Azadirachtin production in stirred tank reactors by Azadirachta indica suspension culture

Successful scale-up of Azadirachta indica suspension culture for azadirachtin production was done in stirred tank bioreactor with two different impellers. The kinetics of biomass accumulation, nutrient consumption and azadirachtin production of A. indica cell suspension culture were studied in a stirred tank bioreactor equipped with centrifugal impeller and compared with similar bioreactor with a setric impeller to investigate the role of O₂ transfer efficiency of centrifugal impeller bioreactor on overall culture metabolism. The maximum cell mass for centrifugal impeller bioreactor and stirred tank bioreactor (with setric impeller) were 18.7 and 15.5 g/L (by dry cell weight) and corresponding azadirachtin concentrations were 0.071 and 0.05 g/L, respectively. Glucose and phosphate were identified as the major growth-limiting nutrients during the bioreactor cultivation. The centrifugal impeller bioreactor demonstrated less shearing and improved O₂ transfer than the stirred tank bioreactor equipped with setric impeller with respect to biomass and azadirachtin production.     

Transformed root cultures for biotechnology

This review is concerned with the application of hairy roots, i.e. plant roots formed from plant cells after transformation by Agrobacterium rhizogenes for the production of bioactive compounds. Transformed root cultures have been established from numerous species of dicotyledonous plants. The plants, as well as the main products accumulated in hairy root cultures derived from these plants, are listed in this paper. Data are presented on novel compounds, hitherto detected only in transformed roots but not occurring in the corresponding intact plants. The possible use of hairy root cultures for the over-production of secondary metabolites and biotransformation of chemicals is discussed. In order to enhance the productivity of hairy root cultures, various methods have been derived, and optimized procedures are proposed. They include selection of high-producing clones, elicitation, composition of growth media, culture conditions and genetic approach. Hairy roots usually store secondary metabolites in vacuoles inside the cells. Therefore, several methods have been used to increase the amount of products released into the medium. Unfortunately, no general procedure is known that works in all cases, and the excretion behaviour of hairy root cultures varies from one species to another and even within one species from one clone to another. Special attention is given to the cultivation methods and bioreactor systems for hairy root cultures. Hairy roots are cultivated usually in shake flasks; however, shake flask culture is not suitable for the complex optimization and continuous control of the culture conditions. In this paper, we are going to present bioreactors proposed for the cultivation of hairy roots under more or less controlled conditions. Modifications of typical bacterial bioreactors, i.e. stirred tanks, airlift loop reactors and other constructions, are presented. A very special type of bioreactor providing good conditions for loose root mass multiplication without oxygen or substrate limitations, is the mist bioreactor. Nowadays, it is practically impossible to select the one best bioreactor type for hairy root culture.     

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).     

Fed-batch hairy root cultures within situ separation

Fed-batch cultures ofL. erythrorhizon hairy root were carried out by controlling sucrose concentration and media conductivity in a shake flask and a modified stirred tank reactor. For the efficient product recovery from the culture,in situ adsorption by XAD-2 was also conducted. When sucrose was used as a carbon source, the highest shikonin production and hairy root growth were obtained. When glucose or fructose was used instead, the growth was severely inhibited. In addition, it was found that alternating feeding of sucrose could be used as an effective strategy for enhancing the productivity of shikonin derivatives., As the XAD-2 amount was increased up to 1.5 g/L, shikonin production was enhanced by removing shikonin produced and other products which might be inhibitory to cell growth. Most amount of shikonin produced was successfully recovered in XAD-2 (Over 99%). Using hairy root culture in a modified stirred tank reactor, the shikonin productivity and hairy root growth rate on the average were 9.34 mg/L day and 0.49 g DCW/L · day, respectively.     

Short Communication: Effect of agitation rate on the growth and production of xylanase free of cellulase by Thermomyces lanuginosus MH4 in bioreactor

Cellulase-free xylanase production by T. lanuginosus MH4 was investigated in a 3-litre stirred tank bioreactor under different agitation rates and an aeration rate of 1v/v/m. The cultivation time in the bioreactor was reduced significantly over that in shake culture conditions. A xylanase productivity of 0.1 mkat1–1h–1 was achieved on xylan in the bioreactor. This was nearly double to that obtained in shake culture. The agitation rates influenced both growth and enzyme secretion in the bioreactor. The highest level of biomass concentration and activities of both xylanase and -xylosidase were obtained at 150 revmin–1     

Statistical medium optimization for enhanced azadirachtin production in hairy root culture of Azadirachta indica

Azadirachtin, a well-known biopesticide, is a secondary metabolite extracted from the seeds of Azadirachta indica. In the present study, azadirachtin was produced in hairy roots of A. indica, generated by Agrobacterium rhizogenes-mediated transformation of leaf explants. Liquid cultures of A. indica hairy roots were developed with a liquid-to-flask volume ratio of 0.15. The kinetics of growth and azadirachtin production were established in a basal plant growth medium containing MS medium major and minor salts, Gamborg’s medium vitamins, and 30 g l⁻¹ sucrose. The highest azadirachtin accumulation in the hairy roots (up to 3.3 mg g⁻¹) and azadirachtin production (∼44 mg l⁻¹) was obtained on Day 25 of the growth cycle, with a biomass production of 13.3 g l⁻¹ dry weight. To enhance the production of azadirachtin, a Plackett–Burman experimental design protocol was used to identify key medium nutrients and concentrations to support high root biomass production and azadirachtin accumulation in hairy roots. The optimal nutrients and concentrations were as follows: 40 g l⁻¹ sucrose, 0.19 g l⁻¹ potassium dihydrogen phosphate, 3.1 g l⁻¹ potassium nitrate, and 0.41 g l⁻¹ magnesium sulfate. Concentrations were determined by a central composite design protocol and verified in shake-flask cultivation. The optimized medium composition yielded a root biomass production of 14.2 g l⁻¹ and azadirachtin accumulation of 5.2 mg g⁻¹, which was equivalent to an overall azadirachtin production of 73.84 mg l⁻¹, 68% more than that obtained under non-optimized conditions.     

Performance of hairy root cultures of Cichorium intybus L. In bioreactors of different configurations

Summary A transformed root culture of Cichorium intybus L. cv. Lucknow Local grown in different configurations of bioreactors was examined. The roots grown in an acoustic mist bioreactor showed the best performance in terms of increased specific growth rate (0.072d⁻¹) and esculin content (18.5gl⁻¹), the latter of which was comparable to that of shake flask data. C. intybus hairy root cultures grown in an acoustic mist bioreactor produced nearly twice as much esculin as compared to roots grown in bubble column and nutrient sprinkle bioreactors. Studies relating to on-line estimation of conductivity and osmolarity to predict the growth of hairy root cultures are also discussed. The results demonstrate the efficacy and the advantages of an acoustic mist bioreactor for the cultivation of hairy root cultures, especially with reference to C. intybus hairy roots.     

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.     

Bioreactor production of camptothecin by hairy root cultures of Ophiorrhiza pumila

A large-scale culture of hairy root of Ophiorrhiza pumila using a modified 3 l bioreactor was established. The hairy roots, incited by infection of Agrobacterium rhizogenes were grown in the bioreactor equipped with a stainless net. The final concentration of camptothecin was 0.0085% fresh wt of tissue, and the total production of camptothecin, an anti-neoplastic quinoline alkaloid, reached 22 mg over 8 weeks' culture in the reactor. Approx. 17% (3.6 mg) of the total camptothecin produced was excreted into the culture medium.     

Culture filtrate of root endophytic fungus Piriformospora indica promotes the growth and lignan production of Linum album hairy root cultures

The effect of addition of autoclaved and filter-sterilized culture filtrate of Piriformospora indica (a root endophytic fungus) to the growing Linum album hairy root cultures on growth and lignan production was investigated. The addition resulted in a significant enhancement in lignan production and growth. The podophyllotoxin and 6-methoxypodophyllotoxin (the lignans) concentrations were maximally improved by 3.8 times (233.8 mg/L) and 4.4 times (131.9 mg/L) in comparison to control cultures, respectively, upon addition of 3.0% (v/v) filter-sterilized culture filtrate of P. indica to the hairy root cultures of L. album for exposure time of 48 h. This increase in the lignan content also coincided with the increase in phenylalanine ammonia lyase activity, which was 3.1-fold (371.4 μkat/kg protein) higher compared to control cultures under the same conditions. The maximal increase in hairy root biomass was, however, obtained under different conditions; it was enhanced by 1.4 times (21.8 g/L) in comparison to control cultures, when 2% (v/v) filter-sterilized culture filtrate was in contact with L. album cultures for 96 h.     

The influence of methyl jasmonate,cholesterol and l‐arginine on solasodine production in hairy root culture of Solanum mammosum

The increasing demand of diosgenin for high‐revenue synthesis of steroid hormones by the pharmaceutical industries has driven researchers to look for other alternatives. Solasodine which was reported to be present in Solanum mammosum is known to be a potential source. The present study highlighted that added methyl jasmonate, cholesterol and l ‐arginine into the modified liquid full‐strength Murashige and Skoog (MS) medium (with ammonium to nitrate ratio 10.3 mM: 39.4 mM, and 4% (w/v) sucrose) could influence the solasodine production in the hairy roots of S. mammosum. The findings showed that both hairy root line‐ATCC31798 and line‐A4 (which were separately induced by Agrobacterium rhizogenes strain ATCC31798 and A4) acquired solasodine productivity of 4.5 mg/g dry weight roots with average dry biomass of 190 mg after 32 days culture, when using 50 mg fresh weight roots as initial inoculum size, with 100 mM cholesterol, 1000 μM l ‐arginine and 300 μM methyl jasmonate added simultaneously into the culture medium on day 20 of culture. The amount of solasodine obtained was five times higher than those without both the elicitor and precursor treatment. The improved solasodine production with a high‐biomass growth could reduce the production cost of steroid synthesis in the long run.     

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.     

Scopolamine,anisodamine and hyoscyamine production by Brugmansia candida hairy root cultures in bioreactors

Hyoscyamine, anisodamine (6β-hydroxyhyoscyamine) and scopolamine are tropane alkaloids produced by plants belonging to the Solanaceae family such as Brugmansia candida. These alkaloids were traditionally used in medicine because of their anticholinergic activity. Further therapeutical properties for anisodamine were recently described renewing the interest in these alkaloids. The scaling-up of hairy root cultures is an interesting strategy for the pharmaceutical production of these compounds instead of the isolation from plants. In this work, B. candida hairy roots were cultured in a modified 1.5 L stirred tank in order to analyze an alternative production system of scopolamine and anisodamine. It was found that these cultures produced an increased biomass and alkaloids concentration compared to the processes carried out in Erlenmeyer flasks. Anisodamine was the predominant alkaloid reaching a maximum concentration of 10.05 ± 0.76 mg/g DW in modified bioreactor culture system. The results obtained in this work are potentially applicable for the rational scale-up of the process.     

Variability of azadirachtin inAzarirachta indica (neem) and batch kinetics studies of cell suspension culture

Seeds of neem were collected from different parts of India and analyzed for their azadirachtin content by High Performance Liquid Chromatography (HPLC). In order to assess the effects of genotypic and geographical variation on azadirachtin content in cell cultures, callus development was attempted in the seeds containing high and low concentration of azadirachtin. The concentration of azadirachtin in callus cultures was significantly affected by the explant source. Seed kernels with higher azadirachtin content produced higher azadiractin content in callus cultures and lower azadirachtin content was seen in callus cultures produced from seed kernels with low azadiractin content. The protocol for development of elite stock culture ofAzadirachta indica was established with the objective of selecting a high azadirachtin-producing cell line. The highest azadirachtin-producing cell line was selected and the effects of different media and illumination conditions on growth and azadirachtin production were studied in shake flask suspension culture. Detailed batch growth kinetics was also established. These studies provided elite starter culture and associated protocols for cultivation ofA. indica plant cell culture in the bioreactor.     

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.     

Hairy root cultures of Rehmannia glutinosa and production of iridoid and phenylethanoid glycosides

Hairy root lines through the infection of Agrobacterium rhizogenes strain (A4) were established from shoot tips and leaves of Rehmannia glutinosa Libosch. Ten lines of hairy roots were selected on the basis of biomass increase in half-strength Gamborg medium (¹/₂ B5). Transgenic status of the roots was confirmed by polymerase chain reaction using rolB and rolC specific primers. Iridoid glycosides (catalposide, loganin, aucubin and catalpol) and phenylethanoid glycosides (verbascoside and isoverbascoside) identified using HPLC?CESI?CMS, and their contents were compared with untransformed root culture and roots of 1-year-old field-grown plants of R. glutinosa by RP-HPLC. The growth and production of secondary metabolites in ten hairy root lines varied considerably as to the media. Woody plant (WP) medium displayed higher growth in terms of fresh (FW) and dry weights (DW) compared to ¹/₂ B5 medium. High-yielding hairy root lines produced higher amounts of loganin, catalposide, verbascoside and isoverbascoside in comparison to the untransformed root culture and roots of 1-year-old field-grown plants. The highest amounts of catalposide and loganin in transformed roots were 4.45?mg?g^?1 DW (RS-2 hairy root line) and 4.66?mg?g^?1 DW (RS-1 hairy root line), respectively. Aucubin and catalpol were detected in some lines in trace amounts. The highest amounts of verbascoside (16.9?mg?g^?1 DW) and isoverbascoside (3.46?mg?g^?1 DW) were achieved in RS-2 root line. The contents of catalposide, verbascoside and isoverbascoside in high-producing lines were several times higher than in untransformed root culture and roots of R. glutinosa plants grown in soil. Loganin and aucubin could not be detected in roots of field-grown plants. However, the levels of catalpol were much lower in the in vitro roots.     

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.     

Effects of Agrobacterium rhizogenes strains and other parameters on production of isoflavonoids in hairy roots of Pueraria candollei Grah. ex Benth. var. candollei

Using several explants of Pueraria candollei Grah. ex Benth. var. candollei and two strains of Agrobacterium rhizogenes (ATCC 15834 and 43057), hairy root cultures were established. Including 100???M acetosyringone in the culture medium enhanced frequency of hairy root induction by up to 58?%. Subsequently, effects of inoculum size (IS) and temperature on growth and production of isoflavonoids in hairy roots were determined. Conditions of 1?%?IS and 32?°C promoted the highest accumulation of total isoflavonoid content, up to 31.0?±?22.6?mg/g dry weight (DW), in hairy roots. Moreover, culture of hairy roots at 32?°C decreased browning of hairy roots. Furthermore, this temperature promoted accumulation of the secondary metabolite daidzein; whereas, hairy root cultures at the stationary phase accumulated higher amounts of the isoflavonoid puerarin rather than daidzein.     

Improvement of rifemycins production by Amycolatopsis mediterranei in batch and fed-batch cultures

The production of rifamycins B and SV using glucose as main C-source by Amycolatopsis mediterranei in batch and fed-batch culture was investigated. Fed-batch culture using glucose as mono feeding substrate either in the form of pulse addition, in case of shake flask, or with constant feeding rate, in bioreactor level, proved to be an alternative production system with a significant increase in both volumetric and specific antibiotic production. The maximal concentrations of about 1146 mg/l and 2500 mg/l of rifamycins B and SV, respectively, was obtained in fed-batch culture in bioreactor level under non-oxygen limitation. On the other hand, the rate of rifamycins production was increased from 6.58 to 12.13 mg/l x h for rifamycin B and from 9.47 to 31.83 mg/l x h for rifamycin SV on the bioprocess transfer and improvement from the conventional batch cultivation in shake flask to fed-batch cultivation in stirred tank bioreactor.