Growth of transformed roots in a nutrient mist bioreactor: reactor performance and evaluation

Summary A nutrient mist bioreactor was modified for culturing transformed roots of Beta vulgaris and Carthamus tinctorius on a nylon support. Culture conditions of misting cycle, inoculum size, batch or continuous operation and sucrose concentration were varied in order to maximize growth over a 1-week period. Root tissue cultured in nutrient mists in a 1.8-1 culture chamber achieved levels of growth equivalent to hairy roots cultured in shake flasks with identical medium. Our results demonstrate the effectiveness of nutrient mist culture as applied to hairy roots, thereby providing an alternative means for successful culture of these tissues. Correspondence to: A. A. DiIorio     

Production of carbonyl reductase by Metschnikowia koreensis

A new strain of the yeast Metschnikowia koreensis was grown in shake flasks and a stirred bioreactor for the production of carbonyl reductase. The optimal conditions in the bioreactor for maximizing the biomass specific activity of the enzyme were found to be: a medium composed of glucose (20 g/L), peptone (5 g/L), yeast extract (5 g/L) and zinc sulfate (0.3g/L); the pH controlled at 7; the temperature controlled at 25 °C; an agitation speed of 500 rpm; and an aeration rate of 0.25 vvm. In the bioreactor, a biomass specific enzyme activity of 115.6 U/gDCW was obtained and the maximum biomass concentration was 15.3 gDCW/L. The biomass specific enzyme activity obtained in the optimized bioreactor culture was 11-fold higher than the best result achieved in shake flasks. The bioreactor culture afforded a 2.7-fold higher biomass concentration than could be attained in shake flasks.     

Effect of bioreactor configuration on the growth and maturation of Picea sitchensis somatic embryo cultures

Somatic embryo suspension cultures of Picea sitchensis (Sitka spruce) derived from two cell lines, SS03 and SS10, were grown in shake flasks, air-lift, bubble, stirred tank and hanging stirrer bar bioreactors. Cell line SS03 yielded freely suspended and individual stage 1 embryos, while the embryos of SS10 were present in large aggregates. Compared to shake flasks, proliferation in bioreactors resulted in increased biomass; however, cell line morphology influenced the effect of different bioreactor configurations on growth and maturation of embryo cultures. Somatic embryos grown in shake flasks and bioreactors were matured on gelled solid medium and in submerged culture where gelled solid medium was covered with a layer of liquid medium. The number of stage 3 (mature) embryos produced from SS03 in the bubble bioreactor was significantly higher than those from stirred tank and hanging stirrer bar bioreactors with both solid medium and submerged culture. Submerged culture was unsuitable for SS10 embryo maturation. This revised version was published online in June 2006 with corrections to the Cover Date.     

Biomass production of hairy roots of Artemisia annua and Arachis hypogaea in a scaled‐up mist bioreactor

Hairy roots have the potential to produce a variety of valuable small and large molecules. The mist reactor is a gas phase bioreactor that has shown promise for low‐cost culture of hairy roots. Using a newer, disposable culture bag, mist reactor performance was studied with two species, Artemisia annua L. and Arachis hypogaea (peanut), at scales from 1 to 20 L. Both species of hairy roots when grown at 1 L in the mist reactor showed growth rates that surpassed that in shake flasks. From the information gleaned at 1 L, Arachis was scaled further to 4 and then 20 L. Misting duty cycle, culture medium flow rate, and timing of when flow rate was increased were varied. In a mist reactor increasing the misting cycle or increasing the medium flow rate are the two alternatives for increased delivery of liquid nutrients to the root bed. Longer misting cycles beyond 2–3 min were generally deemed detrimental to growth. On the other hand, increasing the medium flow rate to the sonic nozzle especially during the exponential phase of root growth (weeks 2–3) was the most important factor for increasing growth rates and biomass yields in the 20 L reactors. A. hypogaea growth in 1 L reactors was µ = 0.173 day^?1 with biomass yield of 12.75 g DW L^?1. This exceeded that in shake flasks at µ = 0.166 day^?1 and 11.10 g DW L^?1. Best growth rate and biomass yield at 20 L was µ = 0.147 and 7.77 g DW L^?1, which was mainly achieved when medium flow rate delivery was increased. The mist deposition model was further evaluated using this newer reactor design and when the apparent thickness of roots (+hairs) was taken into account, the empirical data correlated with model predictions. Together these results establish the most important conditions to explore for future optimization of the mist bioreactor for culture of hairy roots. Biotechnol. Bioeng. 2010;107: 802–813. © 2010 Wiley Periodicals, Inc.     

Production of monoclonal antibodies by tobacco hairy roots

Hairy roots of tobacco (Nicotiana tabacum) were used to produce full-length murine lgG(1) monoclonal antibody. The presence of heavy (gamma) and light (kappa) chains and fully assembled antibody was verified by Western blot analysis of root extracts. Antibody levels in the biomass and medium were quantified by ELISA based on detection of gamma-kappa complexes. Antibody produced by hairy roots was fully functional as demonstrated in bacterial aggregation assays which confirmed bivalent antigen-binding capacity. Eight antibody-producing hairy root clones retained their ability to produce mouse immunoglobulin over a period of 19 months after transformation with Agrobacterium rhizogenes. For hairy roots grown in Gamborg's B5 medium, the maximum level of assembled antibody after 21-day culture in shake flasks was 18 mg L(-1) or 1.8% total soluble protein; up to 14% of the antibody was secreted into the medium. Antibody production by transgenic hairy roots had a negligible effect on growth compared with hairy roots of wild-type tobacco. Antibody accumulation was growth associated with constant specific accumulation rate at the beginning of the culture; however, degradation of antibody was significant after 14 days and the amount of assembled antibody declined. Unlike hybridoma cultures, the time course of antibody accumulation by hairy roots showed a distinctive maximum very soon after the end of exponential growth. Total antibody levels were increased by addition of nitrate, polyvinylpyrrolidone, or gelatin to the medium. Polyvinylpyrrolidone and gelatin also markedly improved extracellular antibody concentrations; with these treatments, up to 43% of the antibody present was secreted into the medium. Antibody production was tested using hairy roots grown in an air-driven bioreactor. The intracellular antibody content after 30-day bioreactor culture was similar to that measured in shake flasks; however, the final extracellular antibody level was 1.7 times higher than the maximum measured in shake flasks. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 401-415, 1997.     

Modeling of growth and laccase production by Pycnoporus sanguineus

Production of extracellular laccase by the white-rot fungus Pycnoporus sanguineus was examined in batch submerged cultures in shake flasks, baffled shake flasks and a stirred tank bioreactor. The biomass growth in the various culture systems closely followed a logistic growth model. The production of laccase followed a Luedeking-Piret model. A modified Luedeking-Piret model incorporating logistic growth effectively described the consumption of glucose. Biomass productivity, enzyme productivity and substrate consumption were enhanced in baffled shake flasks relative to the cases for the conventional shake flasks. This was associated with improved oxygen transfer in the presence of the baffles. The best results were obtained in the stirred tank bioreactor. At 28 °C, pH 4.5, an agitation speed of 600 rpm and a dissolved oxygen concentration of ~25 % of air saturation, the laccase productivity in the bioreactor exceeded 19 U L^?1 days^?1, or 1.5-fold better than the best case for the baffled shake flask. The final concentration of the enzyme was about 325 U L^?1.     

Methyl jasmonate effect on diterpenoid accumulation in Salvia sclarea hairy root culture in shake flasks and sprinkle bioreactor

Hairy root cultures of Salvia sclarea were grown in shake flasks and 10 L nutrient sprinkle bioreactor, running for 30 days and the effects of methyl jasmonate (MJ) on their growth and capacity to accumulate diterpenoids were measured. We found that MJ concentration and exposure time to the elicitor were factors that strongly affected the diterpenoid production. The highest diterpenoid accumulation (67.5 ± 7.1 mg g⁻¹ dry weight, calculated as a sum of ferruginol, salvipisone, aethiopinone and 1-oxoaethiopinone) without reduction of biomass, was achieved when the 23-day-old hairy roots in bioreactor culture were exposed to 125 μM MJ for 7 days. The roots produced 9 and 3.8 times as much aethiopinone (40 ± 5.9 mg g⁻¹ dry weight) and salvipisone (12.6 ± 0.4 mg g⁻¹ dry weight), respectively, as roots cultured in shake flasks. Our results imply that cultivation of S. sclarea hairy roots in sprinkle bioreactor after elicitation with MJ may be valuable to enhance production of the bioactive diterpenoids.     

Bioproduction of phenylethanoid glycosides by plant cell culture of Scrophularia striata Boiss.: from shake-flasks to bioreactor

Phenylethanoid glycosides (PeG) are a class of polyphenols found in some plants that have pharmaceutical effects as anti-inflammatories and anti-oxidants. The presence of PeG (acteoside) in the aerial parts of Scrophularia striata Boiss. has been demonstrated. Considerable progress has been made using plant cell cultures to stimulate formation and accumulation of secondary metabolites. The present study optimized phenylethanoid production from shake flasks to bioreactor using a cell culture of S. striata. The optimal conditions for production of cell biomass by scale-up to a bioreactor were determined to be a pH of 4.8, air flow rate of 0.5–1.5 l min⁻¹, and mixing speed of 110–170 rpm at 25 ± 1 °C in darkness. Growth parameters and PeG production were measured and compared with the results from the shake flasks. The results showed that cell biomass was high in the bioreactor (15.64 g l⁻¹ DW) and in the shake flasks (14.16 g l⁻¹ DW). The acteoside content in the bioreactor was 1404.20 μg g⁻¹ DW, which is threefold higher than in the shake flasks (459.71 μg g⁻¹ DW). The echinacoside concentration in the bioreactor was 1449.39 μg g⁻¹, 1.36-fold lower than in the shake flasks (1973.03 μg g⁻¹ DW). This study established an efficient way for production of acteoside, the major PeG, in a bioreactor.

     

The production and antiprotozoal activity of abietane diterpenes in Salvia austriaca hairy roots grown in shake flasks and bioreactor

The biomass and concentration of bioactive quinone methide-type diterpenes in hairy roots of Salvia austriaca were determined and compared with levels of these metabolites in roots of field-grown plants. The cultures were maintained in shake flasks and a nutrient sprinkle bioreactor. Diterpene production was more efficient in the shake flask root culture than the bioreactor one. Biomass and diterpene production within the shake flask culture was evaluated using Schenk and Hildebrandt (SH), Gamborg (B5), and woody plant medium (WPM), with both full- and half-strength macro and micronutrient concentrations (1/2 SH, 1/2 B5, and 1/2 WPM). Among the tested media, SH medium proved to be most effective for biomass and diterpene production. In this medium, the transformed roots accumulated the levels of taxodone (3.89?mg?g^?1 DW; equivalent to 63.3?mg?L^?1), taxodione (1.15?mg?g^?1 DW; equivalent to 17.4?mg?L^?1), 15-deoxy-fuerstione (2.15?mg?g^?1 DW; equivalent to 32.5?mg?L^?1), and 7-(2′-oxohexyl)-taxodione (0.076?mg?g^?1 DW; equivalent to 1.1?mg?L^?1). Three diterpenes were also detected in the roots of S. austriaca intact plants, but their concentrations were lower than those in hairy root culture. No 7-(2′-oxohexyl)-taxodione was found in the roots of field-grown plants. The hairy roots were able to maintain high metabolite levels even for 6 years of cultivation. Taxodone, taxodione, 15-deoxy-fuerstione, and 7-(2′-oxohexyl)-taxodione were tested for in vitro activity against Trypanosoma brucei rhodesiense, T. cruzi, and Plasmodium falciparum and their cytotoxicity was determined using L6 cells. Among these compounds, taxodione was the most active against T. brucei rhodesiense [IC₅₀?=?0.05?µM with high selectivity, selectivity index (SI)?=?38]. Taxodione was found to inhibit the growth of P. falciparum and T. cruzi by 50% at respective concentrations of 1.9 and 7.1?µM (SI values of 1.0 and 0.27). Other diterpenoids demonstrated weaker activity against tested parasites (IC₅₀ values ranging from 0.62 to 194.7?µM) and lower selectivity (SI value ranged from 0.4 to 5.0).     

Ajmalicine production by cell cultures of Catharanthus roseus: from shake flask to bioreactor

The productivity of a cell culture for the production of a secondary metabolite is defined by three factors: specific growth rate, specific product formation rate, and biomass concentration during production. The effect of scaling-up from shake flask to bioreactor on growth and production and the effect of increasing the biomass concentration were investigated for the production of ajmalicine by Catharanthus roseus cell suspensions. Growth of biomass was not affected by the type of culture vessel. Growth, carbohydrate storage, glucose and oxygen consumption, and the carbon dioxide production could be predicted rather well by a structured model with the internal phosphate and the external glucose concentration as the controlling factors. The production of ajmalicine on production medium in a shake flask was not reproduced in a bioreactor. The production could be restored by creating a gas regime in the bioreactor comparable to that in a shake flask. Increasing the biomass concentration both in a shake flask and in a stirred fermenter decreased the ajmalicine production rate. This effect could be removed partly by controlling the oxygen concentration in the more dense culture at 85% air saturation.     

Biomass segregation in sage cell suspension culture

The biomass of sage (Salvia officinalis L.) cell suspension culture was composed of single cells and cell aggregates. The development of aggregated cell culture from a single-cell suspension was monitored by particle size distribution for four particle size classes. Particle size distribution was compared between the biomass grown in bioreactor and shake flasks. The size of the particles had a strong influence on content of secondary metabolite, ursolic acid (UA). The single cell biomass fraction accumulated up to 7.7 mg UA g^–1 DW which was up to 50 times higher compared to aggregated biomass fractions.     

Production of podophyllotoxin using cross-species coculture of Linum flavum hairy roots and Podophyllum hexandrum cell suspensions

Novel cross-species coculture systems using Linum flavum hairy roots and Podophyllum hexandrum cell suspensions were applied for in vitro production of podophyllotoxin. The hairy roots and suspensions were cocultured in Linsmaier and Skoog medium in dual shake flasks and dual bioreactors. In separate experiments, coniferin feeding was shown to be an effective strategy for increasing the accumulation of podophyllotoxin in P. hexandrum suspensions. Because roots of L. flavum are a natural source of coniferin, hairy roots of this species were used in coculture with P. hexandrum to provide an in situ supply of coniferin. Compared with P. hexandrum suspensions cultured alone in shake flasks or bioreactors, podophyllotoxin concentrations in cocultured P. hexandrum cells were increased by 240% and 72% in dual shake flask and dual bioreactor systems, respectively. The availability and stability of coniferin in the medium are the most likely factors limiting podophyllotoxin synthesis in coculture. Intensification of the coculture process is required to further improve total podophyllotoxin accumulation on a volumetric basis.     

A shaken disposable bioreactor system for controlled insect cell cultivations at milliliter‐scale

While wave‐mixed and stirred bag bioreactors are common devices for rapid, safe insect cell culture‐based production at liter‐scale, orbitally shaken disposable flasks are mainly used for screening studies at milliliter‐scale. In contrast to the two aforementioned bag bioreactor types, which can be operated with standard or disposable sensors, shaker flasks have not been instrumented until recently. The combination of 250 mL disposable shake flasks with PreSens's Shake Flask Reader enables both pH and dissolved oxygen to be measured, as well as allowing characterization of oxygen mass transfer. Volumetric oxygen transfer coefficients (k_La‐values) for PreSens 250 mL disposable shake flasks, which were determined for the first time in insect cell culture medium at varying culture volumes and shaker frequencies, ranged between 4.4 and 37.9/h. Moreover, it was demonstrated that online monitoring of dissolved oxygen in shake flasks is relevant for limitation‐free growth of insect cells up to high cell densities in batch mode (1.6×10⁷ cells/mL) and for the efficient expression of an intracellular model protein.     

Development of a nontoxic acoustic window nutrient-mist bioreactor and relevant growth data

Summary A nutrient-mist bioreactor was designed that separates the nutrient medium from the electronic components via an acoustic window. This eliminates compromising culture sterility when repairing mechanical failures common with commercially available mist reactors. The experimental mist bioreactor is low cost and can be assembled in any laboratory. Toxicity tests of several potential acoustically transparent materials are included. Details of the construction procedures include methods for casting the window. Growth data using the newly designed nutrient mist bioreactor are compared to data from a commercial mist reactor, shake flasks, and Gelrite cultures.Artemisia annua hairy roots andNephrolepis exaltata shoot cultures showed growth comparable to the conventional tissue culture methods.     

Yield enhancement strategies for the production of picroliv from hairy root culture of Picrorhiza kurroa Royle ex Benth.

Fast-growing hairy root cultures of Picrorhiza kurroa induced by Agrobacterium rhizogenes offers a potential production system for iridoid glycosides. In present study we have investigated the effects of various nutrient medium formulations viz B5, MS, WP and NN, and sucrose concentrations (1–8%) on the biomass and glycoside production of selected clone (14-P) of P. kurroa hairy root. Full strength B5 medium was found to be most suitable for maximum biomass yield on the 40th day of culture (GI = 32.72 ± 0.44) followed by the NN medium of the same strength (GI = 22.9 ± 0.43). Secondary metabolite production was 1.1 and 1.3 times higher in half strength B5 medium respectively in comparison to MS medium. Maximum biomass accumulation along with the maximum picroliv content was achieved with 4% sucrose concentration in basal medium. RT vitamin and Thiamine-HCl effected the growth and secondary metabolite production of hairy roots growing on MS medium but did not show any effect on other media. The pH of the medium played significant role in growth and secondary metabolite production and was found to be highest at pH 6.0 while lowest at pH 3.0 and pH 8.0. To enhance the production of biomass and Picroliv 5 liter working capacity bioreactor was used, 27-fold (324 g FW) higher growth was observed in bioreactor than shake flask and secondary metabolite production was similarly enhanced.     

Comparison of Cell Growth and Alkaloid Production of Catharanthus roseus Cells Cultured in Shake Flask and in Bioreactor

The cell growth and alkaloid production of Catharanthus roseus (L.) G. Don cells cultured in the shake flasks with different volumes and in the stirred tank bioreactor (10 L) were compared. Cell dry weight and alkaloid production showed no significant difference in the small volume scale-up shake flasks. When more broths were added to a certain volume in the shake flask, both cell weight and alkaloid production were decreased. The maximum cell dry weight was similar between the cell cultures in the shake flask and the bioreactor, but the alkaloid production of cells was much less in the bioreactor. Gas regime and shear stress were recognized to be the main factors contributing the important effect on alkaloid production during the scale-up processes.     

Improved guggulsterone production from sugars, precursors, and morphactin in cell cultures of Commiphora wightii grown in shake flasks and a bioreactor

Cell cultures of Commiphora wightii (Arnott.) Bhandari were grown in shake flasks and a bioreactor and an increase in guggulsterone accumulation up to 18 μg l⁻¹ was recorded in cells grown in the production medium containing a combination of sucrose:glucose (4% total), precursors (phenylalanine, pyruvic acid, xylose, and sodium acetate), morphactin, and 2iP. A yield of 10 g l⁻¹ biomass and ∼200 μg l⁻¹ guggulsterone was recorded in a 3-l flask and in a 2-l stirred tank bioreactor compared with 6.6 g biomass and 67 μg l⁻¹ guggulsterone in 250-ml flasks. Increased vessel size was correlated with increased biomass and guggulsterone accumulation. 2iP alone was not effective for biomass and guggulsterone accumulation in cell cultures of C. wightii.     

Nitrogen and phosphorus as the factors affecting ginsenoside production in hairy root cultures of <Emphasis Type="Italic">Panax quinquefolium</Emphasis> cultivated in shake flasks and nutrient sprinkle bioreactor

The study assesses the influence of different concentrations of nitrogen and phosphorus sources on ginsenoside biosynthesis in Panax quinquefolium hairy roots cultivated in shake flasks and a nutrient sprinkle bioreactor. The saponin content was determined using HPLC. The maximum yield (12.45 mg g^?1 dw) of the sum of six examined ginsenosides (Rb1, Rb2, Rc, Rd, Re and Rg1) in hairy roots cultivated in shake flasks was achieved in modified Gamborg B-5 medium containing 0.83 mM l^?1 phosphate, 12.4 mM l^?1 nitrate and 0.5 mM l^?1 ammonium. The yield itself was 1.93 times higher than that achieved in standard Gamborg medium. The modified medium also favourably influenced the biosynthesis of studied saponins in bioreactor cultures. The saponin content (35.11 mg g^?1 d.w.) was 2.75-times higher than that achieved in control medium.     

Experimental design and metabolic flux analysis tools to optimize industrially relevant Haemophilus influenzae type b growth medium

Haemophilus influenzae type b (Hib), a Gram‐negative capsulated bacterium, is a causative agent of meningitis worldwide. The capsular polysaccharide, a high molecular mass polymer consisting of the repeated units of the polyribosyl‐ribitol‐phosphate, is considered the main virulence factor and it is used as an antigen to vaccines, conjugated to a carrier protein. The industrial production of the polysaccharide requires the cultivation of Hib in rich medium, which impacts process costs and product recovery. In this study, a central composite rotational experimental design strategy was used to access the influence of key components of culture medium (soy peptone, yeast extract and glucose) on biomass formation and polysaccharide production in shake‐flasks. The optimized medium formulation, containing half of the usual yeast extract and soytone concentrations, was further validated in batch bioreactor cultivations. High polysaccharide production (～500 mg/L) was obtained in a cheaper and more competitive production process for use in Hib vaccine production. In addition, simulations of a metabolic model describing Hib central metabolism were used to assess the role of key amino acids on growth. A chemically defined medium supplemented only with amino acids from α‐ketoglutarate and oxaloacetate families as well as phenylalanine was suggested as a promising alternative for reduced acetate accumulation and enhanced polysaccharide production in Hib cultures. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1508–1519, 2017