Effect of oxygen transfer and carbon source composition on the growth of Corynebacterium melassecola

Corynebacterium melassecola, a glutamate producing bacteria, has been cultivated in a 4-l batch aerated fermentor with glucose and fructose mixtures of various proportions as carbon sources and mineral ammonium as nitrogen source. Experimental results are analysed in order to obtain the specific rates and the conversion yields. A data reconciliation technique is used to manage with the experiments performed in similar conditions. The redundant experimental informations are used to test the carbon, nitrogen, available electrons, phosphorus and protons balances. The measurement of dissolved oxygen tension and volumetric oxygen transfer coefficient indicates that oxygen was never a limiting substrate in the experimental device though the oxygen demand was up to 70 mmoles/l.h and the heterogeneity of the liquid phase. The highest specific growth rate (0.59 h^?1) and the highest biomass production yield (0.48 gX/gS) are obtained with glucose as the sole carbon source. These two parameters progressively decrease with the increase of the proportion of fructose in the medium down to 0.43 h^?1 and 0.38 gX/gS on fructose so that the specific carbon uptake rate remains constant and equal to 0.04 C-mole/gX h. From a metabolic point of view, this decrease of the carbon conversion efficiency into cellular material is correlated to a lower carbon flux through the pentose pathway as the fructose proportion is increased. This is correlated with an accumulation of fructose 1,6-biphosphate which further activates the lactate deshydrogenase resulting to lactate production though the metabolism remains strictly aerobic.     

Amplified expression of fructose 1,6-bisphosphatase in Corynebacterium glutamicum increases in vivo flux through the pentose phosphate pathway and lysine production on different carbon sources

The overexpression of fructose 1,6-bisphosphatase (FBPase) in Corynebacterium glutamicum leads to significant improvement of lysine production on different sugars. Amplified expression of FBPase via the promoter of the gene encoding elongation factor TU (EFTU) increased the lysine yield in the feedback-deregulated lysine-producing strain C. glutamicum lysCfbr by 40% on glucose and 30% on fructose or sucrose. Additionally formation of the by-products glycerol and dihydroxyacetone was significantly reduced in the PEFTUfbp mutant. As revealed by 13C metabolic flux analysis on glucose the overexpression of FBPase causes a redirection of carbon flux from glycolysis toward the pentose phosphate pathway (PPP) and thus leads to increased NADPH supply. Normalized to an uptake flux of glucose of 100%, the relative flux into the PPP was 56% for C. glutamicum lysCfbr PEFTUfbp and 46% for C. glutamicum lysCfbr. The flux for NADPH supply was 180% in the PEFTUfbp strain and only 146% in the parent strain. Amplification of FBPase increases the production of lysine via an increased supply of NADPH. Comparative studies with another mutant containing the sod promoter upstream of the fbp gene indicate that the expression level of FBPase relates to the extent of the metabolic effects. The overexpression of FBPase seems useful for starch- and molasses-based industrial lysine production with C. glutamicum. The redirection of flux toward the PPP should also be interesting for the production of other NADPH-demanding compounds as well as for products directly stemming from the PPP.     

Metabolic flux analysis of Gluconacetobacter xylinus for bacterial cellulose production

Metabolic flux analysis was used to reveal the metabolic distributions in Gluconacetobacter xylinus (CGMCC no. 2955) cultured on different carbon sources. Compared with other sources, glucose, fructose, and glycerol could achieve much higher bacterial cellulose (BC) yields from G. xylinus (CGMCC no. 2955). The glycerol led to the highest BC production with a metabolic yield of 14.7 g/mol C, which was approximately 1.69-fold and 2.38-fold greater than that produced using fructose and glucose medium, respectively. The highest BC productivity from G. xylinus CGMCC 2955 was 5.97 g BC/L (dry weight) when using glycerol as the sole carbon source. Metabolic flux analysis for the central carbon metabolism revealed that about 47.96 % of glycerol was transformed into BC, while only 19.05 % of glucose and 24.78 % of fructose were transformed into BC. Instead, when glucose was used as the sole carbon source, 40.03 % of glucose was turned into the by-product gluconic acid. Compared with BC from glucose and fructose, BC from the glycerol medium showed the highest tensile strength at 83.5 MPa, with thinner fibers and lower porosity. As a main byproduct of biodiesel production, glycerol holds great potential to produce BC with superior mechanical and microstructural characteristics.     

Amplified Expression of Fructose 1,6-Bisphosphatase in Corynebacterium glutamicum Increases In Vivo Flux through the Pentose Phosphate Pathway and Lysine Production on Different Carbon Sources

The overexpression of fructose 1,6-bisphosphatase (FBPase) in Corynebacterium glutamicum leads to significant improvement of lysine production on different sugars. Amplified expression of FBPase via the promoter of the gene encoding elongation factor TU (EFTU) increased the lysine yield in the feedback-deregulated lysine-producing strain C. glutamicum lysC^fbr by 40% on glucose and 30% on fructose or sucrose. Additionally formation of the by-products glycerol and dihydroxyacetone was significantly reduced in the P_EFTUfbp mutant. As revealed by ¹³C metabolic flux analysis on glucose the overexpression of FBPase causes a redirection of carbon flux from glycolysis toward the pentose phosphate pathway (PPP) and thus leads to increased NADPH supply. Normalized to an uptake flux of glucose of 100%, the relative flux into the PPP was 56% for C. glutamicum lysC^fbr P_EFTUfbp and 46% for C. glutamicum lysC^fbr. The flux for NADPH supply was 180% in the P_EFTUfbp strain and only 146% in the parent strain. Amplification of FBPase increases the production of lysine via an increased supply of NADPH. Comparative studies with another mutant containing the sod promoter upstream of the fbp gene indicate that the expression level of FBPase relates to the extent of the metabolic effects. The overexpression of FBPase seems useful for starch- and molasses-based industrial lysine production with C. glutamicum. The redirection of flux toward the PPP should also be interesting for the production of other NADPH-demanding compounds as well as for products directly stemming from the PPP.     

Study of the production of fructose and ethanol from sucrose media by Saccharomyces cerevisiae

The production of ethanol and enriched fructose syrups from a synthetic medium with various sucrose concentrations using the mutant Saccharomyces cerevisiae ATCC 36858 was investigated. In batch tests, fructose yields were above 90% of theoretical values for the sucrose concentrations between 35 g/l and 257 g/l. The specific growth rates and biomass yields were from 0.218 to 0.128 h(-1) and from 0.160 to 0.075 g biomass/g of glucose and fructose consumed, respectively. Ethanol yields were in the range of 72 to 85% of theoretical value when sucrose concentrations were above 81 g/l. The volumetric ethanol productivity was 2.23 g ethanol/(l h) in a medium containing 216 g/l sucrose. Fructo-oligosaccharides and glycerol were also produced in the process. A maximum fructo-oligosaccharides concentration (up to 9 g/l) was attained in the 257 g/l sucrose medium in the first 7 h of the fermentation. These sugars started to be consumed when the concentrations of sucrose in the media were less than 30% of its initial values. The fructo-oligosaccharides mixture was composed of 6-kestose (61.5%), neokestose (29.7%) and 1-kestose (8.8%). The concentration of glycerol produced in the process was less than 9 g/l. These results will be useful in the production of enriched fructose syrups and ethanol using sucrose-based raw materials.     

Comparative metabolic flux analysis of lysine-producing Corynebacterium glutamicum cultured on glucose or fructose

A comprehensive approach to (13)C tracer studies, labeling measurements by gas chromatography-mass spectrometry, metabolite balancing, and isotopomer modeling, was applied for comparative metabolic network analysis of lysine-producing Corynebacterium glutamicum on glucose or fructose. Significantly reduced yields of lysine and biomass and enhanced formation of dihydroxyacetone, glycerol, and lactate in comparison to those for glucose resulted on fructose. Metabolic flux analysis revealed drastic differences in intracellular flux depending on the carbon source applied. On fructose, flux through the pentose phosphate pathway (PPP) was only 14.4% of the total substrate uptake flux and therefore markedly decreased compared to that for glucose (62.0%). This result is due mainly to (i) the predominance of phosphoenolpyruvate-dependent phosphotransferase systems for fructose uptake (PTS(Fructose)) (92.3%), resulting in a major entry of fructose via fructose 1,6-bisphosphate, and (ii) the inactivity of fructose 1,6-bisphosphatase (0.0%). The uptake of fructose during flux via PTS(Mannose) was only 7.7%. In glucose-grown cells, the flux through pyruvate dehydrogenase (70.9%) was much less than that in fructose-grown cells (95.2%). Accordingly, flux through the tricarboxylic acid cycle was decreased on glucose. Normalized to that for glucose uptake, the supply of NADPH during flux was only 112.4% on fructose compared to 176.9% on glucose, which might explain the substantially lower lysine yield of C. glutamicum on fructose. Balancing NADPH levels even revealed an apparent deficiency of NADPH on fructose, which is probably overcome by in vivo activity of malic enzyme. Based on these results, potential targets could be identified for optimization of lysine production by C. glutamicum on fructose, involving (i) modification of flux through the two PTS for fructose uptake, (ii) amplification of fructose 1,6-bisphosphatase to increase flux through the PPP, and (iii) knockout of a not-yet-annotated gene encoding dihydroxyacetone phosphatase or kinase activity to suppress overflow metabolism. Statistical evaluation revealed high precision of the estimates of flux, so the observed differences for metabolic flux are clearly substrate specific.     

Comparative Metabolic Flux Analysis of Lysine-Producing Corynebacterium glutamicum Cultured on Glucose or Fructose

A comprehensive approach to ¹³C tracer studies, labeling measurements by gas chromatography-mass spectrometry, metabolite balancing, and isotopomer modeling, was applied for comparative metabolic network analysis of lysine-producing Corynebacterium glutamicum on glucose or fructose. Significantly reduced yields of lysine and biomass and enhanced formation of dihydroxyacetone, glycerol, and lactate in comparison to those for glucose resulted on fructose. Metabolic flux analysis revealed drastic differences in intracellular flux depending on the carbon source applied. On fructose, flux through the pentose phosphate pathway (PPP) was only 14.4% of the total substrate uptake flux and therefore markedly decreased compared to that for glucose (62.0%). This result is due mainly to (i) the predominance of phosphoenolpyruvate-dependent phosphotransferase systems for fructose uptake (PTS_Fructose) (92.3%), resulting in a major entry of fructose via fructose 1,6-bisphosphate, and (ii) the inactivity of fructose 1,6-bisphosphatase (0.0%). The uptake of fructose during flux via PTS_Mannose was only 7.7%. In glucose-grown cells, the flux through pyruvate dehydrogenase (70.9%) was much less than that in fructose-grown cells (95.2%). Accordingly, flux through the tricarboxylic acid cycle was decreased on glucose. Normalized to that for glucose uptake, the supply of NADPH during flux was only 112.4% on fructose compared to 176.9% on glucose, which might explain the substantially lower lysine yield of C. glutamicum on fructose. Balancing NADPH levels even revealed an apparent deficiency of NADPH on fructose, which is probably overcome by in vivo activity of malic enzyme. Based on these results, potential targets could be identified for optimization of lysine production by C. glutamicum on fructose, involving (i) modification of flux through the two PTS for fructose uptake, (ii) amplification of fructose 1,6-bisphosphatase to increase flux through the PPP, and (iii) knockout of a not-yet-annotated gene encoding dihydroxyacetone phosphatase or kinase activity to suppress overflow metabolism. Statistical evaluation revealed high precision of the estimates of flux, so the observed differences for metabolic flux are clearly substrate specific.     

不同碳源对大肠杆菌lpdA突变菌累积丙酮酸的影响

为了利用大肠杆菌构建模式"细胞工厂",必须了解在构建过程中各种因素的影响。本研究选用敲除了lpdA基因的大肠杆菌作为模型细胞,考察了该突变菌在合成培养基中利用葡萄糖、果糖、木糖和甘露糖累积丙酮酸的能力。结果显示,在初始糖浓度为10g/L的情况下,lpdA突变菌可以很好地利用葡萄糖、果糖、木糖和甘露糖转化丙酮酸,其得率分别达到了0.884g/g、0.802g/g、0.817g/g和0.808g/g,且在以葡萄糖、果糖和木糖发酵时,丙酮酸的积累过程与细胞生长偶联。甘露糖发酵的情况则不同:菌浓度很快达到平台期,随后丙酮酸积累和甘露糖消耗都表现为线性变化。当在考察了不同的接种量对lpdA突变菌发酵葡萄糖的影响时发现,大接种量能加快葡萄糖消耗速率、丙酮酸的积累速率和细胞生长速率,但丙酮酸得率却明显下降。这些结果对构建以大肠杆菌为母体的模式"细胞工厂"有参考价值。     

Effect of different carbon sources on the production of succinic acid using metabolically engineered Escherichia coli

Succinic acid (SA) is an important platform molecule in the synthesis of a number of commodity and specialty chemicals. In the present work, dual-phase batch fermentations with the E. coli strain AFP184 were performed using a medium suited for large-scale industrial production of SA. The ability of the strain to ferment different sugars was investigated. The sugars studied were sucrose, glucose, fructose, xylose, and equal mixtures of glucose and fructose and glucose and xylose at a total initial sugar concentration of 100 g L-1. AFP184 was able to utilize all sugars and sugar combinations except sucrose for biomass generation and succinate production. For sucrose as a substrate no succinic acid was produced and none of the sucrose was metabolized. The succinic acid yield from glucose (0.83 g succinic acid per gram glucose consumed anaerobically) was higher than the yield from fructose (0.66 g g-1). When using xylose as a carbon source, a yield of 0.50 g g-1 was obtained. In the mixed-sugar fermentations no catabolite repression was detected. Mixtures of glucose and xylose resulted in higher yields (0.60 g g-1) than use of xylose alone. Fermenting glucose mixed with fructose gave a lower yield (0.58 g g-1) than fructose used as the sole carbon source. The reason is an increased pyruvate production. The pyruvate concentration decreased later in the fermentation. Final succinic acid concentrations were in the range of 25-40 g L-1. Acetic and pyruvic acid were the only other products detected and accumulated to concentrations of 2.7-6.7 and 0-2.7 g L-1. Production of succinic acid decreased when organic acid concentrations reached approximately 30 g L-1. This study demonstrates that E. coli strain AFP184 is able to produce succinic acid in a low cost medium from a variety of sugars with only small amounts of byproducts formed.     

Influence of glucose,fructose and sucrose as carbon sources on kinetics and stoichiometry of lysine production by <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Batch cultivations of l-lysine-producing Corynebacterium glutamicum ATCC 21253 were carried out on the different carbon sources, glucose, sucrose and fructose. The time profiles of substrate and product concentrations were evaluated to compare kinetics and stoichiometry of lysine production. The lysine yield (mol C/mol C) on glucose was 8% higher than on sucrose and 30% higher than on fructose. The highest final biomass concentration of 5.0 g/l was obtained on glucose, whereas fructose and sucrose yielded 20% less biomass. Compared to glucose, fructose resulted in significantly higher respiration rates, a higher substrate uptake rate but a lower lysine production rate during the cultivation process. This was probably due to a higher tricarboxylic cycle activity combined with a lower activity of the pentose phosphate pathway. On sucrose, specific rates and yields differed significantly from those on fructose and glucose. Transport and metabolism of sucrose, therefore, are not a simple superposition of its building blocks, glucose and fructose. Journal of Industrial Microbiology & Biotechnology (2002) 28, 338–343 DOI: 10.1038/sj/jim/7000252 Received 28 November 2001/ Accepted in revised form 06 March 2002     

Carbon and energy balances of glucose fermentation with hydrogenproducing bacterium Citrobacter amalonaticus Y19

For the newly isolated H2-producing chemoheterotrophic bacterium Citrobacter amalonaticus Y19, anaerobic glucose metabolism was studied in batch cultivation at varying initial glucose concentrations (3.5- 9.5 g/l). The carbon-mass and energy balances were determined and utilized to analyze the carbon metabolic-pathways network. The analyses revealed (a) variable production of major metabolites (H2, ethanol, acetate, lactate, CO2, and cell mass) depending on initial glucose levels; (b) influence of NADH regeneration on the production of acetate, lactate, and ethanol; and (c) influence of the molar production of ATP on the production of biomass. The results reported in this paper suggest how the carbon metabolic pathway(s) should be designed for optimal H2 production, especially at high glucose concentrations, such as by blocking the carbon flux via lactate dehydrogenase from the pyruvate node.     

Biotechnological valorization of low-cost sugar-based media for bacteriocin production by Leuconostoc mesenteroides E131

The aim of the present study was to evaluate the suitability of low-cost carbon sources for bacteriocin production by Leuconostoc mesenteroides strain E131. For this purpose, inexpensive sugars derived from a sugar refinery plant (glucose, fructose and sucrose) as well as waste molasses were utilized as carbon sources in submerged shake-flask experiments and the kinetic response of the microorganism was evaluated. Interestingly, in the case of molasses, non-negligible decolorization-detoxification (up to ～27%) of the residue was performed together with the production of bacteriocin. In all instances the initial concentration of sugars employed was adjusted at 20 and 30 g/L, therefore the effect of both the nature and the initial quantity of sugar upon the growth of the microorganism was assessed. All media proved to be suitable for both biomass and bacteriocin production by L. mesenteroides, whereas variable quantities of lactate, acetate and ethanol were detected into the medium. Employment of fructose, sucrose or molasses as carbon sources resulted in the accumulation of mannitol (in some cases in significant quantities) into the medium; remarkable portion thus of the available or released fructose acted as electron acceptor instead of carbon source by the microorganism. The highest bacteriocin production achieved (=640 AU/mL) was obtained when initial glucose at 30 g/L was used as substrate. Finally, utilization of waste molasses as carbon source by L. mesenteroides resulted in satisfactory bacteriocin production (up to 320 AU/mL) besides the decolorization of the residue.     

Heterotrophic production of biomass and lutein by Chlorella protothecoides on various nitrogen sources

The effects of nitrate, ammonium, and urea as nitrogen sources on the heterotrophic growth of Chlorella protothecoides were investigated using flask cultures. No appreciable inhibitory effect on the algal growth was observed over a nitrogen concentration range of 0.85-1.7 g l(-)(1). In contrast, differences in specific growth rate and biomass production were found among the cultures with the various nitrogen compounds. The influence of different nitrogen sources at a concentration equivalent to 1.7 g l(-)(1) nitrogen on the heterotrophic production of biomass and lutein by C. protothecoides was investigated using the culture medium containing 40 g l(-)(1) glucose as the sole carbon and energy source in fermentors. The maximum biomass concentrations in the three cultures with nitrate, ammonium, and urea were 18.4, 18.9, and 19.6 g l(-)(1) dry cells, respectively. The maximum lutein yields in these cultures were between 68.42 and 83.81 mg l(-)(1). The highest yields of both biomass and lutein were achieved in the culture with urea. It was therefore concluded that urea was the best nitrogen source for the production of biomass and lutein. Based on the experimental results, a group of kinetic models describing cell growth, lutein production, and glucose and nitrogen consumption were proposed and a satisfactory fit was found between the experimental results and predicted values. Dynamic analysis of models demonstrated that enhancing initial nitrogen concentration in fermentor cultures, which correspondingly enhances cell growth and lutein formation, may shorten the fermentation cycle by 25-46%.     

Metabolism and Energetics of Lactococcus lactis during Growth in Complex or Synthetic Media

When Lactococcus lactis was grown in various complex or synthetic media, the fermentation of glucose remained homolactic whatever the medium used, with a global carbon balance of about 87%. Moreover, the nitrogen balance was not equilibrated, indicating that some amino acids led to the production of unknown nitrogen-containing carbon compounds while part of the glucose might contribute to anabolic pathways. In minimal medium containing six amino acids, a high concentration of serine was deaminated to pyruvate. This did not occur in more complete media, suggesting the presence of a regulation of this phenomenon by an amino acid. Ammonia produced during serine consumption was partly reconsumed after serine exhaustion. The values for biomass yield and biomass yield relative to ATP (Y(infATP)), the maximal growth rate, the specific rate of glucose consumption, and the corresponding rate of ATP synthesis all increased with the complexity of the medium, amino acid composition having the most pronounced effect. The Y(infATP) values were shown to range from 6.6 to 17.6 g of biomass(middot)mol of ATP(sup-1) on minimal and complex media.     

Optimization of Escherichia coli cultivation methods for high yield neuropeptide Y receptor type 2 production

The recombinant expression of human G protein-coupled receptors usually yields low production levels using commonly available cultivation protocols. Here, we describe the development of a high yield production protocol for the human neuropeptide Y receptor type 2 (Y2R), which provides the determination of expression levels in a time, media composition, and process parameter dependent manner. Protein was produced by Escherichia coli in a defined medium composition suitable for isotopic labeling required for investigations by nuclear magnetic resonance spectroscopy. The Y2 receptor was fused to a C-terminal 8x histidine tag by means of the pET vector system for easy one-step purification via affinity chromatography, yielding a purity of 95-99% for every condition tested, which was determined by SDS-PAGE and Western blot analysis. The Y2 receptor was expressed as inclusion body aggregates in complex media and minimal media, using different carbon sources. We investigated the influences of media composition, temperature, pH, and set specific growth rate on cell behavior, biomass wet weight specific and culture volume specific amounts of the target protein, which had been identified by inclusion body preparation, solubilization, followed by purification and spectrometric determination of the protein concentration. The developed process control strategy led to very high reproducibility of cell growth and protein concentrations with a maximum yield of 800 μg purified Y2 receptor per gram wet biomass when glycerol was used as carbon source in the mineral salt medium composition (at 38 °C, pH 7.0, and a set specific growth rate of 0.14 g/(gh)). The maximum biomass specific amount of purified Y2 receptor enabled the production of 35 mg Y2R per liter culture medium at an optical density (600 nm) of 25.     

利用木糖-葡萄糖为原料产乙醇酵母的筛选、鉴定及发酵试验

建立筛选利用木糖为碳源产乙醇酵母模型,获得一株适合利用木质纤维素为原料产乙醇的酵母菌株。样品经麦芽汁培养基培养后,以木糖为唯一碳源的筛选培养基初筛,再以重铬酸钾显色法复筛。通过生理生化和26D1/D2区对筛选得到的菌株进行分析和鉴定,该菌初步鉴定为Pichia caribbica。经过筛选得到的菌株Y2-3以木糖（40g/L）为唯一碳源发酵时：生物量为23.5g/L,木糖利用率为94.7 %,乙醇终产量为4.57 g/L;以混合糖（葡萄糖40 g/L,木糖20 g/L）发酵时：生物量为28.6 g/L,木糖利用率为94.2 %,葡萄糖利用率为95.6%,乙醇终产量为20.6 g/L。Pichia caribbica是可以转化木糖及木糖-葡萄糖混合糖为乙醇的酵母菌株,为利用木质纤维素发酵乙醇的进一步研究奠定了基础。     

Heterotrophic high cell-density fed-batch cultures of the phycocyanin-producing red alga Galdieria sulphuraria

Growth and phycocyanin production in batch and fed-batch cultures of the microalga Galdieria sulphuraria 074G, which was grown heterotrophically in darkness on glucose, fructose, sucrose, and sugar beet molasses, was investigated. In batch cultures, specific growth rates and yields of biomass dry weight on the pure sugars were 1.08-1.15 day-1 and 0.48-0.50 g g-1, respectively. They were slightly higher when molasses was the carbon source. Cellular phycocyanin contents during the exponential growth phase were 3-4 mg g-1 in dry weight. G. sulphuraria was able to tolerate concentrations of glucose and fructose of up to 166 g L-1 (0.9 M) and an ammonium sulfate concentration of 22 g L-1 (0.17 M) without negative effects on the specific growth rate. When the total concentration of dissolved substances in the growth medium exceeded 1-2 M, growth was completely inhibited. In carbon-limited fed-batch cultures, biomass dry weight concentrations of 80-120 g L-1 were obtained while phycocyanin accumulated to concentrations between 250 and 400 mg L-1. These results demonstrate that G. sulphuraria is well suited for growth in heterotrophic cultures at very high cell densities, and that such cultures produce significant amounts of phycocyanin. Furthermore, the productivity of phycocyanin in the heterotrophic fed-batch cultures of G. sulphuraria was higher than is attained in outdoor cultures of Spirulina platensis, where phycocyanin is presently obtained.     

Optimization of the medium composition for production of mycelial biomass and exo-polymer by Grifola frondosa GF9801 using response surface methodology

In this work, a three-level Box-Behnken factorial design was employed combining with response surface methodology (RSM) to optimize the medium composition for the production of the mycelial biomass and exo-polymer in submerged cultures by Grifola frondosa GF9801. A mathematical model was then developed to show the effect of each medium composition and their interactions on the production of mycelial biomass and exo-polymer. The model estimated that, a maximal yield of mycelial biomass (17.61 g/l) could be obtained when the concentrations of glucose, KH2PO4, peptone were set at 45.2 g/l, 2.97 g/l, 6.58 g/l, respectively; while a maximal exo-polymer yield (1.326 g/l) could be achieved when setting concentrations of glucose, KH2PO4, peptone at 58.6 g/l, 4.06 g/l and 3.79 g/l, respectively. These predicted values were also verified by validation experiments. Compared with the values obtained by other runs in the experimental design, the optimized medium resulted in a significant increase in the yields of mycelial biomass and exo-polymer. Maximum mycelial biomass yield of 22.50 g/l was achieved in a 15-l fermenter using the optimized medium.     

In vitro production of gymnemic acid from cell suspension cultures of Gymnema sylvestre R. Br

Gymnema sylvestre is an important medicinal plant that bears bioactive compound namely gymnemic acids. The present work deals with the optimization of a cell suspension culture system of Gymnema sylvestre for the production of biomass and gymnemic acid, which has anti‐diabetic properties. We investigated the effect of inoculum densities (2.5–20.0 g/L), the strength of the Murashige and Skoog (MS) medium (0.25–2.0), carbon source (sucrose, glucose, fructose, maltose), and the concentration of the sucrose (1–8% w/v) to determine their effects on biomass accumulation and production of gymnemic acid. Overall, 10 g/L of inoculum density, full‐strength MS medium supplemented with 2,4‐dichlorophenoxy acetic acid (2.0 mg/L) and Kinetin (0.1 mg/L), and 3% w/v sucrose was found best for the accumulation of biomass and gymnemic acid content (9.95 mg/g dry weight). The results of the current study will be useful for bioprocess and biochemical engineers for large‐scale production of gymnemic acid in cell culture.     

Improving carbon and energy distribution by coupling growth and medium chain length polyhydroxyalkanoate production from fatty acids by <Emphasis Type="Italic">Pseudomonas putida</Emphasis> KT2440

The production of medium chain length polyhydroxyalkanoates by Pseudomonas putida KT2440 from fatty acids leads to the loss of a large proportion of carbon. We studied the possibility of a shift of potentially available energy and carbon towards monitored residual growth during the production phase. A Fed-Batch culture achieving 125.6 g/L of total biomass containing 54.4% (g/g) of medium chain length polyhydroxyalkanoates was carried out leading to an overall experimental carbon yield of 0.7 Cmole/Cmole. The analysis of modeling fluxes deduced from experimental data indicated how carbon and reduced cofactors (NADH and FADH₂) were managed to conclude that part of the carbon and reduced cofactors made available by polymer production were used in anabolic pathways. The strategy which consisted in coupled growth and medium chain length polyhydroxyalkanoate production enhanced the global yields compared to growth followed by a production phase. The understanding of carbon and energy fluxes distribution allowed deducing optimized culture strategy to perform the highest reported in the literature.