bacteria was obtained under certain conditions. Shake-flask and fermentor experiments showed the importance of adjusting the mineral composition of the medium for improved biomass production and higher growth rates. High-cell-density cultures were obtained without the need for oxygen-enriched air; once the oxygen transfer capacity of the fermentor was reached, methanol was thereafter added in proportion to the amount of available dissolved oxygen, thus preventing oxygen limitation. Controlling the methanol concentration at a very low level (less than 0.01 g/l), during the PHB production phase, led not only to prevention of oxygen limitation but also to the production of very high-molecular-mass PHB, in the 900–1800 kDa range. Biomass yields relative to the total methanol consumed were in the range 0.29–0.33 g/g, whereas PHB yields were in the range 0.09–0.12 g/g. During the active period of PHB synthesis, PHB yields relative to the total methanol consumed were between 0.2 g/g and 0.22 g/g. M. extorquens ATCC 55366 appears to be a promising organism for industrial PHB production.     

Modeling of mini-proinsulin production in Pichia pastoris using the AOX promoter

An unstructured model based on mass balance equations for a recombinant methylotrophic yeast Pichia pastoris Mut^S (Methanol Utilization Slow) strain expressing the mini-proinsulin (MPI), was successfully established in quasi-steady state fed-batch fermentations with varying total quantity of biomass in a 7 l fermenter. The model describes the relationships between the total biomass and induction time, both in the batch and fed-batch phases. In addition, good correlations were obtained when the total quantity of MPI was correlated with the total biomass, demonstrating that the product of interest is associated with growth in the methanol phase. The parameters of the fermentation model obtained are similar to those reported by other researchers.     

High-level ethanol production from starch by a flocculent <Emphasis Type="Italic">Saccharomyces cerevisiae </Emphasis>strain displaying cell-surface glucoamylase

A Strain of host yeast YF207, which is a tryptophan auxotroph and shows strong flocculation ability, was obtained from SaccharomYces diastaticus ATCC60712 and S. cerevisiae W303-1B by tetrad analysis. The plasmid pGA11, which is a multicopy plasmid for cell-surface expression of the Rhyzopus oryzae glucoamylase/alpha-agglutinin fusion protein, was then introduced into this flocculent yeast strain (YF207/pGA11). Yeast YF207/pGA11 grew rapidly under aerobic condition (dissolved oxygen 2.0 ppm), using soluble starch. The harvested cells were used for batch fermentation of soluble starch to ethanol under anaerobic condition and showed high ethanol production rates (0.71 g h(-1) l(-1)) without a time lag, because glucoamylase was immobilized on the yeast cell surface. During repeated utilization of cells for fermentation, YF207/pGA11 maintained high ethanol production rates over 300 h. Moreover, in fed-batch fermentation with YF207/pGA11 for approximately 120 h, the ethanol concentration reached up to 50 g l(-1). In conclusion, flocculent yeast cells displaying cell-surface glucoamylase are considered to be very effective for the direct fermentation of soluble starch to ethanol.     

Production of pediocin SM-1 by Pediococcus pentosaceus Mees 1934 in fed-batch fermentation: Effects of sucrose concentration in a complex medium and process modeling

Production of pediocin SM-1 by Pediococcus pentosaceus Mees 1934 was investigated in semi-aerobic, pH-controlled, batch and fed-batch fermentations using a complex medium containing sucrose as the main source of carbon. The effects of sucrose concentration were studied in fed-batch fermentations in which a sucrose solution was added at stable feeding rates (5, 7, 9 and 10 g/l/h). The results showed that pediocin is produced as a product of the primary metabolism and its titer could be greatly improved by adjusting the sucrose feeding rate in fed-batch fermentation. The maximum titer of pediocin of 145 AU/ml was obtained in the fed-batch culture with 7 g/l/h feeding rate and that was 119% higher compared to the titer obtained in batch culture. Higher feeding rates (9 and 10 g/l/h) resulted in decreased pediocin yields while biomass levels appeared to be rather unaffected. The specific rate of pediocin formation was also sensitive to sucrose concentration levels. A mathematical model developed on the basis of well-known rate equations for batch and fed-batch cultures and growth associated production, described successfully cell growth, sucrose assimilation, lactate production and pediocin production in fed-batch culture.     

中性内切型纤维素酶在毕赤酵母中高水平表达的研究

中性内切型纤维素酶在纺织及造纸工业具有重要的应用,为了进一步提高从我国草菇中克隆的一种新的中性内切型纤维素酶(EG1)在Pichiapastoris中的表达水平,我们进行了提高基因拷贝数及高密度发酵等多种手段实现其高水平表达的研究。在前期研究的基础上,利用对已整合eg1的重组子再转化的方法,从含有2000μgLZeocin的YPDSZ平板上筛选到高抗Zeocin转化子,在摇瓶培养条件下,该转化子表达量比原来提高了3.8倍,在pH4～8条件下均有稳定表达,接种量(OD600=5.0)表达水平最好,提高甲醇的诱导浓度对表达有显著的促进作用。用3.2L发酵罐进行了高密度发酵,甲醇诱导95.5h后达到最高值,比摇瓶培养再提高了6.4倍,因此利用高抗Zeocin转化子及高密度发酵的手段,使EG1的表达水平提高了34倍,蛋白表达量达8.80mgmL,EG1酶活达到543.36IUmL,实现了中性内切纤维素酶的高水平表达,本研究将大大促进建立我国纺织用纤维素酶大规模高效生产技术。     

A feeding strategy for tetramethylpyrazine production by Bacillus subtilis based on the stimulating effect of ammonium phosphate

To examine the effects of ammonium salts on tetramethylpyrazine (TTMP) production by Bacillus subtilis CCTCC M 208157, different ammonium salts were tested, and diammonium phosphate (DAP) was found to have a predominant effect on stimulating TTMP synthesis. The DAP requirements for TTMP production were then investigated, experimental results showed that higher concentrations of DAP favored TTMP production, while both the ammonium and phosphate ions exhibited inhibitory effects on the cell growth and precursor 3-hydroxy-2-butanone accumulation. Based on the results above, a DAP feeding strategy was developed and verified in further experiments. By applying the proposed fed-batch strategy, the maximum TTMP concentrations reached 7.46 and 7.34 g/l in flask and fermenter experiments, increased by 55.1 and 29.0% compared to that of the batch TTMP fermentation, respectively. To our knowledge, these results, i.e., TTMP yields in flask or fermenter fermentations, were new records on TTMP fermentation by B. subtilis.     

Introducing a new bioengineered bug: Methylobacterium extorquens tuned as a microbial bioplastic factory

Discussion on and use of methanol as chemical feedstock and as alternative fuel has gained momentum during the past years. Consequently, microorganism and product design based on 'methylotrophism' is in vogue as reflected by increasing research and development activities in methanol-related areas. A recent example of microorganism and product development is the use of recombinant Methylobacterium extorquens ATCC 55366 strains in the production of second generation biopolyesters. Feeding n-alkenoic acids in addition to methanol yielded functionalized polyhydroxyalkanoates (PHAs) and uncovered how M. extorquens copes with fatty acids. While some parts of the degradation pathway remain unclear, possible metabolic routes are suggested that may explain the significant loss of double bonds prior to polymerization of PHA precursors and occurrence of odd-numbered monomers derived from even-numbered n-alkenoic acids. In addition, microbial discoloration upon fatty acid feeding is discussed and future directions for further genetic modification of M. extorquens are provided.     

Improvement in the bioreactor specific productivity by coupling continuous reactor with repeated fed-batch reactor for acetone-butanol-ethanol production

In comparison to the different fermentation modes for the production of acetone, butanol and ethanol (ABE) researched to date, the continuous fermentation is the most economically favored. Continuous fermentation with two or more reactor cascade is reported to be the most efficient as it results in a more stable solvent production process. In this work, it is shown that a continuous (first-stage) reactor coupled to a repeated fed-batch (second stage) is superior to batch and fed-batch fermentations, including two-stage continuous fermentation. This is due to the efficient catalyst use, reported through the specific product rate and rapid glucose consumption rate. High solvents are produced at 19.4 g(ABE) l?1, with volumetric productivities of 0.92 g(butanol) l?1 h?1 and 1.47 g(ABE) l ?1 h?1. The bioreactor specific productivities of 0.62 and 0.39 g g?1(cdw) h?1 obtained show a high catalyst activity. This new process mode has not been reported before in the development of ABE fermentation and it shows great potential and superiority to the existing fermentation methods.     

Multicopy integration and expression of heterologous genes in Methylobacterium extorquens ATCC 55366

High-level expression of chromosomally integrated genes in Methylobacterium extorquens ATCC 55366 was achieved under the control of the strong M. extorquens AM1 methanol dehydrogenase promoter (PmxaF) using the mini-Tn7 transposon system. Stable maintenance and expression of the integrated genes were obtained in the absence of antibiotic selective pressure. Furthermore, using this technology, a multicopy integration protocol for M. extorquens was also developed. Chromosomal integration of one to five copies of the gene encoding the green fluorescent protein (gfp) was achieved. The multicopy-based expression system permitted expression of a preset number of gene copies. A unique specific Tn7 integration locus in the chromosome of M. extorquens, known as the Tn7 attachment site (attTn7 site), was identified. This single attTn7 site was identified in an intergenic region between glmS, which encodes the essential enzyme glucosamine-6-phosphate synthetase, and dhaT, which encodes 1,3-propanediol dehydrogenase. The fact that the integration event is site specific and the fact that the attTn7 site is a noncoding region of the chromosome make the mini-Tn7 transposon system very useful for insertion of target genes and subsequent expression. In all transformants tested, expression and segregation of the transforming gene were stable without generation of secondary mutations in the host. In this paper, we describe single and multicopy chromosome integration and stable expression of heterologous genes (bgl [beta-galactosidase], est [esterase], and gfp [green fluorescent protein]) in M. extorquens.     

Production of poly(4-hydroxybutyric acid) by fed-batch cultures of recombinant strains of Escherichia coli

A recombinant strain of Escherichia coli was used to produce poly(4-hydroxybutyric acid), P(4HB), homopolyester by fed-batch culture in M9 mineral salts medium containing glucose and 4-hydroxybutyric acid as carbon sources. The final cell dry weight, P(4HB) concentration and P(4HB) content were 12.6 g/l, 4.4 g/l, and 36% of cell dry weight, respectively, in a 27-l stirred and aerated fermenter after 60 h of fed-batch fermentation at constant pH.     

Dissolved-oxygen-stat controlling two variables for methanol induction of rGuamerin in Pichia pastoris and its application to repeated fed-batch

A DO-stat control strategy for two variables was introduced to the rGuamerin production process in Pichia pastoris and applied to repeated fed-batch culture. Two interrelated variables, namely the ratio of partial pressure of pure O2 in the inlet air-stream and the methanol feed rate, were controlled simultaneously. By using this control strategy, methanol feeding for induction could be controlled automatically while efficiently controlling the dissolved oxygen level. As a result, the cell concentration reached more than 140 g l(-1) and rGuamerin expression level 450 iu l(-1). rGuamerin was secreted into the culture medium and reached a level that was 40% higher than achieved in a fed-batch process using manual control of the methanol feeding rate. Repeated rGuamerin induction was achieved by repeating the methanol feeding and withdrawing the culture broth during extended production. During more than 250 h of culture, expression of rGuamerin was maintained at an average of about 430 iu l(-1 )(473 mg l(-1)), without causing the cell density to decrease. In addition to the rGuamerin production process, the proposed control system might be applied to cultivation of other methylotrophic yeasts in the production of therapeutic proteins.     

Kinetics and modelling of kojic acid production by Aspergillus flavus Link in batch fermentation and resuspended mycelial system

An unstructured model based on logistic and Luedeking-Piret equations was proposed to describe growth, substrate consumption and kojic acid production by Aspergillus flavus Link strain 44-1 in batch fermentation and also in a resuspended cell system. The model showed that kojic acid production was non-growth associated. The maximum kojic acid and cell concentrations obtained in batch fermentations using the fermenter with optimized dissolved oxygen control (32.5 g/l and 11.8 g/l, respectively) and using a shake-flask (36.5 and 12.3 g/l, respectively) were not significantly different. However, the maximum specific growth rate and a non-growth-associated rate constant for kojic acid formation (n) for batch fermentation using the fermenter (0.085/h and 0.0125 g kojic acid/g cell.h, respectively) were approximately three and two times higher than the values obtained for fermentation using a shake-flask, respectively. Efficient conversion of glucose to kojic acid was achieved in a resuspended pellet or mycelial system, in a solution containing only glucose with citrate buffer at pH 3.5 and at a temperature of 30 °C. The resuspended cell material in the glucose solution was still active in synthesizing kojic acid after prolonged incubation (up to about 600 h). The rate constant of kojic acid production (n) in a resuspended cell system using 100 g glucose/l was almost constant at an average value of 0.011 g kojic acid/g cell.h up to a cell concentration of 19.2 g/l, above which it decreased. A drastic reduction of n was observed at a cell concentration of 26.1 g/l. However, the yield based on glucose consumed (0.45 g/g) was similar for all cell concentrations investigated.     

Optimization of fed-batch production of the model recombinant protein GFP in Lactococcus lactis

Optimization of recombinant protein production using lactic acid bacteria (LAB) remains an important obstacle on the road to realizing LAB as oral vaccine delivery vehicles. Despite this, there have been few published investigations to explore the higher limits of LAB recombinant protein expression in fed-batch fermentations. In this study, results from response surface experiments suggested an optimal set of conditions for expression of green fluorescent protein (GFP), a model recombinant protein, in bench-scale, fed-batch Lactococcus lactis IL1403 fermentations. The 48 4-L fed-batch fermentations in this set of experiments, along with preliminary studies, investigated the effects of pH, temperature, hemin concentration, concentration of the nisin inducer per cell, and time of induction. Cell densities in this data set ranged from 2.9 to 7.4 g/L and maximum GFP expression per cell ranged from 0.1 to 4.4 relative fluorescence units (RFU)/g. The optimal 4-L, fed-batch fermentation process found here yields growth and protein expression values that dramatically improve upon results from traditional test tube and flask processes. Relative to the traditional process, the experimental optimum conditions yield 4.9 times the cell density, 1.6 times the protein per cell mass, and 8 times the total protein concentration. Unexpectedly, experiments also revealed that the compound hemin, known previously to improve growth and survival of Lactococcus lactis (L. lactis), negatively impacted recombinant protein production when added in concentrations from 5 to 20 microg/mL with this strain. The improvement in protein expression over traditional processes demonstrated here is an important step toward commercial development of LAB for oral delivery of recombinant vaccines and therapeutic proteins.     

Scalable,two-stage,autoinduction of recombinant protein expression in E. coli utilizing phosphate depletion

We report the scalable production of recombinant proteins in Escherichia coli, reliant on tightly controlled autoinduction, triggered by phosphate depletion in the stationary phase. The method, reliant on engineered strains and plasmids, enables improved protein expression across scales. Expression levels using this approach have reached as high as 55% of the total cellular protein. The initial use of the method in instrumented fed-batch fermentations enables cell densities of ∼30 gCDW/L and protein titers up to 8.1 ± 0.7 g/L (∼270 mg/gCDW). The process has also been adapted to an optimized autoinduction media, enabling routine batch production at culture volumes of 20 μl (384-well plates), 100 μl (96-well plates), 20 ml, and 100 ml. In batch cultures, cell densities routinely reach ∼5–7 gCDW/L, offering protein titers above 2 g/L. The methodology has been validated with a set of diverse heterologous proteins and is of general use for the facile optimization of routine protein expression from high throughput screens to fed-batch fermentation.     

Bacterial cellulose production by fed-batch fermentation in molasses medium

Batch and fed-batch fermentations for bacterial cellulose (BC) production using molasses as a carbon source by Acetobacter xylinum BPR2001 were carried out in a jar fermentor. For improvement of BC production, molasses was subjected to H2SO4-heat treatment. The maximum BC concentration by this treated molasses increased 76%, and the specific growth rate increased 2-fold compared with that by untreated molasses. In batch fermentation, when the initial sugar concentrations of H2SO4-heat-treated molasses were varied from 20 to 70 g/L, the highest value of maximum BC concentration of 5.3 g/L was observed at 20 g/L. BC production in intermittent fed-batch (IFB) fermentation was conducted referring to the data in batch fermentation, and the highest BC production of 7.82 g/L was obtained when 0.2 L of molasses medium was added five times. When continuous fed-batch (CFB) fermentations were conducted, maximum BC concentration was obtained with a feeding rate of 6.3 g-sugar/h, which was derived from the optimal IFB experiment.     

Dissolved-oxygen-stat fed-batch fermentation of 1,3-dihydroxyacetone from glycerol by Gluconobacter oxydans ZJB09112

This study investigated the effects of DO concentration on DHA fermentation and of DO-stat fed-batch fermentation using a pH control strategy, on 1,3-dihydroxyacetone (DHA) production. The results showed that DO-stat fed-batch fermentation with pH-shift control was the optimal bioprocess for DHA production. DO-stat fed-batch fermentation was carried out at 30% air saturation, and the culture pH was automatically maintained at pH 6.0 during the first 20 h and then shifted to pH 5.0 until the end of the fermentation. An optimal DHA concentration of 175.9 ± 6.7 g/L, with a production yield to glycerol of 0.87 ± 0.04 g/g, was obtained at 72 h of DO-stat fed-batch fermentation at 30°C in a 15 L fermenter.     

Xylitol production by <Emphasis Type="Italic">Candida tropicalis</Emphasis> in a chemically defined medium

A chemically defined medium that included urea (5 g l(-1)) as a nitrogen source and various vitamins was substituted for a complex medium containing yeast extract (10 g l(-1)) in the production of xylitol by Candida tropicalis. In a fed-batch culture with the chemically defined medium, 237 g xylitol l(-1) was produced from 270 g xylose l(-1) after 120 h. The volumetric rate of xylitol production and the xylitol yield from xylose were 2 g l(-1) h(-1) and 89%, respectively. These values were about 5% lower and 4% higher, respectively, than those obtained using the complex medium. These results indicate that xylitol can be produced effectively in a chemically defined medium.     

Evaluation of plastic-composite supports in repeated fed-batch biofilm lactic acid fermentation by Lactobacillus casei

A customized stirred-tank biofilm reactor was designed for plastic-composite supports (PCS). In repeated-batch studies, the PCS-biofilm reactors outperformed the suspended-cell reactors by demonstrating higher lactic acid productivities (2.45 g l(-1) h(-1) vs 1.75 g l(-1) h(-1)) and greater glucose consumption rates (3.27 g l(-1) h(-1) vs 2.09 g l(-1) h(-1)). In the repeated fed-batch studies, reactors were spiked periodically with concentrated glucose (75%) to maintain a concentration of approximately 80 g of glucose l(-1) in the bioreactor. In suspended-cell fermentations with 10 g of yeast extract (YE) l(-1) and zero, one, two, and three glucose spikes, the lactic acid productivities were 2.64, 1.58, 0.80, and 0.62 g l(-1) h(-1), respectively. In comparison, biofilm reactors with 7 g of YE l(-1) and zero, one, two, and three glucose spikes achieved lactic acid productivities of 4.20, 2.78, 0.66, and 0.94 g l(-1) h(-1), respectively. The use of nystatin (30 U ml(-1)) subdued the contaminating yeast population with no effect on the lactic acid productivity of the biofilm reactors, but it did affect productivity in the suspended-cell bioreactor. Overall, in repeated fed-batch fermentations, the biofilm reactors consistently outperformed the suspended-cell bioreactors, required less YE, and produced up to 146 g of lactic acid l(-1) with 7 g of YE l(-1), whereas the suspended-cell reactor produced 132 g l(-1) with 10 g of YE l(-1).