Inulinase (β-fructofuranosidase) production by Kluyeromyces marxianus in batch culture

Summary Production of inulinase in batch fermentation using various carbon sources with Kluyermoyces marxianus was examined. Inulinase synthesis in the culture proceeded parallel to cell growth. Glucose, fructose and sucrose were inferior carbon sources for inulinase broduction. Highest production (212 U/mL) was achieved on inulin based media.     

Enhanced production of α-ketoglutarate by fed-batch culture in the metabolically engineered strains of Corynebacterium glutamicum

The fed-batch culture system was employed to enhance production of α-ketoglutarate (α-KG) by the strainsof Corynebacterium glutamicum, whose genes encoding the key enzymes responsible for the biosynthesis of L-glutamate from α-KG were deleted. In a shake flask fermentation, C. glutamicum JH110 in which the 3 genes, gdh (encoding glutamate dehydrogenase), gltB (encoding glutamate synthase), and aceA (encoding isocitrate lyase) were disrupted showed the highest production of α-KG (12.4 g/L) compared to the strains JH102 (gdh mutant), JH103 (gltB mutant), and JH107 (gdh gltB double mutant). In the fed-batch cultures using a 5 L-jar fermenter, the strain JH107 produced more α-KG (19.5 g/L), but less glutamic acid (23.3 g/L) than those produced by the parent strain HH109, as well as JH102. The production of α-KG was significantly enhanced and the accumulation of glutamicacid was minimized by the ammonium-limited fed-batch cultures employing C. glutamicum JH107. Further improvement of α-KG production by the strain JH107 was achieved through the ammonium-limited fed-batch culture with the feeding of molasses, and the levels of α-KG and glutamic acid produced were 51.1 and 0.01 g/L, respectively.     

Formulation of a lactose-free, low-cost culture medium for the production of β- D-galactosidase by Kluyveromyces marxianus

A lactose-free, low-cost culture medium for the production of -d-galactosidase by Kluyveromyces marxianus was formulated. At high aeration rates (2.2 vvm) and concentrations of 100 g sugar cane molasses l^–1 as carbon source and 100 g corn steep liquor l^–1 as vitamin and nitrogen source an enzyme production of 708 U l^–1 h was achieved. This was 20% higher than using a medium that contained lactose which is considered the primary inductor of -d-galactosidase synthesis.     

The production of α-amylase (E.C.3.2.1.1.) byBacillus amyloliquefaciens,in a complex and a totally defined synthetic culture medium

The production of -amylase byBacillus amyloliquefaciens in both complex and synthetic culture media was examined at a laboratory fermenter scale. In a complex medium which supports fast growth rates, enzyme production occurred only when the growth rate declined, principally in the stationary phase. By contrast, in a synthetic culture medium with lactose as the carbon source supporting much lower growth rates, enzyme formation occurred simultaneously with cell growth. The repression of enzyme formation during rapid growth may be due either to catabolite repression or to the low level of mRNA synthesis concerned with the production of exoproteins.     

Bioconversion of lutein using a microbial mixture—maximizing the production of tobacco aroma compounds by manipulation of culture medium

The generation of aroma compounds by carotenoid cleavage in the 9–10 position was studied, due to the importance of these compounds in the flavor and fragrance industry. The bioconversion of the carotenoid lutein to C₁₃ norisoprenoids utilizing a microbial mixture composed of Trichosporon asahii and Paenibacillus amylolyticus was carried out by a fermentation process. Applying an experimental design methodology, the effects of nutritional factors on the production of aroma compounds present in the tobacco profile were studied. After an assessment of the significance of each nutritional factor, the levels of the variables yielding the maximum response were calculated. Glucose, tryptone, and yeast extract exerted a strong negative effect over the objective function, with glucose being the strongest. Lutein possessed a positive effect over the tobacco aroma production, while sodium chloride and trace elements showed no influence over the process. The yield attained after culture medium manipulation was almost ten-fold higher, compared with the base medium; and the aroma mixture was characterized as: 7,8-dihydro--ionol (95.2%), 7,8-dihydro--ionone (3.7%), and -ionone (1.1%).     

Investigation of poly ( β-L-malic acid) production by strains of Aureobasidium pullulans

 Eight strains of the genus Aureobasidium obtained from culture collections were tested for their capability to produce poly(β-L-malic acid) (PMA). Four of the tested strains showed positive results. The most productive strain, A. pullulans CBS 591.75, was used to study the production of PMA in stirred-tank reactors. It was found that PMA was mainly produced in the late exponential phase, and the production related positively to glucose consumption. At the beginning of the fermentation the pH increased from 4.0 to about 7.0; subsequently the pH decreased and remained stable at around 3.0–3.5 for several days. Temperatures higher than 25^°C were detrimental to PMA production and cell growth. PMA production and cell growth at 20^°C and 25^°C exhibited no significant differences. PMA production and cell growth were studied under pH-controlled fermentation (at pH 2.0, 4.0, 5.5). The highest PMA production occurred at pH 4.0. PMA production was reduced at pH 2.0 although quite reasonable cell growth occurred at this pH value. Under optimized conditions 9.8 g PMA/l was produced during 9 days of fermentation in the stirred-tank reactors with an overall yield of 0.11 g PMA/g glucose. A procedure for the isolation of PMA and its separation from the other components of the fermentation broth was developed. The isolated PMA was characterized by ¹H and ¹³C-NMR spectroscopy as well as by infrared absorption spectroscopy. Gel-permeation chromatography revealed a relative molecular mass of approximately 3000–5000 by comparison with polyethylene glycol standards. Received: 13 February 1996/Received revision: 25 April 1996/Accepted: 1 May 1996     

Effect of oxygen transfer rate on β-carotene production from synthetic medium by Blakeslea trispora in shake flask culture

The effect of oxygen transfer rate (OTR) on β-carotene production by Blakelsea trispora in shake flask culture was investigated. The results indicated that the concentration of β-carotene (704.1 mg/l) was the highest in culture grown at maximum OTR of 20.5 mmol/(l h). In this case, the percentage of zygospores was over 50.0% of the biomass dry weight. On the other hand, OTR level higher than 20.5 mmol/(l h) was found to be detrimental to cell growth and pigment formation. To elucidate the effect of oxidative stress on β-carotene synthesis, the accumulation of hydrogen peroxide during fermentation under different OTRs was determined. A linear response of β-carotene synthesis to the level of H₂O₂ was observed, indicating that β-carotene synthesis is stimulated by H₂O₂. However, there was an optimal concentration of H₂O₂ (2400 μM) in enhancing β-carotene synthesis. At a higher concentration of H₂O₂, β-carotene decreased significantly due to its toxicity.     

Production of α-amylase by Bacillus amyloliquefaciens in batch and continuous culture using a defined synthetic medium

Summary Using a totally defined synthetic medium the effect of lactose and nitrogen on cell physiology and -amylase production by Bacillus amyloliquefaciens B155 were investigated. Results showed cell growth and -amylase production patterns to be similar regardless of the limiting nutrient and suggested stationary phase gene control of -amylase production as opposed to a direct response to nutrient limitation.     

Protein production (β-galactosidase) from a baculovirus vector inSpodoptera frugiperda andTrichpolusia ni cells in suspension culture

Protein production capabilities ofTrichpolusia ni (TN 368) cells andSpodoptera frugiperda (Sf9) cells were compared in GTC100 medium in suspension culture using as a vector a genetically engineeredAutographa californica nuclear polyhedrosis virus. TN 368 produces more -galactosidase than Sf9, on a per cell basis (2.2×10⁵ and 1.7×10⁵ units/ 10⁶ cells¹ respectively). In growth experiments serum-free medium supported a higher maximum Sf9 cell density (4±1×10⁶ cells/ml) than the serum- based media (1.5±5×10⁶ cells/ml in GTC100 and 2±1×10⁶ cells/ml in TNM-FH). However, using a cell density of 5×0⁵ cells/ml, the productivity per cell varied, from a low of 4.5×10⁴ units in EX-CELL-400 medium to a high of 7.6×10⁴ units in TNM-FH. The TN 368 cells were twice a large as Sf9 cells and appeared to be more shear sensitive than Sf9 cells.     

Effects of culture conditions on β-poly(l-malate) production by Physarum polycephalum

Culture conditions for the fermentative production of β-poly(l-malate) (PMLA) by microplasmodia of Physarum polycephalum were investigated and optimized. Optimal production was achieved in the presence of CaCO₃. For 1.5% (w/v) d-glucose, 1% bactotryptone and 1% CaCO₃, a maximum of 1.7 g PMLA/l was secreted in 3 days. For 4.5% glucose and otherwise the same conditions, 2.7 g PMLA/l was produced in 6 days. The contribution of carbonate was inhibited by avidin. PMLA and biomass production were not strictly coupled: PMLA was also synthesized at the beginning of the stationary phase. At pH 5.5 PMLA production was twice that at pH 4.0, while biomass was not changed. Optimal temperatures were 24–28 °C. Received: 12 November 1998 / Received revision: 10 February 1999 / Accepted: 12 February 1999     

Effect of culture pH on recombinant antibody production by a new human cell line, F2N78, grown in suspension at 33.0 °C and 37.0 °C

The human host cell line, F2N78, is a new somatic hybrid cell line designed for therapeutic antibody production. To verify its potential as a human host cell line, recombinant F2N78 cells that produce antibody against rabies virus (rF2N78) were cultivated at different culture pH (6.8, 7.0, 7.2, 7.4, and 7.6) and temperatures (33.0 °C and 37.0 °C). Regardless of the culture temperature, the highest specific growth rate was obtained at a pH of 7.0–7.4. Lowering the culture temperature from 37.0 °C to 33.0 °C suppressed cell growth while allowing maintenance of high cell viability for a longer period. However, it did not enhance antibody production because specific antibody productivity did not increase at 33.0 °C. The highest maximum antibody concentration was obtained at 37.0 °C and pH 6.8. The N-linked glycosylation of the antibody was affected by the culture pH rather than the temperature. Nevertheless, G1F was dominant and G2F occupied a larger portion than G0F in all culture conditions. Compared to the same antibody produced from recombinant CHO cells, the antibody produced from rF2N78 cells has more galactose capping and was more similar to human plasma IgG. Taken together, the results obtained here demonstrate the potential of F2N78 as an alternative human host cell line for therapeutic antibody production.     

Improvement in cell yield of Methylobacterium sp. by reducing the inhibition of medium components for poly-β-hydroxybutyrate production

The inhibitory effect of the concentrations of medium components on the growth of Methylobacterium sp. for poly--hydroxybutyrate production was investigated by measuring the specific growth rates for various concentrations of each medium component. When the methanol concentration was increased, the cell growth decreased and was strongly inhibited above 6% (v/v) methanol. Ammonia, calcium and iron ion did not significantly inhibit the cell growth while there were some inhibitory effects at high concentrations of sodium, potassium, and magnesium. In particular, phosphate gave most significant inhibition at concentrations higher than 75 mM. By using an automatic feeding control system of methanol, ammonia, phosphate, and minerals, their concentrations were maintained within the level necessary to reduce the inhibition of medium components. The finial dry cell weight of Methylobacterium sp. in such a system was 172 g/l at 84 h.     

Outdoor H₂ production in a 50-L tubular photobioreactor by means of a sulfur-deprived culture of the microalga Chlamydomonas reinhardtii

In the past decade, H? production using the green microalga Chlamydomonas reinhardtii has been extensively studied under laboratory-scale photobioreactors, while information on outdoor cultures is still lacking. In this paper, the results of experiments conducted with sulfur-deprived cultures of C. reinhardtii carried out in a 50-L horizontal tubular photobioreactor are presented. Hydrogen production experiments were carried out under both artificial and direct solar light. In both cases, the H? output attained was 18-20% of what obtained in the laboratory. However, no significant changes in the H? production were observed when cells grown outdoors were tested under laboratory conditions. Chlorophyll fluorescence measurements showed that outdoor cultures were subjected to strong photo-inhibition, due to the combination of high solar light intensity and sulfur-deprivation. Indeed, H? production was only achieved outdoors when cultures were previously acclimated to sunlight, a condition that caused a number of physiological changes, namely: (i) a decrease in the chlorophyll content per unit of dry weight; (ii) an increase in the photosynthesis and respiration rates, and (iii) a higher induction of the xanthophyll cycle pigments as compared to non-acclimated cultures. It was concluded that the reduced H? output achieved in the 50-L photobioreactor was due to the different illumination pattern to which the cultures were exposed (one-sided vs. two-sided illumination provided in the laboratory), as well as to the great difference in the mixing times (60 min vs. 15.5s achieved in the lab-scale photobioreactor). To the very best of our knowledge this is the first time that H? production with green algae has been achieved by means of solar light.     

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.     

Poly(β-hydroxybutyrate) production in oilseed leukoplasts of Brassica napus

Polyhydroxyalkanoates (PHAs) comprise a class of biodegradable polymers which offer an environmentally sustainable alternative to petroleum-based plastics. Production of PHAs in plants is attractive since current fermentation technology is prohibitively expensive. The PHA homopolymer poly(β-hydroxybutyrate) (PHB) has previously been produced in leaves of Arabidopsis thaliana (Nawrath et al., 1994, Proc Natl Acad Sci USA 91: 12760–12764). However, Brassica napus oilseed may provide a better system for PHB production because acetyl-CoA, the substrate required in the first step of PHB biosynthesis, is prevalent during fatty acid biosynthesis. Three enzymatic activities are needed to synthesize PHB: a β-ketothiolase, an acetoacetyl-CoA reductase and a PHB synthase. Genes from the bacterium Ralstonia eutropha encoding these enzymes were independently engineered behind the seed-specific Lesquerella fendleri oleate 12-hydroxylase promoter in a modular fashion. The gene cassettes were sequentially transferred into a single, multi-gene vector which was used to transform B. napus. Poly(β-hydroxybutyrate) accumulated in leukoplasts to levels as high as 7.7% fresh seed weight of mature seeds. Electron-microscopy analyses indicated that leukoplasts from these plants were distorted, yet intact, and appeared to expand in response to polymer accumulation. Received: 26 May 1999 / Accepted: 16 June 1999     

Evaluation of the grazer–prey interaction as a biotechnological strategy to increase toxin production by dinoflagellate cultures in photobioreactors

In this paper, we extend an existing approach to biotechnologically assess grazer–prey interactions between the crustacean Artemia salina (grazer) and the toxic dinoflagellate Protoceratium reticulatum (prey). The applied strategy is presented as a bioprocessing tool for enhancing the production of toxins and bioactive compounds in dinoflagellate cultures. Interactions were based on direct and indirect contact between the grazer and the prey, as well as on the use of different extracts from A. salina cysts and supernatants from cultures in which A. salina had been grown. Several treatments were found to stimulate the growth and yessotoxin production of P. reticulatum mainly due to the action of dissolved excreted substances and/or metabolites released and/or extracted from A. salina. One of the best results was obtained with a culture medium formulation containing 10 % (v/v) supernatant from a culture of A. salina nauplii. This treatment was scaled up to a 15-L photobioreactor. The average maximum specific growth rate (μ _max) of P. reticulatum in this photobioreactor, operated in batch mode, increased by 27 %, whereas the maximum cell concentration (C _max) decreased by 20 % relative to the corresponding control culture. An average increase in yessotoxin production of 50 % with respect to the control culture was observed.     

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.     

Poly(β-L-malic acid) production by diverse phylogenetic clades of Aureobasidium pullulans

Poly(β-L-malic acid) (PMA) is a natural biopolyester that has pharmaceutical applications and other potential uses. In this study, we examined PMA production by 56 strains of the fungus Aureobasidium pullulans representing genetically diverse phylogenetic clades. Thirty-six strains were isolated from various locations in Iceland and Thailand. All strains from Iceland belonged to a newly recognized clade 13, while strains from Thailand were distributed among 8 other clades, including a novel clade 14. Thirty of these isolates, along with 26 previously described strains, were examined for PMA production in medium containing 5% glucose. Most strains produced at least 4 g PMA/L, and several strains in clades 9, 11, and 13 made 9–11 g PMA/L. Strains also produced both pullulan and heavy oil, but PMA isolated by differential precipitation in ethanol exhibited up to 72% purity with no more than 12% contamination by pullulan. The molecular weight of PMA from A. pullulans ranged from 5.1 to 7.9 kDa. Results indicate that certain genetic groups of A. pullulans are promising for the production of PMA.