Fed-batch culture of<Emphasis Type="Italic"> Bacillus thuringiensis</Emphasis> based on motile intensity

The operation of a fed-batch culture is more complicated than that of batch or continuous culture. Thus, an appropriate feeding strategy for fed-batch cultures should be carefully designed. In this study, a simple feeding strategy for fed-batch culture of Bacillus thuringiensis based on motile intensity is described. The feeding strategy consisted of two steps: (1) initiating feeding at the peak of motile intensity; (2) terminating feeding at low motile intensity (or non-motility) of the cells. In addition, the motile intensity of B. thuringiensis was used to determine the optimum environmental conditions (pH, temperature, and dissolved oxygen) and optimum medium composition. Using this fed-batch strategy, the production of thuringiensin increased 34% compared with batch culture using the same environmental conditions and medium composition. The proposed strategy for fed-batch culture helps to avoid overfeeding of substrate and facilitates on-line control. A comparison of several alternative strategies for fed-batch culture demonstrated that strategies such as glucose-stat and DO-stat result in a lower productivity than that obtained using the motility intensity method.     

Scale-up fermentation of recombinant <Emphasis Type="Italic">Candida rugosa</Emphasis> lipase expressed in <Emphasis Type="Italic">Pichia pastoris</Emphasis> using the GAP promoter

The high-cell-density fermentation of Candida rugosa lipase in the constitutive Pichia pastoris expression system was scaled up from 5 to 800 l in series by optimizing the fermentation conditions at both lab scale and pilot scale. The exponential feeding combined with pH-stat strategy succeeded in small scale studies, while a two-stage fermentation strategy, which shifted at 48 h by fine tuning the culture temperature and pH, was assessed effective in pilot-scale fermentation. The two-stage strategy made an excellent balance between the expression of heterogeneous protein and the growth of host cells, controlling the fermentation at a relatively low cell growth rate for the constitutive yeast expression system to accumulate high-level product. A stable lipase activity of approximately 14,000 IU ml⁻¹ and a cell wet weight of ca. 500 g l⁻¹ at the 800-l scale were obtained. The efficient and convenient techniques suggested in this study might facilitate further scale-up for industrial lipase production.     

Fermentative production of P(3HB-co-3HV) from propionic acid by Alcaligenes eutrophus in fed-batch culture with pH-stat continuous substrate feeding method

The feeding of propionic acid for production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] by Alcaligenes eutrophus ATCC17697 was optimized using a fed-batch culture system. The concentration of propionic acid was maintained at 3 g l^–1 as growth was inhibited by propionic acid in the broth. A pH-stat substrate feeding system was used in which propionic acid was fed automatically to maintain a pH of the culture broth at 7.0. By feeding a substrate solution containing 20% (w/v) propionic acid, 4.9% (w/v) ammonia water [at a molar ratio of carbon to nitrogen (C/N molar ratio) of 10] in cell growth phase, the concentration of propionic acid in the broth was maintained at 3 g l^–1 giving a specific growth rate of 0.4 h^–1. To promote P(3HB-co-3HV) production, two stage fed-batch culture which consisted of the stage for the cell growth and the stage for the P(3HB-co-3HV) accumulation was carried out. When the substrate solution whose C/N molar ratio was 50 was fed in P(3HB-co-3HV) accumulation phase, the cell concentration and the P(3HB-co-3HV) content in the cells reached 64 g l^–1 and 58% (w/w) in 55.5 h, respectively.     

Mixed-feed exponential feeding for fed-batch culture of recombinant methylotrophic yeast

A simple, accurate model capable of predicting cell growth and methanol utilization during the mixed substrate fed-batch fermentation of Mut^S recombinant Pichia pastoris was developed and was used to design an exponential feeding strategy for mixed substrate fed-batch fermentation at a constant specific growth rate. Mixed substrate feeding has been shown to boost productivity in recombinant fed-batch culture of P. pastoris, while fixed growth rate exponential feeding during fed-batch culture is a useful tool in process optimization and control.     

High-level production of arachidonic acid by fed-batch culture of <Emphasis Type="Italic"> Mortierella alpina</Emphasis> using NH<Subscript>4</Subscript>OH as a nitrogen source and pH control

Mortierella alpina was grown in a fed-batch culture using a 12-l jar fermenter with an initial 8-l working volume containing 20 g glucose l⁻¹ and 10 g corn-steep powder l⁻¹. Glucose was intermittently fed to give 32 g l⁻¹ at each time. The pH of culture was maintained using 14% (v/v) NH₄OH, which also acted as a nitrogen source. A final cell density of 72.5 g l⁻¹ was reached after 12.5 days with a content of arachidonic acid (ARA) at 18.8 g l⁻¹. These values were 4 and 1.8 times higher than the respective values in batch culture. Our results suggest that the combined feeding of glucose and NH₄⁺ to the growth of M. alpina could be applied for the industrial scale production of ARA.     

Improving intracellular production of recombinant protein in <Emphasis Type="Italic">Pichia pastoris</Emphasis> using an optimized preinduction glycerol-feeding scheme

High-cell-density production of recombinant growth hormone of Lateolabrax japonicus (rljGH) expressed intracellularly in Pichia pastoris was investigated. In the regular strategy of induction at a cell density of 160 g l⁻¹, short duration of intracellular rljGH accumulation (17 h) resulted in a low final cell density of 226 g l⁻¹. Thus, a novel strategy of induction at a cell density of 320 g l⁻¹ was investigated. In this strategy, the preinduction glycerol-feeding scheme had a significant effect on the post-induction production. Constant glycerol feeding led to a decrease of the specific rljGH production and specific production rate because of low preinduction specific growth rate. This decrease was avoided by exponential glycerol feeding to maintain a preinduction specific growth rate of 0.16 h⁻¹. The results from exponential glycerol feeding indicated that the rljGH production depended on the preinduction specific growth rate. Moreover, mixed feeding of methanol and glycerol during induction improved the specific production rate to 0.07 mg g⁻¹ h⁻¹ from 0.043 mg g⁻¹ h⁻¹. Consequently, both high cell density (428 g l⁻¹) and high rljGH production could be achieved by the novel strategy: growing the cells at the specific growth rate of 0.16 h⁻¹ to the cell density of 320 g l⁻¹ and inducing the expression by mixed feeding.     

Fed-batch fermentation for production of Kluyveromyces marxianusFII 510700 cultivated on a lactose-based medium

A strain of Kluyveromyces marxianus was grown in batch culture in lactose-based media at varying initial lactose concentrations (10–60 g L^–1) at 30°C, pH 5.0, dissolved oxygen concentrations greater than 20%. Increasing the concentration of mineral salts three-fold at 40 g L^–1 and 60 g L^–1 initial lactose concentration showed only a small increase in the yield of biomass, from 0.38 g g^–1 to 0.41 g g^–1, indicating that the initial batch cultures were not significantly nutrient- (mineral salts)-limited. A relatively high biomass concentration (105 g L^–1) was obtained in fed-batch culture following extended lactose feeding. An average specific growth rate (0.27 h^–1), biomass yield (0.38 g g^–1) and overall productivity (2.9 g L^–1 h^–1) were obtained for these fed-batch conditions. This fed-batch protocol provides a strategy for achieving relatively high concentrations and productivities of K. marxianus on other lactose-based substrate streams (e.g., whey) from the dairy industry.     

Ethanol production from sweet sorghum juice in batch and fed-batch fermentations by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Sweet sorghum juice supplemented with 0.5% ammonium sulphate was used as a substrate for ethanol production by Saccharomyces cerevisiae TISTR 5048. In batch fermentation, kinetic parameters for ethanol production depended on initial cell and sugar concentrations. The optimum initial cell and sugar concentrations in the batch fermentation were 1 × 10⁸ cells ml⁻¹ and 24 °Bx respectively. At these conditions, ethanol concentration produced (P), yield (Y _ps) and productivity (Q _p ) were 100 g l⁻¹, 0.42 g g⁻¹ and 1.67 g l⁻¹ h⁻¹ respectively. In fed-batch fermentation, the optimum substrate feeding strategy for ethanol production at the initial sugar concentration of 24 °Bx was one-time substrate feeding, where P, Y _ps and Q _p were 120 g l⁻¹, 0.48 g g⁻¹ and 1.11 g l⁻¹ h⁻¹ respectively. These findings suggest that fed-batch fermentation improves the efficiency of ethanol production in terms of ethanol concentration and product yield.     

Stimulation of menthol production in <Emphasis Type="Italic">Mentha piperita</Emphasis> cell culture

Plant cell culture provides an alternative means for producing secondary metabolites. In this study, experiments were carried out to study the impact of several parameters, independently and in combination, on the stimulation of menthol production in the cell suspension culture of Mentha piperita. Callus was obtained from leaf segments of in vitro grown plantlets on Murashige and Skoog (MS) medium supplemented with 0.2 mg l⁻¹of 2,4-dichlorophenoxy acetic acid to initiate cell suspension culture. This culture was maintained in half-strength MS medium supplemented with 0.2 mg l⁻¹of 2,4-dichlorophenoxy acetic acid at 15 d interval and used for further studies. Precursor feeding alone, i.e., menthone, at 35 μM concentration showed slightly improved productivity. γ-Cyclodextrin alone at 60 μM concentration and in combination with menthone feeding at 35 μM increased menthol yield up to 92 and 110 mg l⁻¹ in comparison to 77 mg l⁻¹ of control culture. Synergistic potentiation effect of menthone feeding at 35 μM and γ-cyclodextrin at 60 μM treatment followed by in situ adsorption with RP-8 also showed potential stimulation of menthol production in M. piperita cell culture. Fungal elicitor treatment showed enhanced production level up to 140.8 mg l⁻¹ in comparison to that of control. Further studies were carried out with the establishment of Agrobacterium tumefaciens (Ach5) gall-mediated calli, and consequently, cell suspension culture and results showed the significant enhancement of menthol yield up to 278 mg l⁻¹. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

High level expression of a recombinant phospholipase C from <Emphasis Type="Italic">Bacillus cereus</Emphasis> in <Emphasis Type="Italic">Bacillus subtilis</Emphasis>

Twenty-two Bacillus cereus strains were screened for phospholipase C (PLC, EC 3.1.4.3) activity using p-nitrophenyl phosphorylcholine as a substrate. Two strains (B. cereus SBUG 318 and SBUG 516) showed high activity at elevated temperatures (>70°C) at acidic pH (pH 3.5–6) and were selected for cloning and functional expression using Bacillus subtilis. The genes were amplified from B. cereus DNA using primers based on a known PLC sequence and cloned into the expression vector pMSE3 followed by transformation into B. subtilis WB800. On the amino acid level, one protein (PLC318) was identical to a PLC described from B. cereus, whereas PLC516 contained an amino acid substitution (E173D). PLC production using the recombinant strains was performed by an acetoin-controlled expression system. For PLC516, 13.7 U g⁻¹ wet cell weight was determined in the culture supernatant after 30 h cultivation time. Three purification steps resulted in pure PLC516 with a specific activity of 13,190 U mg⁻¹ protein.     

Optimization of production of caffeine demethylase by <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. in a bioreactor

The effect of pH, aeration rate, and agitation rate on specific productivity of caffeine demethylase from Pseudomonas sp. was studied in a bioreactor. Maximum specific productivity of caffeine demethylase of 2,214 U g cell dry weight⁻¹ h⁻¹ was obtained at 0.27 vvm, 700 rpm, and pH 7.0. Under these conditions, volumetric oxygen transfer coefficient was 74.2 h⁻¹, indicating that caffeine demethylase production by Pseudomonas sp. was highly oxygen-dependent. Different metabolite formation at different agitation and aeration rates can be used as a strategy for recovery of pharmaceutically important metabolites from caffeine by manipulation of conditions in a bacterial culture. This is the first report on production of high levels of caffeine demethylase in bioreactors.     

Biosynthesis and properties of an extracellular thermostable serine alkaline protease from <Emphasis Type="Italic">Virgibacillus pantothenticus</Emphasis>

In this communication, we report the presence of a newly identified serine alkaline protease producing bacteria, Virgibacillus pantothenticus (MTCC 6729) in the fresh chicken meat samples and the factors affecting biosynthesis as well as characterization of protease. The strain produced only 14.3 U ml⁻¹ protease in the standard medium after 72 h of incubation, while in optimized culture conditions the production of protease was increased up to 18.2 U ml⁻¹. The strain was able to produce protease at 40°C at pH 9.0. The addition of dextrose and casein improved protease production. The protease was partially purified and characterized in terms of pH and temperature stability, effect of metal ions and inhibitors. The protease was found to be thermostable alkaline by retaining its 100% and 85% stability at pH 10.0 and at 50°C respectively. The protease was compatible with some of the commercial detergents tested, and was effective in removing protein stains from cotton fabrics. The V. pantothenticus, MTCC 6729 protease appears to be potentially useful as an additive in detergents as a stain remover and other bio-formulations.     

Growth inhibition by ammonia and use of a pH-controlled feeding strategy for the effective cultivation of Mycobacterium chlorophenolicum

The inhibitory effect of ammonia on the growth of the polychlorinated xenobiotic-degrading bacterium Mycobacterium chlorophenolicum was examined. The strain is inhibited by both the ionized and nonionized forms of ammonia. At pH 6.9 50% reduction of the growth rate was observed at 6.8 g l^–1 total ammonium. For 23 experiments performed in shake-flask culture at different pH values and ammonium concentrations a growth model based on the extended Monod kinetic fits the data with a deviation of 5.3%. To overcome growth inhibition in bioreactors a pH-controlled feeding strategy was developed for effective cultivation of M. chlorophenolicum at an ammonium level below 0.3 g l^–1. The ammonium addition was controlled on-line by the stoichiometric interdependence of ammonium consumption and pH decline. With this on-line control strategy a biomass concentration as high as 26.2 g l^–1 can be achieved within less than 1 week of cultivation, compared to a biomass concentration of 15.5 g l^–1 in normal batch culture after 2 weeks of cultivation. The yield is also increased from 0.32 g to 0.43 g biomass (g glucose)^–1. The strategy developed provides an effective method for the production of biomass of M. chlorophenolicum serving as the inoculum in remediation technologies.     

Improvement of nisin production in pH feed-back controlled,fed-batch culture by <Emphasis Type="Italic">Lactococcus lactis</Emphasis>subsp<Emphasis Type="Italic">. lactis</Emphasis>

Nisin production by Lactococcus lactis subsp. lactisin fed-batch culture was doubled by using a pH feed-back controlled method. Sucrose concentration was controlled at 10 g l^–1 giving 5010 IU nisin ml^–1 compared to 2660 IU nisin ml^–1 in batch culture.     

<Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> NAD-dependent, <Emphasis Type="SmallCaps">D</Emphasis>-fructose reducing,polyol dehydrogenases activity: screening,medium optimisation and application for enzymatic polyol production

Gluconobacter oxydans LMG 1489 was selected as the best strain for NAD(P)-dependent polyol dehydrogenase production. The highest enzyme activities were obtained when this strain was cultivated on a medium consisting of 30 g glycerol l^–1, 7.2 g peptone l–1 and 1.8 g yeast extract l^–1. Two D-fructose reducing, NAD-dependent intracellular enzymes were present in the G. oxydans cell-free extract: sorbitol dehydrogenase, and mannitol dehydrogenase. Substrate reduction occurred optimally at a low pH (pH 6), while the optimum for substrate oxidation was situated at alkaline pHs (pH 9.5–10.5). The mannitol dehydrogenase was more thermostable than the sorbitol dehydrogenase. The cell-free extract could be used to produce D-mannitol and D-sorbitol enzymatically from D-fructose. Efficient coenzyme regeneration was accomplished by formate dehydrogenase-mediated oxidation of formate into CO₂.     

Purification and Properties of a Phytate-degrading Enzyme from <Emphasis Type="Italic">Pantoea agglomerans</Emphasis>

A periplasmatic phytate-degrading enzyme from Pantoea agglomerans isolated from soil was purified about 470-fold to apparent homogeneity with a recovery of 16% referred to the phytate-degrading activity in the crude extract. It behaved as a monomeric protein with a molecular mass of about 42 kDa. The purified enzyme exhibited a single pH optimum at 4.5. Optimum temperature for the degradation of phytate was 60°C. The kinetic parameters for the hydrolysis of sodium phytate were determined to be K_M = 0.34 mmol/l and k_cat = 21 s^-1 at pH 4.5 and 37°C. The enzyme exhibited a narrow substrate selectivity. Only phytate and glucose-1-phosphate were identified as good substrates. Since this Pantoea enzyme has a strong preference for glucose-1-phosphate over phytate, under physiological conditions glucose-1-phosphate is its most likely substrate. The maximum amount of phosphate released from phytate by the purified enzyme suggests myo-inositol pentakisphosphate as the final product of enzymatic phytate degradation.     

Development of a fed-batch process for the production of a dye-linked formaldehyde dehydrogenase in <Emphasis Type="Italic">Hyphomicrobium zavarzinii ZV 580</Emphasis>

The dye-linked formaldehyde dehydrogenase (dlFalDH) from Hyphomicrobium zavarzinii ZV 580 processes formaldehyde in a highly selective manner and without need for NAD(P). The enzyme thus has considerable potential for technical applications if the difficulties associated with its efficient production can be resolved. In this contribution, a fed-batch bioprocess is developed, which improves both the biomass production of H. zavarzinii ZV 580 (from 0.6 to 2 g l⁻¹ dry mass) and the specific dlFalDH production (from 0.1 to 0.3 units g⁻¹ biomass), resulting in an overall improvement of the productivity by more than an order of magnitude compared to the previously reported process (Klein et al., Biochem J 301:289–295, 1994). In particular, the process uses an automated feeding strategy controlled via the dissolved oxygen concentration. In addition, our results show that the growth of H. zavarzinii ZV 580 is rather sensitive toward increasing salt concentration in the culture medium. Growth is also inhibited by the presence of surfactant-based antifoam reagents. Adjustment of the pH via the addition of methylamine instead of NaOH, on the other hand, leads to an increase in biomass yield.     

Polyphenol oxidase activity in dormant saffron (<Emphasis Type="Italic">Crocus sativus</Emphasis> L<Emphasis Type="Italic">.</Emphasis>) corm

Crocus sativus L., cultivated since ancient times as the source of saffron, is a triploid plant that can be propagated only via its corms which undergo a period of dormancy. Understanding the processes taking place in the corm is essential to preserve the plant and improve its quality. Color and taste being of prime importance in the quality of the saffron spice, knowledge on polyphenol oxidase (PPO) activity in the plant is of particular interest given the role of the enzyme in fruit and vegetable browning during processing and during the storage of processed food. In this paper, PPO activity was investigated for the first time in extracts obtained from dormant C. sativus L. corms. PPO activity was detectable using l-DOPA, pyrogallol, catechol or p-cresol as substrate, each being oxidized to its corresponding o-quinone; no activity was detectable with l-tyrosine, tyramine or phenol as substrate. Two pH optima, respectively at 4.5 and 6.7, were observed with all substrates and a third one, at 8.5, was found with l-DOPA and p-cresol. Kinetics parameters studied at pH 6.7 indicated the highest catalytic efficiency (in units mg⁻¹ prot mM⁻¹) with pyrogallol: 150, then catechol: 39, l-DOPA: 6.4 and p-cresol: 4.6. The enzymatic activity was inhibited by 50% in the presence of 0.22, 0.35, 0.5 and 0.7 mM kojic acid with, respectively, catechol, pyrogallol, p-cresol and l-DOPA as substrate. When stained for PPO activity, non-denaturing gel electropherograms of extract revealed three distinct bands, indicating the presence of multiple isoenzymes in dormant C. sativus L. corms.     

Purification and characterization of lignin peroxidases from <Emphasis Type="Italic">Penicillium decumbens</Emphasis> P6

Summary Peroxidases are essential enzymes in biodegradation of lignin and lignite which have been investigated intensively in the white-rot fungi. This is the first report of purification and characterization of lignin peroxidase from Penicillium sp. P6 as lignite degradation fungus. The results indicated that the lignin peroxidase of Penicillium decumbens P6 had physical and chemical properties and a N-terminal amino acid sequence different from the lignin peroxidases of white-rot fungi. The lignin peroxidase was isolated from a liquid culture of P. decumbens P6. This enzyme had a molecular weight of 46.3 KDa in SDS-PAGE and exhibited greater activity, temperature stability and wider pH range than those previously reported. The isolation procedure involved (NH₄)₂SO₄ precipitation, ion-exchange chromatography on DEAE-cellulose and CM-cellulose, gel filtration on Sephadex G-100, and non-denaturing, discontinuous polyacrylamide gel electrophoresis. The K _m and V _max values of this enzyme using veratryl alcohol as substrate were 0.565 mmol L ⁻¹ and 0.088 mmol (mg protein) ⁻¹ min ⁻¹ respectively. The optimum pH of P6 lignin peroxidase was 4.0, and 70.6 of the relative activity was remained at pH 9.0. The optimum temperature of the enzyme was 45 °C.     

Lactose-induced Production of Human Soluble B Lymphocyte Stimulator (hsBLyS) in E. coli with Different Culture Strategies

Over-production of human soluble B lymphocyte stimulator (hsBLyS) was carried out with four different fed-batch culture strategies using lactose as inducer, instead of IPTG, in a fed-batch culture of Escherichia coli. As lactose acted as both inducer and carbon source, the best and simplest culture strategy was direct feeding of lactose after batch culture, thereby giving hsBLyS at 3.7 g l⁻¹ and a productivity of 0.11 g l⁻¹ h⁻¹. Revisions requested 1 September 2005 and 11 November 2005; Revisions received 7 November 2005 and 4 January 2006