Dynamics and modeling on fermentative production of poly (β-hydroxybutyric acid) from sugars via lactate by a mixed culture of Lactobacillus delbrueckii and Alcaligenes eutrophus

The mixed culture system was considered in the present research where sugars such as glucose were converted to lactate by Lactobacillus delbrueckii and the lactate was converted to poly β-hydroxybutyrate (PHB) by Alcaligenes eutrophus in one fermentor. For the modeling of the effect of NH₃ concentration on the cell growth of A. eutrophus and PHB production rates, metabolic flux distributions were computed at two culture phases of cell growth and PHB production periods. It was found that the NADPH, generated through isocitrate dehydrogenate in TCA cycle, was predominantly utilized for the reaction from α-ketoglutalate to glutamate when NH₃ was abundant, while it tended to be utilized for the PHB production through acetoacetyl CoA reductase as NH₃ concentration decreased. This phenomenon was reflected in the development of mathematical model. In the mixed culture experiments, the two phases were observed, namely the lactate production phase due to L. delbrueckii and the lactate consumption phase due to A. eutrophus. The lactate concentration could be estimated on-line by the amount of NaOH solution and HCl solution supplied to keep the culture pH at constant level. Several mixed culture experiments were conducted to see the dynamics of the system. Finally, a mathematical model which can describe the dynamic behavior of the present mixed culture was developed and the model parameters were tuned for fitting the experimental data. The model may be used for several purposes such as control, optimization, and understanding process dynamics etc.     

溶氧振荡对聚β羟基丁酸混合培养过程的调控作用

研究生物可降解塑料PHB(Poly β-hydroxy butyrate)生产的低成本和高产率发酵。采用廉价碳源——废食品糕点作为原料,其中同时具有葡萄糖和乳酸。培养是在同一5L发酵罐中先后接入2种细菌,先由乳酸杆菌Lactobacillus delbrueckii消耗葡萄糖产生乳酸,再由真养产碱菌Ralstonia eutrophus消耗乳酸产生PHB。本文应用混沌控制理论设计溶氧振荡来协调混生菌矛盾的生理需求,同时改变振荡节律激励细胞的代谢能。考虑真养产碱菌在乳酸里的代谢,有异养和真养两种途径,其中两种重要代谢通量,生物氧化能ATP和还原能NADPH,能够反映混生菌细胞的生理状态,二者都与供氧密切有关。实验通过取样进行细胞破碎后,由荧光分析仪监测不同发酵阶段的ATP和NADPH,发现2种代谢能随着溶氧控制的不同节律变化而起伏,溶氧节律振荡能够使混合培养的PHB的浓度比常规供氧方法提高1倍。     

Periodic change in DO concentration for efficient poly-β-hydroxy-butyrate production using temperature-inducible recombinant<Emphasis Type="Italic">Escherichia coli</Emphasis> with proteome analysis

RecombinantEscherichia coli strain harboring the λp _R-p _L promotor and heterologus poly-β-hydroxybutyrate (PHB) biosynthesis genes was used to investigate the effect of culture conditions on the efficient PHB production. The expression ofphb genes was induced by a temperature upshift from 33°C to 38°C. The protein expression levels were measured by using two-dimensional electrophoresis, and the enzyme activities were also measured to understand the effect of culture temperature, carbon sources, and the dissolved oxygen (DO) concentration on the metabolic regulations. AcetylCoA is an important branch point for PHB production. The decrease in DO concentration lowers the citrate synthase activity, thus limit the flux toward the TCA cycle, and increase the flux for PHB production. Since NADPH is required for PHB production, the PHB production does not continue leading the overproduction of acetate and lactate. Based on these observations, a new operation was considered where DO concentration was changed periodically, and it was verified its usefulness for the efficient PHB production by experiments.     

Enhancement of poly-3-hydroxybutyrate (PHB) productivity by the two-stage supplementation of carbon sources and continuous feeding of NH4Cl

Gluconate and glucose were selected as the carbon substrates in the production of poly-3-hydroxybutyrate (PHB). Gluconate was utilized to maximize the specific growth rate during the first stage of cell growth, whereas glucose was used to maximize PHB biosynthesis during the second stage of PHB accumulation. The sequential feeding of gluconate and glucose resulted in a 50% enhancement of PHB productivity as compared to the cultures cultivated on glucose alone. In conjunction with secondary glucose uptake, the presence of a trace amount of ammonium increased the rate of PHB biosynthesis during the stage of PHB accumulation. Via the feeding of 0.03 mmol/h of NH₄Cl solution prior to the exhaustion of the initial amount of NH₄Cl, PHB productivity was significantly enhanced as compared to the cultures raised on glucose alone. The glucose-grown culture evidenced a higher level of NADPH during the NH₄Cl-exausted PHB accumulation stage than was observed in the gluconate-grown culture, which reflects that the reason of higher PHB production observed when glucose was used as a carbon source. NH₄Cl feeding following the depletion of initial NH₄Cl resulted in elevated levels of both ATP and NADPH, which increased the PHB biosynthesis rate, and also in a decrease in the level of NADH, which reflected the alleviation of the inhibitory effects on the cells caused by nitrogen depletion. Electronic Supplementary Material  Supplementary material is available for this article at and is accessible for authorized users.     

Growth of Azotobacter vinelandii UWD in Fish Peptone Medium and Simplified Extraction of Poly-β-Hydroxybutyrate

Azotobacter vinelandii UWD was grown in a fermentor with glucose medium with and without 0.1% fish peptone (FP) in batch and fed-batch cultures for the production of the natural bioplastic poly-β-hydroxybutyrate (PHB). Strain UWD formed PHB five times faster than cell protein during growth in glucose and NH₄⁺, but PHB synthesis stopped when NH₄⁺ was depleted and nitrogen fixation started. When FP was added to the same medium, PHB accumulated 16 times faster than cell protein, which in turn was inhibited by 40%, and PHB synthesis was unaffected by NH₄⁺ depletion. Thus, FP appeared to be used as a nitrogen source by these nitrogen-fixing cells, which permitted enhanced PHB synthesis, but it was not a general growth stimulator. The addition of FP to the medium led to the production of large, pleomorphic, osmotically sensitive cells that demonstrated impaired growth and partial lysis, with the leakage of DNA into the culture fluid, but these cells were still able to synthesize PHB at elevated rates and efficiency. When FP was continuously present in fed-batch culture, the yield in grams of polymer per gram of glucose consumed was calculated to range from 0.43 g/g, characteristic of nongrowing cells, to an unprecedented 0.65 g/g. Separation of an FP-free growth phase from an FP-containing growth phase in fed-batch culture resulted in better growth of these pleomorphic cells and good production of PHB (yield, 0.32 g/g). The fragility of these cells was exploited in a simple procedure for the extraction of high-molecular-weight PHB. The cells were treated with 1 N aqueous NH₃ (pH 11.4) at 45°C for 10 min. This treatment removed about 10% of the non-PHB mass from the pellet, of which 60 to 77% was protein. The final product consisted of 94% PHB, 2% protein, and 4% nonprotein residual mass. The polymer molecular weight (1.7 × 10⁶ to 2.0 × 10⁶) and dispersity (1.0 to 1.9) were not significantly affected (P = 0.05) by this treatment. In addition, the NH₃ extraction waste could be recycled in the fermentation as a nitrogen source, but it did not promote PHB production like FP. A scheme for improved downstream extraction of PHB as well as the merits of using pleomorphic cells in the production of bioplastics is discussed.     

Commensalistic Interaction Between Lactobacillus acidophilus and Propionibacterium shermanii

Propionibacterium shermanii and Lactobacillus acidophilus were grown in batch mixed culture in a 5-liter fermenter under controlled conditions of pH 5.8 and 35°C on a semisynthetic medium with glucose as an energy source. Cellular efficiencies and fermentation balances were developed for this pair and compared with P. shermanii grown in pure culture on glucose, lactate, and a mixture of these substrates and with L. acidophilus grown on glucose. P. shermanii had ATP yield coefficient values of 17 for each substrate alone but had an average value of 30 for substrate mixtures. Growth rates were similar for P. shermanii on glucose or lactate but higher cell yields were observed for glucose. P. shermanii used both lactate and glucose in mixed substrate until lactate was exhausted, and growth rates slowed thereafter. L. acidophilus had a similar ATP yield coefficient of 15 but produced lower cell yields than did P. shermanii on glucose. Mixed culture of both microorganisms on glucose resulted in much faster and nearly equal growth rates for both and no lactate accumulation in the medium. Acetic acid production rates per generation were lower in mixed culture, suggesting use by the growing culture. The cause of the synergistic effect was not determined but may be due to the rapid production and removal of lactate or CO₂ enhancement in mixed culture.     

Mass production of poly-β-hydroxybutyric acid by fully automatic fed-batch culture of methylotroph

Summary Fifty-one methylotrophs were checked with respect to their ability of poly--hydroxybutyric acid (PHB) production from methanol. One of them, Pseudomonas sp. K, was chosen from its good growth on a minimum synthetic medium. Optimal temperature and pH for its growth were 30° C and 7.0, respectively. Concentrations of PO ₄ ^3- and NH ₄ ⁺ in the medium should be kept at low levels. PHB formation was stimulated by deficiency of nutrient such as NH ₄ ⁺ , SO ₄ ^2- , Mg²⁺, Fe²⁺ or Mn²⁺. Among them, nitrogen deficiency was chosen from its effectiveness and easiness for PHB accumulation.The microorganism was cultivated to produce a large amount of poly--hydroxybutyric acid (PHB) from methanol by means of microcomputer-aided fully automatic fed-batch culture technique. During the cultivation, temperature, dissolved oxygen concentration (DO), and methanol concentration in the culture broth were maintained at 30° C 2.5±0.5 ppm and 0.5±0.2 g/l, respectively. Other nutrients, nitrogen source and mineral ions, were also controlled to maintain their initial concentrations in the medium during cell growth phase. When the high cell concentration was achieved (160 g/l), feedings of ammonia and minerals were stopped and only methanol was supplied successively to accumulate PHB. At 175 h, high concentration of PHB (136 g/l) was obtained and total cell concentration became 206 g/l. DO must be maintained above the critical level during the PHB formation phase, too. PHB yield from methanol (g PHB/g methanol) was 0.18 and the maximum PHB content reached 66% of dry weight. Solid PHB produced by the strain had the melting point of 176° C and the average molecular weight of 3.0x10⁵.     

Competitive Exclusion of Salmonella enterica serovar Enteritidis by Lactobacillus crispatus and Clostridium lactatifermentans in a Sequencing Fed-Batch Culture

Competitive exclusion of Salmonella enterica serovar Enteritidis by a mixed culture of Lactobacillus crispatus and Clostridium lactatifermentans was studied in a sequencing fed-batch reactor mimicking the cecal ecophysiology of broiler chickens. Growth of serovar Enteritidis was inhibited by a mixed culture of L. crispatus and C. lactatifermentans at pH 5.8 but not by a monoculture of L. crispatus at the same pH. Moreover, experiments performed at pH 7.0 did not show growth inhibition of serovar Enteritidis. L. crispatus fermented lactose to lactate, and C. lactatifermentans fermented the lactate to acetate and propionate in a mixed culture of L. crispatus and C. lactatifermentans growing on lactose. In contrast, only lactate was produced from lactose by a monoculture of L. crispatus. At pH 5.8 considerable concentrations of acetate and propionate were present as undissociated acids, whereas only trace levels of undissociated lactate were present at pH 5.8 due to the low pK_a of lactate. At pH 7.0 all three acids were present in their dissociated forms. We conclude that a mixed culture of L. crispatus and C. lactatifermentans inhibits growth of serovar Enteritidis under cecal growth conditions. The undissociated forms of acetate and propionate produced in the mixed culture inhibited the growth of serovar Enteritidis.     

Applications of improved stoichiometric model in medium design and fed-batch cultivation of animal cells in bioreactor

In our previous work (Xie and Wang, 1994a), a simplified stoichiometric model on energy metabolism for animal cell cultivation was developed. Fed-batch experiments were performed in T-flasks using this model in supplemental medium design (Xie and Wang, 1994b). In this work, the major pathways of glucose and glutamine metabolism were incorporated into the stoichiometric model. Fed-batch culture was conducted in a 2-liter bioreactor with appropriate process control strategies. Nutrient concentrations, especially glucose and glutamine, were maintained at constant but low levels through the automated feeding of a supplemental medium formulated using the improved stoichiometric model. The formation of toxic byproducts, such as ammonia and lactate (Hassellet al., 1991), was greatly reduced. The specific lactate production rate was decreased by 62-fold compared with batch culture in bioreactor and by 8-fold compared to fed-batch culture in T-flask using the previous stoichiometric model. Ammonia formation was also decreased compared with both the batch and fed-batch cultures. Most importantly, the monoclonal antibody concentration reached 900 mg l^?1, an increase of 17- and 1.6-fold compared with the batch and fed-batch cultures respectively.     

Nisin Production by a Mixed-Culture System Consisting of Lactococcus lactis and Kluyveromyces marxianus

To control the pH during antimicrobial peptide (nisin) production by a lactic acid bacterium, Lactococcus lactis subsp. lactis (ATCC11454), a novel method involving neither addition of alkali nor a separation system such as a ceramic membrane filter and electrodialyzer was developed. A mixed culture of L. lactis and Kluyveromyces marxianus, which was isolated from kefir grains, was utilized in the developed system. The interaction between lactate production by L. lactis and its assimilation by K. marxianus was used to control the pH. To utilize the interaction of these microorganisms to maintain high-level production of nisin, the kinetics of growth of, and production of lactate, acetate, and nisin by, L. lactis were investigated. The kinetics of growth of and lactic acid consumption by K. marxianus were also investigated. Because the pH of the medium could be controlled by the lactate consumption of K. marxianus and the specific lactate consumption rate of K. marxianus could be controlled by changing the dissolved oxygen (DO) concentration, a cascade pH controller coupled with DO control was developed. As a result, the pH was kept constant because the lactate level was kept low and nisin accumulated in the medium to a high level compared with that attained using other pH control strategies, such as with processes lacking pH control and those in which pH is controlled by addition of alkali.     

Isolation of a Bacterial Culture That Degrades Methyl t-Butyl Ether

We have isolated a mixed bacterial culture (BC-1) which is capable of degrading the gasoline oxygenate methyl t-butyl ether (MTBE). BC-1 was developed from seed microorganisms present in a chemical plant biotreater sludge. This enrichment culture has been maintained in continuous culture treating high concentrations of MTBE (120 to 200 mg/liter) as the sole carbon source in a simple feed containing NH₄⁺, PO₄^3-, Mg²⁺, and Ca²⁺ nutrients. The unit had a stable MTBE removal rate when maintained with a long cell retention time (ca. 80 to 90 days); however, when operated at a ≤50-day cell waste rate, loss of MTBE-degrading activity was observed. The following three noteworthy experimental data show that MTBE is biodegraded extensively by BC-1: (i) the continuous (oxygen-sparged) culture was able to sustain a population of autotrophic ammonia-oxidizing bacteria which could nitrify influent NH₄⁺ concentrations at high rates and obtain CO₂ (sole carbon source for growth) from the metabolism of the alkyl ether, (ii) BC-1 metabolized radiolabeled either (¹⁴CH₃O-MTBE) to ¹⁴CO₂ (40%) and ¹⁴C-labeled cells (40%), and (iii) cell suspensions of the culture were capable of degrading (substrate depletion experiments) MTBE to t-butyl alcohol, a primary metabolite of MTBE. BC-1 is a mixed culture containing several bacterial species and is the first culture of its kind which can completely degrade an alkyl ether.     

Effect of dissolved oxygen concentration on repeated production of gluconic acid by immobilised mycelia of Aspergillus niger

Summary Gluconic acid production from corn starch hydrolysates by immobilised mycelia of Aspergillus niger was studied in a laboratory-scale stirred fermentor at different concentrations of glucose (S ₀) and dissolved oxygen (DO) in the culture broth. Its evolution was simulated quite well by applying the same unstructured model set up in previous experiments using stirred and airlift fermentors. In particular, increasing S ₀ in the range 70–160 g/l, although uninfluential upon the yield coefficient, resulted in an exponential decrease in the gluconic acid formation rate constant. Nevertheless, the greater the oxygen transfer rate used in the fermentor, the smaller the inhibitor effect of the higher concentrations of glucose on gluconate productivity became. This was achieved by enriching the inlet air with pure oxygen so as to maintain the DO level above 75% saturation throughout the fermentation. Offprint requests to: M. Moresi     

Selection of Type I and Type II methanotrophic proteobacteria in a fluidized bed reactor under non-sterile conditions

Type II methanotrophs produce polyhydroxybutyrate (PHB), while Type I methanotrophs do not. A laboratory-scale fluidized bed reactor was initially inoculated with a Type II Methylocystis-like dominated culture. At elevated levels of dissolved oxygen (DO, 9 mg/L), pH of 6.2–6.5 with nitrate as the N-source, a Methylobacter-like Type I methanotroph became dominant within the biofilms which did not produce PHB. A shift to biofilms capable of PHB production was achieved by re-inoculating with Type II Methylosinus culture, providing dissolved N₂ as the N-source, and maintaining a low influent DO (2.0 mg/L). The resulting biofilms contained both Types I and II methanotrophs. Batch tests indicated that biofilm samples grown with N₂ became dominated by Type II methanotrophs and produced PHB. Enrichments with nitrate or ammonium were dominated by Type I methanotrophs without PHB production capability. The key selection factors favoring Type II were N₂ as N-source and low DO.     

Utilization of aminoaromatic acids by a methanogenic enrichment culture and by a novel<Emphasis Type="Italic"> Citrobacter freundii</Emphasis> strain

Following incubation of mesophilic methanogenic floccular sludge from a lab-scale upflow anaerobic sludge bed reactor used to treat cattle manure wastewater, a stable 5-aminosalicylate-degrading enrichment culture was obtained. Subsequently, a Citrobacter freundii strain, WA1, was isolated from the 5-aminosalicylate-degrading methanogenic consortium. The methanogenic enrichment culture degraded 5-aminosalicylate completely to CH₄, CO₂ and NH₄ ⁺, while C. freundii strain WA1 reduced 5-aminosalicylate with simultaneous deamination to 2-hydroxybenzyl alcohol during anaerobic growth with electron donors such as pyruvate, glucose or serine. When grown on pyruvate, C. freundii WA1 converted 3-aminobenzoate to benzyl alcohol and also reduced benzaldehyde to benzyl alcohol. Pyruvate was fermented to acetate, CO₂, H₂ and small amounts of lactate, succinate and formate. Less lactate (30%) was produced from pyruvate when C. freundii WA1 grew with 5-aminosalicylate as co-substrate.     

Effectors of fatty acid synthesis in hepatoma tissue culture cells

An investigation was undertaken to better understand the process of fatty acid synthesis in hepatoma tissue culture (HTC) cells. By comparing the findings to the normal liver some of the differences between normal and cancer tissue were defined. Incubation of the HTC cells in a buffered salt-defatted albumin medium showed that fatty acid synthesis was dependent upon the addition of substrate. The order of stimulation was glucose + pyruvate ～- glucose + alanine ～- glucose + lactate ～- pyruvate > glucose > alanine ? no additions. Fatty acid synthesis in HTC cells was decreased by oleate. In these respects HTC cells are similar to the liver; however, in contrast to the normal liver, N⁶, O²-dibutyryl cyclic adenosine 3′,5′-monophosphate (dibutyryl-cAMP) did not inhibit glycolysis or fatty acid synthesis. The cytoplasmic redox potential, as reflected by the lactate to pyruvate ratio, was found to be elevated compared to normal liver but unchanged by the addition of dibutyryl cAMP. Since higher rates of fatty acid synthesis are associated with lower lactate-to-pyruvate ratios in normal liver, it was expected that by decreasing the lactate-to-pyruvate ratio in HTC cells the rate of fatty acid synthesis would increase. One way to lower the lactate to pyruvate ratio is to increase the activity of the malate-aspartate shuttle. Stimulators of the hepatic malate-aspartate shuttle in normal liver (ammonium ion, glutamine, and lysine) had mixed effects on the redox state and fatty acid synthesis in HTC cells. Both ammonium ion and glutamine decreased the redox potential and increased the rate of fatty acid synthesis. Lysine was without effect on either process. Since NH₄Cl and glutamine stimulate the movement of reducing equivalents into the mitochondria and decrease the redox potential, then the stimulation of fatty acid synthesis by NH₄Cl and glutamine may be due to an increase in the movement of reducing equivalents into the mitochondria. However, if the shuttle were rate determining for fatty acid synthesis the rate from added lactate would be the same as from glucose alone but would be lower than from pyruvate which does not require the movement of reducing equivalents. This was not the case. Lactate and pyruvate gave comparable rates which were higher than glucose alone. Other possible sites of stimulation were investigated. The possibility that NH₄⁺ and glutamine stimulated fatty acid synthesis by activating pyruvate dehydrogenase was excluded by finding that dichloroacetate, an activator of pyruvate dehydrogenase, did not stimulate fatty acid synthesis when glucose was added. Stimulation by NH₄⁺ and glutamine at steps beyond pyruvate dehydrogenase was ruled out by the observation that NH₄⁺ caused no stimulation from added pyruvate. NH₄⁺ and glutamine did not alter the pentose phosphate pathway as determined by ¹⁴CO₂ production from [1-¹⁴C]- or [6-¹⁴C]glucose. Ammonium ion and glutamine increased glucose consumption and increased lactate and pyruvate accumulation. The increased glycolysis in HTC cells appears to be the explanation for the stimulation of fatty acid synthesis by NH₄⁺ and glutamine, even though glycolysis is much more rapid than fatty acid synthesis in these cells. The following observations support this conclusion. First, the percentage increase in glycolysis caused by NH₄⁺ or glutamine is closely matched by the percentage increase in fatty acid synthesis. Second, the malate-aspartate shuttle, the pentose phosphate pathway, and the steps past pyruvate are not limiting in the absence of NH₄⁺ or glutamine.     

Deletion of cscR in Escherichia coli W improves growth and poly-3-hydroxybutyrate (PHB) production from sucrose in fed batch culture

Sucrose has several advantages over glucose as a feedstock for bioprocesses, both environmentally and economically. However, most industrial Escherichia coli strains are unable to utilize sucrose. E. coli W can grow on sucrose but stops growing when sucrose concentrations become low. This is undesirable in fed-batch conditions where sugar levels are low between feeding pulses. Sucrose uptake rates were improved by removal of the cscR gene, which encodes a protein that represses expression of the sucrose utilization genes at low sucrose concentrations. Poly-3-hydroxybutyrate (PHB) was used as a model compound in order to assess the effect of improved sugar utilization on bio-production. In the cscR knockout strain, production from sucrose was improved by 50%; this strain also produced 30% more PHB than the wild-type using glucose. This result demonstrates the feasibility of utilizing sucrose as an industrial feedstock for E. coli-based bioprocesses in high cell density culture.     

Influence of electron acceptor,carbon, nitrogen,and phosphorus on polyhydroxyalkanoate (PHA) production by <Emphasis Type="Italic">Brachymonas</Emphasis> sp. P12

Polyhydroxyalkanoates (PHAs), intracellular carbon and energy reserve compounds in many bacteria, have been used extensively in biodegradable plastics. PHA formation is influenced by nutrient limitations and growth conditions. To characterize the PHA accumulation in a new denitrifying phosphorus-removing bacterium Brachymonas sp. P12, batch experiments were conducted in which the electron acceptor (oxygen or nitrate) was varied and different concentrations of carbon (acetate), nitrogen (NH₄Cl), and phosphorus (KH₂PO₄) were used. Polyhydroxybutyrate (PHB) was the dominant product during PHA formation when acetate was the sole carbon source. The PHB content of aerobically growing cells increased from 431 to 636 mg PHB g⁻¹ biomass, but the PHB concentration of an anoxic culture decreased (−218 mg PHB g⁻¹ biomass), when PHB was utilized simultaneously with acetate as an electron donor for anoxic denitrification. The specific PHB production rate of the carbon-limited batch, 158.2 mg PHB g⁻¹ biomass h⁻¹, was much greater than that of batches with normal or excess carbon. The effects of phosphorus and nitrogen concentrations on PHB accumulation were clearly less than the effect of carbon concentration. According to the correlation between the specific PHB production rate and the specific cell growth rate, PHB accumulation by Brachymonas sp. P12 is enhanced by nutrient limitation, is growth-associated, and provides additional energy for the biosynthesis of non-PHB cell constituents to increase the cell growth rate beyond the usual level.     

Control of glucose feeding using exit gas data and its application to the production of PHB from tapioca hydrolysate byAlcaligenes eutrophus

Summary A method to estimate the glucose concentration in the culture broth using CO₂ evolution rate (CER) data from a mass spectrometer was developed.Alcaligenes eutrophus was cultivated to produce poly(3-hydroxybutyric acid) (PHB) from tapioca hydrolysate using this method. Thek value (g glucose/mol CO₂), defined as the glucose consumption per CO₂ evolution, decreased with culture time and was automatically changed using CER data. The glucose concentration in the culture broth could be controlled at 10 to 20 g/L. A final cell concentration of 106 g/L, PHB concentration of 61 g/L. and PHB content of 58 % of dry cell weight were obtained after 59 h of cultivation.     

Production of Polyhydroxyalkanoate Co-polymer by Bacillus thuringiensis

Integrative processes for the production of bioenergy and biopolymers are gaining importance in recent years as alternatives to fossil fuels and synthetic plastics. In the present study, Bacillus thuringiensis strain EGU45 has been used to generate hydrogen (H₂), polyhydroxybutyrate (PHB) and new co-polymers (NP). Under batch culture conditions with 250 ml synthetic media, B. thuringiensis EGU45 produced up to 0.58 mol H₂/mol of glucose. Effluent from the H₂ production stage was incubated under shaking conditions leading to the production of PHB up to 95 mg/l along with NP of levulinic acid up to 190 mg/l. A twofold to fourfold enhancement in PHB and up to 1.5 fold increase in NP yields was observed on synthetic medium (mixture of M-9+GM-2 medium in 1:1 ratio) containing at 1–2 % glucose concentration. The novelty of this work lies in developing modified physiological conditions, which induce bacterial culture to produce NP.     

Poly(3-hydroxybutyrate) production by <Emphasis Type="Italic">Halomonas boliviensis</Emphasis> in fed-batch culture

High poly(3-hydroxybutyrate) (PHB) content and volumetric productivity were achieved by fed-batch culture of Halomonas boliviensis using a defined medium. Initial shake flask cultivations in a minimal medium revealed that the growth of H. boliviensis was supported only when the medium was supplemented with aspartic acid, glycine, or glutamine. Addition of 0.1% (w/v) glutamine in the medium resulted in the highest cell dry weight (CDW; 3.9 g l⁻¹). Glutamine was replaced by the less expensive monosodium glutamate (MSG) in the medium without any notable change in the final cell density. Effect of initial concentrations of NH₄Cl and K₂HPO₄ on cell growth and PHB accumulation by H. boliviensis was then analyzed using a fed-batch fermentation system. The best conditions for PHB production by H. boliviensis were attained using 0.4% (w/v) NH₄Cl and 0.22% (w/v) K₂HPO₄ and adding MSG intermittently to the fermentor. Poly(3-hydroxybutyrate) content and CDW reached 90 wt.% and 23 g l⁻¹, respectively, after 18 h of cultivation. In order to increase CDW and PHB content, MSG, NH₄Cl, and K₂HPO₄ were initially fed to the fermentor to maintain their concentrations at 2%, 0.4%, and 0.22% (w/v), respectively, and subsequently their feed was suppressed. This resulted in a CDW of 44 g l⁻¹, PHB content of 81 wt.%, and PHB volumetric productivity of 1.1 g l⁻¹ h⁻¹.