Monoterpenoid oxindole alkaloid production by Uncaria tomentosa (Willd) D.C. cell suspension cultures in a stirred tank bioreactor

Cell growth, monoterpenoid oxindole alkaloid (MOA) production, and morphological properties of Uncaria tomentosa cell suspension cultures in a 2-L stirred tank bioreactor were investigated. U. tomentosa (cell line green Uth-3) was able to grow in a stirred tank at an impeller tip speed of 95 cm/s (agitation speed of 400 rpm), showing a maximum biomass yield of 11.9 +/- 0.6 g DW/L and a specific growth rate of 0.102 d(-1). U. tomentosa cells growing in a stirred tank achieved maximum volumetric and specific MOA concentration (467.7 +/- 40.0 microg/L, 44.6 +/- 5.2 microg/g DW) at 16 days of culture. MOA chemical profile of cell suspension cultures growing in a stirred tank resembled that of the plant. Depending on culture time, from the total MOA produced, 37-100% was found in the medium in the bioreactor culture. MOA concentration achieved in a stirred tank was up to 10-fold higher than that obtained in Erlenmeyer flasks (agitated at 110 rpm). In a stirred tank, average area of the single cells of U. tomentosa increased up to 4-fold, and elliptical form factor increased from 1.40 to 2.55, indicating enlargement of U. tomentosa single cells. This work presents the first report of U. tomentosa green cell suspension cultures that grow and produce MOA in a stirred tank bioreactor.     

The accumulation of isocamptothecin A and B in suspension cell culture of <Emphasis Type="Italic">Camptotheca acuminata</Emphasis>

The initiation of the suspension culture of Camptotheca acuminata M42 cell line was reported. Isocamptothecin A (ICPTA) and isocamptothecin B (ICPTB), two alkaloids that do not exist in the parent plant were identified in the suspension cell culture of Camptotheca acuminata. Suspension cell culture was carried out in both flasks and a 5-l airlift bioreactor and the time course for cell growth and accumulations of ICPTA and ICPTB were investigated. It was found that accumulations of ICPTA and ICPTB was partly associated with cell growth and the size of cell aggregates affected the contents of ICPTA and ICPTB in the cultures to some extent (cell aggregates with a size of 2--4 mm in diameter presented the highest ICPTA and ICPTB contents). Although the cell dry weight of 15.1 g l^-1 achieved in a 5-l airlift bioreactor was lower than that in flasks, 18.4 g l^-1, the contents of ICPTA and ICPTB were almost the same levels.     

Influence of auxins and sucrose in monoterpenoid oxindole alkaloid production by Uncaria tomentosa cell suspension cultures

Growth and alkaloid production in Uncaria tomentosa cell suspension cultures were studied in Murashige and Skoog medium supplemented with 10 microM 2,4-dichlorophenoxyacetic acid, 10 microM kinetin, and 58 mM sucrose for maintenance and with 10 microM indole-3-acetic acid, 10 microM kinetin, and 58 mM sucrose for production. A U. tomentosa pale Uth-3 cell line, cultured in the production medium, showed a reduced lag phase and a specific growth rate (mu) of 0.27 day(-1), while cells growing in the maintenance medium showed mu = 0.20 day(-1). U. tomentosa cells growing in the production medium produced monoterpenoid oxindole alkaloids (MOA) in amounts of 10.2 +/- 1.6 microg g(-1) dry weight (DW). The chemical profile of MOA produced by in vitro cell cultures was similar to that found in the plant. After 10 subcultures, maximum MOA production decreased to 2.0 +/- 0.7 microg g(-1) DW, while tryptamine alkaloids (TA) were produced with a maximum of 6.2 +/- 0.4 microg g(-1) DW. The increase of initial sucrose concentration up to 145 mM in the production medium enhanced the cell biomass by 3.2-fold (from 10.2 +/- 0.1 to 32.8 +/- 1.1 g DW L(-1)), reduced mu from 0.27 to 0.23 day(-1), and provoked a substantial accumulation of TA (23.1 +/- 4.7 microg g(-1) DW). A high sucrose concentration stimulated MOA production in the maintenance medium (2.7 +/- 0.5 microg g(-1) DW), even in the presence of 2,4-dichlorophenoxyacetic acid.     

Effect of bioreactor configuration on substrate uptake by cell suspension cultures of the plant Eschscholtzia californica

Summary The uptake of carbohydrates and oxygen by cell suspension cultures of the plant Eschscholtzia californica (California poppy) was studied in relation to biomass production in shake flasks, a 1-1 stirred-tank bioreactor and a 1-1 pneumatically agitated bioreactor. The sequence of carbohydrate uptake was similar in all cases, with sucrose hydrolysis occurring followed by the preferential uptake of glucose. The uptake of fructose was found to be affected by the oxygen supply rate. Carbohydrate utilization occurred at a slower rate in the bioreactors. Apparent biomass yields, Y _X/S, ranged from 0.42 to 0.50 g biomass/g carbohydrate, while true biomass yields, Y _X/S, were about 0.69 g/g. The maintenance coefficient for carbohydrate, m _S, ranged between 0.002 and 0.008 g/dry weight (DW) per hour. The maximum measured specific oxygen uptake rate was 0.56 mmol O₂/g DW per hour and occurred early in the growth stage. The decline in specific uptake rate coincided with a decline in cell viability. The oxygen uptake rate was faster in shake flasks, corresponding to the higher growth rate obtained. The true growth yield on oxygen, YX/O₂, was calculated to range from 0.83 to 1.23 g biomass/g O₂, while the maintenance coefficient, mO₂, ranged from 0.15 to 0.25 mmol O₂/g DW per hour. The growth yields for oxygen determined from the stoichiometry of an elemental balance were within 10% of those calculated from experimental data. Offprint requests to: Raymond L. Legge     

Repeated elicitation enhances taxane production in suspension cultures of Taxus chinensis in bioreactors

Methyl jasmonate added at 100 M on days 8, 14 and 20 to cultures of Taxus chinensis growing in flasks and 1 l airlift bioreactors improved taxuyunnanine C (TC) production by 50–60% in flasks and by about 80% in airlift bioreactors compared with single addition of 100 M methyl jasmonate on day 8. The final TC production in the airlift bioreactors reached 565±47 mg l^–1, which is the highest reported for taxoid production in a bioreactor.     

Enhancement of somatic embryogenesis of Ipomoea batatas in solid eultures and production of mature somatic embryos in liquid cultures for application to a bioreactor production system

Somatic embryos of Ipomoea batatas Lam. (sweet potato cv. White Star) were produced in an airlift bioreactor. This work describes the optimization of the embryogenic system on semisolid medium, followed by transfer of the system to liquid cultures and ultimately to the airlift bioreactor. The physiological age of embryogenic callus influenced the number and overall morphology of the embryo population in both semisolid and liquid medium. Maximum mature embryo production (35 embryos 10 mg^-1 inoculum) was obtained from six-week-old callus at 30°C. Somatic embryogenesis occurred in liquid cultures containing 20 mM NH₄NO₃ and 30 mM KCl. Globular embryos formed and continued development in suspension producing viable, mature cotyledonary embryos by day 14. Embryo formation and development was limited in the bioreactor. Although shear stress was responsible for some embryogenic damage, the effect of purging the system with fresh air needed to be investigated. To isolate aeration effects from shear stress effects, atmospheric determinations were performed on shaker flask cultures. Initially the gas composition within the Erlenmeyer headspace was that of room air. Ethylene increased to a maximum of 6.4 ppm (day 16), maximum CO₂, 21.2%, was also evident on day 16, and oxygen was depleted to a minimum of 8.1% by day 14. Purging the cultures with fresh air reduced the number of embryos formed; however, they were significantly longer than those formed in closed flasks. The gas response model of Ipomoea batatas will enable atmosphere replenishment in the bioreactor mimicking that of the shaker flask environment. Once the damaging effects of shear stress have been overcome, the regulation of bioreactor gasses should allow somatic embryo formation in the bioreactor comparable to that in shaker flasks.     

Galanthamine production by Leucojum aestivum L. shoot culture in a modified bubble column bioreactor with internal sections

Shoot culture of summer snowflake (Leucojum aestivum L.) was successfully cultivated in an advanced modified glass‐column bioreactor with internal sections for production of Amaryllidaceae alkaloids. The highest amounts of dry biomass (20.8 g/L) and galanthamine (1.7 mg/L) were achieved when shoots were cultured at 22°C and 18 L/(L·h) flow rate of inlet air. At these conditions, the L. aestivum shoot culture possessed mixotrophic‐type nutrition, synthesizing the highest amounts of chlorophyll (0.24 mg/g DW (dry weight) chlorophyll A and 0.13 mg/g DW chlorophyll B). The alkaloids extract of shoot biomass showed high acetylcholinesterase inhibitory activity (IC₅₀ = 4.6 mg). The gas chromatography–mass spectrometry (GC/MS) profiling of biosynthesized alkaloids revealed that galanthamine and related compounds were presented in higher extracellular proportions while lycorine and hemanthamine‐type compounds had higher intracellular proportions. The developed modified bubble‐column bioreactor with internal sections provided conditions ensuring the growth and galanthamine production by L. aestivum shoot culture.     

Cultivation of transgenicNicotiana tabacum suspension cells in bioreactors for the production of mGM-CSF

TransgenicNicotiana tabacum cells were cultivated for the production of murine granulocyte macrophage-colony stimulating factor (mGM-CSF) in both a stirred, tank biore|actor and an airlift bioreactor with draft tube. Cell growth and mGM-CSF production in the airlift bioreactor were found to be better than those achieved in the stirred tank bioreactor. In the airlift bioreactor. 9.0 g/L of cells and 2.2 ng/mL of mGM-CSF were obtained (11.0 g/L and 2.4 ng/mL, respectively in shake flasks). Although the lag period was prolonged and mGM-CSF production was lowered by 33% in the stirred tank bioreactor as compared to the control culture, the maximum cell density was increased up to 12.0 g/L due to better mixing by agitation at the higher cell density.     

Hydrodynamic stress induces monoterpenoid oxindole alkaloid accumulation by Uncaria tomentosa (Willd) D. C. cell suspension cultures via oxidative burst

Uncaria tomentosa cell suspension cultures were grown in a 2-L stirred tank bioreactor operating at a shear rate gamma(.)(avg)=86 s(-1). The cultures showed an early monophasic oxidative burst measured as H2O2 production (2.15 micromol H2O2 g(-1) dw). This response was followed by a transient production of monoterpenoid oxindole alkaloids (178 +/- 40 microg L(-1) at 24 h). At the stationary phase (144 h), the increase of the shear rate gamma(.)(avg) up to 150 s(-1) and/or oxygen tension up to 85% generated H2O2, restoring oxindole alkaloid production. U. tomentosa cells cultured in Erlenmeyer flasks also exhibited the monophasic oxidative burst but the H2O2 production was 16-fold lower and the alkaloids were not detected. These cells exposed to H2O2 generated in situ produced oxindole alkaloids reaching a maximum of 234 +/- 40 microg L(-1). A positive correlation was observed between the oxindole alkaloid production and the endogenous H2O2 level. On the other hand, addition of 1 microM diphenyleneiodonium (NAD(P)H oxidase inhibitor) or 10 microM sodium azide (peroxidases inhibitor) reduced both H2O2 production and oxindole alkaloids build up, suggesting that these enzymes might play a role in the oxidative burst induced by the hydrodynamic stress.     

Manipulation of ginsenoside heterogeneity of <Emphasis Type="Italic">Panax notoginseng</Emphasis> cells in flask and bioreactor cultivations with addition of phenobarbital

Structure-similar ginsenosides have different or even totally opposite biological activities, and manipulation of ginsenoside heterogeneity is interesting and significant to biotechnological application. In this work, addition of 1 mM phenobarbital to cell cultures of Panax notoginseng at a relatively high inoculation size of 7.6 g dry cell weight (DW)/L enhanced the production of protopanaxatriol-type (Rg₁ + Re) ginsenosides in both shake flask and airlift bioreactor (ALR, 1 L working volume). The content of Rg₁ + Re in the ALR was increased from 42.5 ± 4.0 mg per gram DW in untreated cell cultures (control) to 56.4 ± 4.6 mg per gram DW with addition of 1.0 mM phenobarbital. The maximum productivity of Rg₁ + Re in the ALR reached 5.66 ± 0.38 mg L⁻¹ d⁻¹, which was almost 3.3-fold that of control. The maximum ratio of the detectable ginsenosides protopanaxatriol:protopanaxadiol (Rb₁) was 7.6, which was about twofold that of control. The response of protopanaxadiol 6-hydroxylase (P6H) activity to phenobarbital addition coincided with the above-mentioned change of ginsenoside heterogeneity (distribution). Phenobarbital addition is considered as a useful strategy for manipulating the ginsenoside heterogeneity in bioreactor with enhanced biosynthesis of protopanaxatriol by P. notoginseng cells.     

Stimulating effect of both 4’‐O‐methylnorbelladine feeding and temporary immersion conditions on galanthamine and lycorine production by Leucojum aestivum L. bulblets

Bulb cultures of Leucojum aestivum and L. aestivum ‘Gravety Giant’ were subcultured in medium containing the precursor 4’‐O‐methylnorbelladine (MN) at various concentrations [0 (control), 0.15 and 0.3 g/L]. The cultures were conducted in bioreactor RITA® and lasted for 15, 30, 40 and 50 days. The growth rate and the alkaloid accumulation in bulblets were studied. For this latter purpose, a purification method was developed. It comprised a highly selective solid phase extraction using on the one hand, UPTI‐CLEAN SI and SCX cartridges for plant extracts and on the other hand, 2H cartridges for culture media. Pure alkaloidal fractions were, thus, analyzed by LC‐ESI‐MS allowing the quantitative evaluation of galanthamine and lycorine from culture extracts. Precursor feeding along with temporary immersion conditions was found to significantly improve the accumulation of both galanthamine and lycorine. The maximal concentrations of galanthamine (0.81 mg/g DW) and lycorine (0.54 mg/g DW) in L. aestivum bulblets were reached, respectively, after 40 days of culture with 0.15 g/L of precursor and after 30 days of culture with 0.3 g/L of precursor. In L. aestivum ‘Gravety Giant’ bulb cultures, 0.3 g/L of precursor was the best condition for both galanthamine (0.6 mg/g DW after 50 days) and lycorine (1.13 mg/g DW after 30 days).     

Enhanced ajmalicine production in Catharanthus roseus cell cultures by combined elicitor treatment: from shake-flask to 20-l airlift bioreactor

A two-stage process for enhanced ajmalicine production in elicited Catharanthus roseus cell cultures was developed in shake-flasks and a bioreactor. By using combined elicitor treatment of an Aspergillum niger mycelium and tetramethyl ammonium bromide, yields of ajmalicine were 48 mg l^–1, 52 mg l^–1 and 33 mg l^–1, respectively in 500-ml flasks, 1000-ml flasks and a 20-l airlift bioreactor. The peroxidase and superoxide dismutase activities decreased in elicited cell cultures but catalase and lipoxygenase activities increased in these cultures. The combined elicitor treatment also caused a significant increase of malondialdehyde content in cell cultures.     

The role of thiamine inYersinia kristensenii resistance to antibiotics and heavy metals

The resistance to divalent metal ions, antibiotics and H₂O₂ was investigated inYersinia kristensenii strains 13, 15, 18 by performing subcultivations with CdSO₄ (20 and 100mg/L) in nutrient agar (NA) and M9 medium with thiamine. Metal resistance of all three strains in NA was the same and decreased in the following sequence: Ni>Zn=Co>Cd. The chloramphenicol (Cmp) resistance ranged between 32 and 256 mg/L and the H₂O₂ sensitivity was very low or even zero. In the presence of thiamine the metal resistance sequence changed to Zn=Cd>Ni, Co, Ni and Co tolerance being 10–20 mg/L. Cmp resistance of all strains increased to 256 mg/L and H₂O₂ sensitivity also rose. In Cd-treated cultures, the ratio of glucose to thiamine in culture medium affected Cd resistance. At normal content of glucose and thiamine (5 g/L and 5mg/L), Cd resistance markedly decreased coincident with thiamine exhaustion in these slowly-growing cultures. The Cmp resistance decreased to 16 mg/L, Ni and Co intolerance and H₂O₂ hypersensitivity appeared. At lowered glucose or thiamine levels (5 g/L and 2.5 mg/L or 2.5 g/L and 5 mg/L) a marginal decrease of Cd resistance took place in response to limited glucose uptake. Low thiamine or low-glucose cultures were resistant to H₂O₂, and exhibited a small decrease in Cmp resistance and a low Ni, Co tolerance. The adaptation of strain 15 to Cd induced only a small decrease of Cd resistance. Lowered glucose-to-thiamine ratio in culture medium probably induced in Cd-treated cultures a response triggering Cd resistance.     

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.     

MALDI‐TOF characterization of hGH1 produced by hairy root cultures of Brassica oleracea var. italica grown in an airlift with mesh bioreactor

Expression systems based on plant cells, tissue, and organ cultures have been investigated as an alternative for production of human therapeutic proteins in bioreactors. In this work, hairy root cultures of Brassica oleracea var. italica (broccoli) were established in an airlift with mesh bioreactor to produce isoform 1 of the human growth hormone (hGH1) as a model therapeutic protein. The hGH1 cDNA was cloned into the pCAMBIA1105.1 binary vector to induce hairy roots in hypocotyls of broccoli plantlets via Agrobacterium rhizogenes. Most of the infected plantlets (90%) developed hairy roots when inoculated before the appearance of true leaves, and keeping the emerging roots attached to hypocotyl explants during transfer to solid Schenk and Hildebrandt medium. The incorporation of the cDNA into the hairy root genome was confirmed by PCR amplification from genomic DNA. The expression and structure of the transgenic hGH1 was assessed by ELISA, western blot, and MALDITOF‐MS analysis of the purified protein extracted from the biomass of hairy roots cultivated in bioreactor for 24 days. Production of hGH1 was 5.1 ± 0.42 µg/g dry weight (DW) for flask cultures, and 7.8 ± 0.3 µg/g DW for bioreactor, with productivity of 0.68 ± 0.05 and 1.5 ± 0.06 µg/g DW*days, respectively, indicating that the production of hGH1 was not affected by the growth rate, but might be affected by the culture system. These results demonstrate that hairy root cultures of broccoli have potential as an alternative expression system for production of hGH1, and might also be useful for production of other therapeutic proteins. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:161–171, 2014     

High density cell culture of Panax notoginseng for production of ginseng saponin and polysaccharide in an airlift bioreactor

High cell density of Panax notoginseng in a 17 l airlift bioreactor was achieved in batch cultivation using a modified MS medium. The dry cell weight, ginseng saponin and polysaccharide reached 24, 1.7 and 2.8 g l^–1, respectively, after 15 d. A strategy of sucrose feeding based on changes in the specific O₂ uptake rate was applied to the cell cultures, which increased these respective yields to 30, 2.3 and 3.2 g l^–1.     

High‐yield secretion of recombinant proteins expressed in tobacco cell culture with a designer glycopeptide tag: Process development

Low‐yield protein production remains the most significant economic hurdle with plant cell culture technology. Fusions of recombinant proteins with hydroxyproline‐O‐glycosylated designer glycopeptide tags have consistently boosted secreted protein yields. This prompted us to study the process development of this technology aiming to achieve productivity levels necessary for commercial viability. We used a tobacco BY‐2 cell culture expressing EGFP as fusion with a glycopeptide tag comprised of 32 repeat of ”Ser‐Pro“ dipeptide, or (SP)₃₂, to study cell growth and protein secretion, culture scale‐up, and establishment of perfusion cultures for continuous production. The BY‐2 cells accumulated low levels of cell biomass (～7.5 g DW/L) in Schenk & Hildebrandt medium, but secreted high yields of (SP)₃₂‐tagged EGFP (125 mg/L). Protein productivity of the cell culture has been stable for 6.0 years. The BY‐2 cells cultured in a 5‐L bioreactor similarly produced high secreted protein yield at 131 mg/L. Successful operation of a cell perfusion culture for 30 days was achieved under the perfusion rate of 0.25 and 0.5 day^?1, generating a protein volumetric productivity of 17.6 and 28.9 mg/day/L, respectively. This research demonstrates the great potential of the designer glycopeptide technology for use in commercial production of valuable proteins with plant cell cultures.