Simple fed-batch cultivation strategy for the enhanced production of a single-sugar glucuronic acid-based oligosaccharides by a cellulose-producing <Emphasis Type="Italic">Gluconacetobacter hansenii</Emphasis> strain

The production of water-soluble single-sugar glucuronic acid-based oligosaccharides (WSOS) by a cellulose producing strain Gluconacetobacter hansenii PJK was studied in a periodically recycled and fed-batch cultivations using glucose/ethanol or glucose only. Fermentations were carried out in a 2 L jar fermenter equipped with a turbine impeller with 6 flat blades. WSOS were produced constantly but the bacterial cellulose (BC) production stopped at 48 h of cultivation in a periodically recycled culture using the exhausted medium supplemented with glucose and ethanol. Tremendous quantities of WSOS were obtained in fed-batch cultivations using glucose/ethanol (35.6 g/L at 132 h of cultivation) or glucose only (86 g/L after 240 h of cultivation) as the nutritional source. However, the BC production yield under these nutritional conditions decreased significantly in comparison to previous studies about the BC production by the same strain. The overall results revealed that G. hansenii is capable of producing enormous quantities of WSOS compared to those reported previously for compounds of a related chemical nature. Moreover, the WSOS production was found to be dependent on the pH of the culture broth.     

Effect of addition of water-soluble polysaccharides on bacterial cellulose production in a 50-L airlift reactor

Bacterial cellulose (BC) production was carried out in a batch cultivation of Acetobacter xylinum in a 50-L internal loop airlift reactor by addition of water-soluble polysaccharides into the medium. When 0.1% (w/w) agar was added, BC production reached 8.7 g/L compared with 6.3 g/L in the control, and duration of the cultivation period to reach the maximum concentration of BC was almost half of that without addition of polysaccharides. During cultivation, BC was formed into pellets whose size was smaller when the productivity of BC was higher, indicating that increase in the relative viscosity by addition of polysaccharides hindered formation of large clumps of BC and increase in the volumetric oxygen transfer coefficient at high flow rate led to increase in BC productivity.     

Role of water-soluble polysaccharides in bacterial cellulose production

Acetobacter xylinum BPR2001 produces water-insoluble bacterial cellulose (BC) and a water-soluble polysaccharide called acetan in corn steep liquor-fructose medium. Acetobacter xylinum EP1, which is incapable of acetan production was derived by disrupting the aceA gene of BPR2001. The BC production by EP1 (2.88 g/L) was lower than that by BPR2001 (4.6 g/L) in baffled-flask culture. When purified acetan or agar was added to the medium from the start of cultivation, the BC production by EP1 was enhanced and the final BC yield of EP1 was almost the same as that of BPR2001. A similar improvement of BC production by EP1 by the addition of agar was also confirmed by cultivation in a 50-L airlift reactor. From these results, the role of acetan in BC production is associated with the increase in the viscosity of the culture medium which may hinder coagulation of BC and cells in the culture, thereby accelerating the growth of BPR2001 and BC production by BPR2001.     

Bacterial cellulose production by fed-batch fermentation in molasses medium

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

Statistical optimization of culture conditions for bacterial cellulose production using Box-Behnken design

Culture conditions in a jar fermentor for bacterial cellulose (BC) production from A. xylinum BPR2001 were optimized by statistical analysis using Box-Behnken design. Response surface methodology was used to predict the levels of the factors, fructose (X1), corn steep liquor (CSL) (X2), dissolved oxygen (DO) (X3), and agar concentration (X4). Total 27 experimental runs by combination of each factor were carried out in a 10-L jar fermentor, and a three-dimensional response surface was generated to determine the effect of the factors and to find out the optimum concentration of each factor for maximum BC production and BC yield. The fructose and agar concentration highly influenced the BC production and BC yield. However, the optimum conditions according to changes in CSL and DO concentrations were predicted at almost central values of tested ranges. The predicted results showed that BC production was 14.3 g/L under the condition of 4.99% fructose, 2.85% CSL, 28.33% DO, and 0.38% agar concentration. On the other hand, BC yield was predicted in 0.34 g/g under the condition of 3.63% fructose, 2.90% CSL, 31.14% DO, and 0.42% agar concentration. Under optimized culture conditions, improvement of BC production and BC yield were experimentally confirmed, which increased 76% and 57%, respectively, compared to BC production and BC yield before optimizing the culture conditions.     

Continuous production of lignin peroxidase by Phanerochaete chrysosporium

Phanerochaete chrysosporium spores were immobilized both in agarose and agar gel beads, and used for the production of lignin peroxidase in repeated batch cultures on carbon-limited medium both with 0.5 g l⁻¹ glucose and without glucose. Veratryl alcohol was used as an activator of enzyme production. The biocatalyst was more stable in agarose gel with the maximum activity of 245 U l⁻¹ obtained in a 70 h batch. The biocatalyst could be used for at least 12 batches on the glucose medium with a gradual decrease in lignin peroxidase activity after the sixth batch. Further, mycelium pellets grown on carbon-limited medium were employed both in vertical and horizontal column reactors for the continuous production of lignin peroxidase. The bioreactor produced lignin peroxidase for at least 20 days in the horizontal system at 49 h residence time, with a maximum activity of 95 U l⁻¹.     

Biomass and lipid production of heterotrophic microalgae <Emphasis Type="Italic">Chlorella protothecoides</Emphasis> by using biodiesel-derived crude glycerol

Microalgal lipids may be a more sustainable biodiesel feedstock than crop oils. We have investigated the potential for using the crude glycerol as a carbon substrate. In batch mode, the biomass and lipid concentration of Chlorella protothecoides cultivated in a crude glycerol medium were, respectively, 23.5 and 14.6 g/l in a 6-day cultivation. In the fed-batch mode, the biomass and lipid concentration improved to 45.2 and 24.6 g/l after 8.2 days of cultivation, respectively. The maximum lipid productivity of 3 g/l day in the fed-batch mode was higher than that produced by batch cultivation. This work demonstrates the feasibility of crude biodiesel glycerol as an alternative carbon substrate to glucose for microalgal cultivation and a cost reduction of carbon substrate feed in microalgal lipid production may be expected.     

Improvement of Panax notoginseng cell culture for production of ginseng saponin and polysaccharide by high density cultivation in pneumatically agitated bioreactors

A Panax notoginseng cell culture was successfully scaled up from shake flask to 1.0-L bubble column reactor and concentric-tube airlift reactor. High-density bioreactor batch cultivation was carried out using a modified MS medium. The maximum cell density in batch cultures reached 20.1, 21.0 and 24.1 g/L in the shake flask, bubble column and airlift reactors, respectively, and their corresponding biomass productivity was 950, 1140 and 1350 mg/(L x d) for each. The productivity of ginseng saponin was 70, 96 and 99 mg/(L x d) in the flask, bubble column and airlift reactors, respectively; and the polysaccharide productivity reached 104, 119 and 151 mg/(L x d) for each. Furthermore, a fed-batch cultivation strategy was developed on the basis of specific oxygen uptake rate (SOUR), i.e., sucrose feeding before a sharp decrease of SOUR, and the highest cell density of 29.7 g/L was successfully achieved in the airlift bioreactor on day 17 with a very high biomass productivity of 1520 mg/(L x d). The concentrations of ginseng saponin and polysaccharide reached about 2.1 and 3.0 g/L, respectively, and their productivity was 106 (saponin) and 158 mg/(L x d) (polysaccharide). This work successfully demonstrated the high-density bioreactor cultivation of P. notoginseng cells in pneumatically agitated bioreactors and the reproduction of the shake flask culture results in bioreactors. The cell density, biomass productivity, production titer and productivity of both ginseng saponin and polysaccharide obtained here were the highest that have been reported on a reactor scale for all the ginseng species.     

Production of glycerol by immobilizedPichia farinosa

Summary Cells of the osmophilic yeastPichia farinosa were immobilized in sintered glass Raschig rings for the production of glycerol. The kinetics of production were observed under different conditions in batch, fed-batch and semicontinuous fermentations in fixed-bed column reactors and compared with those of free cells. 2.6 × 10⁹ cells/g sintered glass were adsorbed. The glycerol productivity amounted to 8.1 g/l per day. The highest concentration reached in batch culture was 86 g/l with immobilized cells. Fermentations using immobilized cells were accelerated compared to fermentations using free cells and maximum yield and productivity were reached at lower initial sugar concentrations. Using scanning electron microscopy it was observed that the shape of the cells was related to the sugar concentration in the medium. The experiments show thatP. farinosa produces glycerol with a high and constant productivity over long periods of time.     

Production of fructosyltransferase by <Emphasis Type="Italic">Aureobasidium</Emphasis> sp. ATCC 20524 in batch and two-step batch cultures

A comparison of fructosyltransferase (EC 2.4.1.9) production by Aureobasidium sp. ATCC 20524 in batch and two step batch cultures was investigated in a 1-l stirred tank reactor using a sucrose supply of 200 g/l. Results showed that the innovative cultivation in two step of Aureobasidium sp. produced more fructosyltransferase (FFase) than the single batch culture at the same sucrose concentration with a maximal enzyme production of 523 U/ml, which was 80.5% higher than the one obtained in the batch culture. The production of fructooligosaccharides (FOSs) was also analyzed; their concentration reached a maximum value of 160 g/l the first day in the two-step culture and 127 g/l in the single-batch mode. The use of the two-step batch culture with Aureobasidium sp. ATCC 20524 in allowing the microorganism to grow up prior to the induction of sucrose (second step), proved to be a powerful method for producing fructosyltransferase and FOSs.     

Bakers' yeast cultivation on by-products and wastes of potato and wheat starch production on a laboratory and pilot-plant scale

Saccharomyces cerevisiae was cultivated in a 10 litre laboratory stirred tank, an 80 litre laboratory airlift tower loop and a 4 m³ pilot-plant airlift tower loop reactor using by-products and wastes of potato and wheat starch production in batch and continuous cultures. Potato protein liquor, potato liquor retentate, potato liquor residue, and wheat process water were used as nutrients and glucose from the enzymatic conversion of potato starch as energy source. Besides the performance of the cultivation (cell concentrations, specific growth rates in the first (glucose) and second (ethanol) growth phases, productivities, yield coefficients), the qualities of the effluents (concentrations of phosphate, dissolved organic carbon, dissolved organic nitrogen, and chemical oxygen demand) were also determined in the different reactors as functions of the operational parameters. The optimal conditions were evaluated with regard to cultivation performance and effluent quality. These performances do not vary with the scale of the reactors. The performance of continuous cultures is considerably better than that of batch cultures.     

Physical properties of a single sugar α-linked glucuronic acid-based oligosaccharide produced by a Gluconacetobacter hansenii strain

To date, the physical properties including the morphology, thermal characteristics, and emulsifying activities of a single sugar α-linked glucuronic acid-based water-soluble oligosaccharides (WSOS) produced by Gluconacetobacter hansenii PJK have not been investigated or published elsewhere. Therefore, the current study was undertaken to investigate these important physical properties of WSOS. Field-emission scanning electron microscopy of the WSOS revealed a porous flake-type structure free from adhered bacterial cells. The degradation of the WSOS occurred by four well-differentiated steps with a maximum weight loss (∼40%) in a range of 230–300 °C. The pyrolysis temperature of the WSOS was found to be 278 °C with an enthalpy of 83.01 J/g. The emulsification ability of the WSOS increased initially with concentration, followed by a decrease, and finally became constant. The optimum concentration of WSOS for maximum emulsification (emulsifying ability) was 0.15% (w/v). The emulsions prepared with WSOS did not exhibit significant stability. The formation of oil and aqueous layers was initiated just after 2 min for emulsion prepared with 0.15% (w/v) WSOS, which completely separated after 24 h. It is concluded that WSOS has thermal stability comparable to other microbial polysaccharides. They have moderate emulsification properties, which may be due to the oligomeric nature of WSOS. Additionally the producer organism of WSOS is non-pathogenic. Therefore, the produced WSOS have potential applications in food and/or pharmaceutical preparations and as therapeutic agent in biomedical fields.     

A method for direct harvest of bacterial cellulose filaments during continuous cultivation of Acetobacter xylinum

Continuous filamentation of bacterial cellulose (BC) was successfully achieved by using shallow pan for the incubation to regulate thickness of the BC gel produced by Acetobacter xylinum. The BC filament was harvested and prepared directly by picking up BC pellicles, the thin BC gel, and winding slowly from the surface of the culture medium passed through a preliminary bactericidal washing bath. The X-ray diffraction analysis and scanning electron microscopic observation of the BC filament thus obtained showed that the filament was smooth and the fairly good orientation of BC molecules.

The average tensile strength was 4.4 g denier⁻¹ for the filament prepared by hot alkaline treatment and subsequent washing with distilled water and dried under tension (Filament W): 3.4 g denier⁻¹ for washing with 10% aqueous ethylene glycol after alkaline treatment followed by drying under tension (Filament E) and 2.4 g denier⁻¹ for the treatment with 10% ethylene glycol after normal water-washing followed by drying under tension.     

The structure and physical properties of glucuronic acid oligomers produced by a Gluconacetobacter hansenii strain using the waste from beer fermentation broth

The aim of this work was to study the chemical structure and physical properties of water-soluble oligosaccharides (WSOS) produced by Gluconacetobacter hansenii PJK using the waste from beer fermentation broth as a basal medium. The analysis of the hydrolyzed products and the spectroscopic studies of the native WSOS showed that it is a mixture of oligomers all having a single sugar -linked glucuronic acid as building blocks with an O-acetyl and O-methyl group, in the terminal unit of the non-reducing end. The thermal studies displayed a progressive degradation of WSOS without a major weight loss throughout a range of temperatures. The melting point and pyrolysis temperature were found to be 130.16 and 275.25 °C, respectively. The optimum concentration of WSOS for a maximum emulsifying ability was found to be 0.10% (w/v). The resulting emulsions, however, did not demonstrate a noteworthy stability.     

补料培养与溶氧控制联合应用对红豆杉细胞培养的影响

为进一步提高红豆杉 (Taxuschinensis (Pilg.)Rehd .)细胞培养过程中紫杉醇的产量 ,采用细胞悬浮培养方法研究了补料培养与溶氧控制联合应用对紫杉醇产量的影响。 5L反应器中补料培养研究表明 ,培养过程中第 16天添加含 2 0g/L蔗糖的补料培养液有利于细胞的生长及紫杉醇的合成。 2 0L反应器中补料培养的研究结果表明 :2 0 %饱和度培养时紫杉醇含量最高 (0 .98mg/gDW) ,但 4 0 %～ 6 0 %溶氧饱和度能提高紫杉醇的产量。进一步研究表明 ,细胞在 6 0 %溶氧饱和度培养 2 0d后转入 2 0 %溶氧饱和度继续培养 12d ,能显著提高紫杉醇产量。补料培养与溶氧控制联合应用时 ,2 0L反应器中红豆杉细胞培养紫杉醇产量可达 18.7mg/L。     

Bacterial cellulose production by Acetobacter xylinum in a 50-L internal-loop airlift reactor

Bacterial cellulose (BC) production was realized in a batch cultivation of Acetobacter xylinum subsp. sucrofermentans BPR2001 in a 50-L internal-loop airlift reactor. When the bacterium was cultivated with air supply, 3.8 g/L of BC was produced after 67 hours. When oxygen-enriched gas was supplied, the concentration of BC was doubled and the production rate of BC was 0.116 g/L. h, which was two times higher than that of air-supplied culture and comparable to that in a mechanically agitated stirred-tank fermentor. Bacterial cellulose produced by the airlift reactor formed a unique ellipse pellet (BC pellet), different from the fibrous form which was produced in an agitated stirred-tank fermentor. The BC-pellet suspension was demonstrated to have a higher volumetric oxygen transfer coefficient than the fibrous BC suspension in a 50-L internal-loop airlift reactor. The mixing time of BC-pellet suspension in the airlift reactor was also shorter than that in water.     

Enhancement of Fermentative Hydrogen Production in an Extreme-Thermophilic (70°C) Mixed-Culture Environment by Repeated Batch Cultivation

Repeated batch cultivation was applied to enrich hydrogen fermentative microflora under extreme-thermophilic (70°C) environment. Initial inoculums received from a hydrogen producing reactor fed with organic fraction of household solid wastes. In total seven transfers was conducted and maximum hydrogen yield reached 296 ml H₂/g (2.38 mol/mol) glucose and 252 ml H₂/g (2.03 mol/mol) for 1 and 2 g/l glucose medium, respectively. It was found that hydrogen production was firstly decreased and got increased gradually from third generation. Acetate was found to be the main metabolic by-product in all batch cultivation. Furthermore, the diversity of bacterial community got decreased after repeated batch cultivation. It was proved that repeated batch cultivation was a good method to enhance the hydrogen production by enriching the mixed cultures of dominant species.     

Quantitative characterization of metabolism and metabolic shifts during growth of the new human cell line AGE1.HN using time resolved metabolic flux analysis

For the improved production of vaccines and therapeutic proteins, a detailed understanding of the metabolic dynamics during batch or fed-batch production is requested. To study the new human cell line AGE1.HN, a flexible metabolic flux analysis method was developed that is considering dynamic changes in growth and metabolism during cultivation. This method comprises analysis of formation of cellular components as well as conversion of major substrates and products, spline fitting of dynamic data and flux estimation using metabolite balancing. During batch cultivation of AGE1.HN three distinct phases were observed, an initial one with consumption of pyruvate and high glycolytic activity, a second characterized by a highly efficient metabolism with very little energy spilling waste production and a third with glutamine limitation and decreasing viability. Main events triggering changes in cellular metabolism were depletion of pyruvate and glutamine. Potential targets for the improvement identified from the analysis are (i) reduction of overflow metabolism in the beginning of cultivation, e.g. accomplished by reduction of pyruvate content in the medium and (ii) prolongation of phase 2 with its highly efficient energy metabolism applying e.g. specific feeding strategies. The method presented allows fast and reliable metabolic flux analysis during the development of producer cells and production processes from microtiter plate to large scale reactors with moderate analytical and computational effort. It seems well suited to guide media optimization and genetic engineering of producing cell lines.     

Maximum virginiamycin production by optimization of cultivation conditions in batch culture with autoregulator addition

A strategy for optimization of non-growth-associated production in batch culture employing an empirical approach was developed through the study of virginiamycin production. The strategy is formulated with two aims: attaining a high cell concentration at the beginning of the production phase without decrease in production activity; and enhancing the production activity during the production phase. As a practical example, the goal of a maximum virginiamycin (M and S) production in the batch culture of Streptomyces virginiae was set. To attain a high cell concentration in the production phase of the batch culture, that is, to extend the growth phase for as long as possible, the optimum composition and concentration of the complex medium, especially the yeast extract (YE) concentration, were first investigated. Dissolved oxygen (DO) concentration control was also a parameter considered in maintaining the production activity during the production phase. In addition, to enhance the production activity, an optimum addition strategy of an autoregulator, virginiae butanolide-C (VB-C), was investigated. Combining these measures, the optimum cultivation conditions were found to be an initial YE concentration in the complex medium of 45 g/L, the shot addition of 300 mug/L of VB-C 11.5 h after the start of the batch culture, and a DO concentration maintained above 2 mg/L. The maximum concentrations of virginiamycin M and S were about ninefold those obtained under nonoptimum cultivation conditions. Nonoptimum cultivation conditions consisted of an initial YE concentration one sixth (7.5 g/L) that of the optimum cultivation conditions, and no VB-C addition. These conditions were used as representative of the standard cultivation of virginiamycin in this study. The strategy developed here will be applicable to the production of other antibiotics, especially to the cultivation of Streptomyces species, in which a hormonelike signal material (an autoregulator) plays an important role in antibiotic production. (c) 1996 John Wiley & Sons, Inc.     

Strategies for the production of lipase by Candida rugosa; neural estimation of biomass and lipase activity

Summary Various strategies for the production of lipase by Candida rugosa Diddens and Lodder (ATCC 14830) in stirred tank reactors were investigated. The strain was first screened for lipase production with agar plate assay based on the fluorescent dye Rhodamine B, followed by adaptation to the production medium used. The highest lipase activity of 7.6 U/ml was obtained on a medium containing 40 g olive oil/l and 1 g glucose/l, with supplying pure oxygen. Neural networks were used in the estimation of biomass and lipase activity.