Enhanced production of artemisinin by Artemisia annua L hairy root cultures in a modified inner-loop airlift bioreactor

Hairy root cultures of Artemisia annua L were cultured in a modified inner-loop airlift bioreactor for achieving maximum artemisinin production. The effects of initial pH, air flow rate, cycle of light irradiation and temperature on growth and artmisinin production in Artemisia annua L hairy root cultures were investigated. Under the optimum conditions, the maximum production of artemisinin reached to 577.5?mg/l after 20 days.     

Isolation and production of artemisinin and stigmasterol in hairy root cultures of Artemisia annua

Scaled-up hairy root culture of Artemisia annua L. was established in three-liter Erlenmeyer flask. Both artemisinin and stigmasterol that derive from the common precursors of isopentenyl diphosphate and farnesyl pyrophosphate were isolated from hairy roots. The production rate of artemisinin isolated by column chromatography from hairy root cultures was 0.54% (mg.gDW⁻¹). Stigmasterol was identified by mass spectrometry and nuclear magnetic resonance analysis. The production of stigmasterol isolated by column chromatography from hairy root cultures was 108.3% (mg.gDW⁻¹). In hairy root cultures, the production rate of stigmasterol was estimated to be 201 times greater than that of artemisinin. Our results suggest that investigation of secondary metabolites may provide a new insight to study artemisinin production in hairy root cultures. This revised version was published online in August 2006 with corrections to the Cover Date.     

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.     

Increased shikonin production by hairy roots of Lithospermum erythrorhizon in two phase bubble column reactor

Summary Plant hairy root cultures of Lithospermum erythrorhizon were carried out to produce shikonin derivatives by employing in situ extraction with n-hexadecane in a shake flask and a bubble column bioreactor. Over 95 % shikonin produced was recovered in the n-hexadecane layer. In flask cultures the maximum concentration of shikonin with n-hexadecane extraction was 3 times higher than that obtained without extraction. In the two phase bubble column reactor, 572.6 mg/L of shikonin and 15.6 g/L of dry cell mass were obtained after 54 days. Shikonin was produced at a constant level of 10.6 mg/L day during this period.     

Development of a nutrient mist bioreactor for growth of hairy roots

Summary Hairy root cultures of Artemisia annua L. were cultivated in three different mist bioreactors, each fitted with three stainless steel meshes. The growth rates in the three 2.3-L mist bioreactors differed. After 25 d, the growth index (final dry weight/initial dry weight) of the roots was 42 in a nutrient mist bioreactor, 61 in an inner-loop nutrient mist bioreactor, and 68 in a modified inner-loop nutrient mist bioreactor. Under a misting cycle of 3/30 (ON 3 min/OFF 30 min) for 25 d, dry weight reached 13.6 g/L of medium in the modified inner-loop nutrient mist bioreactor in which nutrient could be supplied without dilution of mist by air flow.     

Inhibitory role of root hairs on transport within root culture bioreactors

An experimental system was developed to produce root cultures of Hyoscyamus muticus with and without the profuse root hairs. Growth in the presence of 7.6 microM pyrene butyric acid (PBA) and 2.2 mM phosphate virtually eliminated root hairs, whereas growth rate, general morphology and nutrient yields remained unchanged in well-mixed flask culture. These root cultures were used to demonstrate decreased flow resistance in a tubular reactor as a result of root hair removal. To assess the impact on bioreactor performance, hairy and hairless root cultures were grown in a highly characterized 15-L bubble column bioreactor. In the absence of root hairs, the mixing was greatly enhanced; mixing times became shorter for the hairless culture at roughly 100 g (fresh weight)/L. By the end of the 3-week culture period, the mixing time of the hairy culture was 29 times longer than that of the hairless culture. The growth rate of the hairless culture in the bioreactor was as much as 2.4 times greater than growth of the hairy culture under the same conditions. The improved reactor performance was reflected in greater biomass accumulation and respiratory activity. These results show that the root hairs-which facilitate nutrient uptake in a static soil environment-are detrimental to growth in a liquid environment as an effect of their stagnating fluid flow and limiting oxygen availability.     

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.     

促进黄花蒿发根青蒿素合成的内生真菌诱导子的制备

应用酸解法对黄花蒿(ArtemisiaannuaL.)内生胶孢炭疽菌(Colletotrichumgloeosporioides)菌丝体进行提取,在黄花蒿发根培养系统中比较了各制备提取物的青蒿素诱导活性。活性提取物经过SephadexG25层析后,部分纯化的内生菌寡糖提取物(MW<2500)可显著促进发根青蒿素的合成,培养23d的发根经诱导子(0.4mg/mL)处理4d后,青蒿素产量可达13.51mg/L,比同期对照产量提高51.63%,诱导作用与诱导子浓度、作用时间相关。内生菌寡糖诱导子的制备和使用,在青蒿素生物技术生产研究中为首次应用。     

Effects of Fungal Elicitors on Cell Growth and Artemisinin Accumulation in Hairy Root Cultures of Artemisia annua

The artemisinin accumulation in the hairy root cultures of Artemisia annua L. was enhanced via a treatment of three fungal elicitors separately ( Verticillium dahliae Kleb., Rhizopus stolonifer (Ehrenb. ex Fr. ) Vuill and Colletotrichum dematium (Pers.) Grove). Among these three elicitors, V. dahliae had the highest inducing efficiency, but none of them manifests any noticeable effects on the cell growth of the hairy root cultures. The artemisinin content of the hairy root cultures treated with V. dahliae elicitor was 1.12 mg/g DW, which was 45% higher than the control (0.77 mg/g DW). The results showed that elicitation was dependent on the elicitor concentration, the incubation period and the physiological stage at which the hairy root cultures were treated. In addition, the authors found that for V. dahliae, the optimum concentration was 0.4 mg carbohydrate per millilitre medium, the strongest response of A. annua hairy root cultures to the elicitation was at the late exponential growth stage, and the highest artemisinin content of the hairy root cultures was on the 4th day post treatment.     

Ri质粒转化的青蒿发根培养及青蒿素的生物合成

用发根农杆菌(Agrobacterium rhizogenes)转化药用植物青蒿(Artemisia annua L．)并建立了发根体外培养系统。Southern杂交、NPT Ⅱ酶的检测证明Ri质粒的T—DNA转移并整合到植物的核基因组上。在发根培养系统中,检测了青蒿的重要次生代谢物一青蒿素的含量,检测了不同理化因子对发根生长及青蒿素含量的影响。结果表明：光照(日光灯,12h光周期,20001x)有利于次生产物青蒿素的积累。培养基的pH值为5．4。蔗糖浓度为3％不仅促进发根的生长,而且促进青蒿素的积累。低浓度萘乙酸(NAA)对发根生长具有促进作用,但抑制青蒿素的合成。赤霉素GA,对发根的生长及次生产物的合成都具有促进作用,其最适浓度为4．8mg／L。     

真菌诱导子对青蒿发根细胞生长和青蒿素积累的影响

３种真菌诱导子（大菌丽花轮枝孢（Ｖｅｒｔｉｃｉｌｌｉｕｍ ｄａｈｉａｅ Ｋｌｅｂ．）、葡枝根霉（Ｒｈｉｚｏｐｕｓ ｓｔｏｌｏｎｉｆｅｒ（Ｅｈｒｅｎｂ．ｅｘＦｒ．）Ｖｕｉｌｌ）和束状刺盘孢（Ｃｏｌｌｅｔｏｒｉｃｈｕｍ ｄｅｍａｔｉｕｍ（Ｐｅｒｓ．）Ｇｒｏｖｅ）处理青蒿（Ａｒｔｅｍｉｓｉａ ａｎｎｕａＬ．）的发根,均能促进发根中青蒿素的积累,其中以大丽花轮枝孢的诱导效果最好;对细胞生长均没有明显影响,     

Comparative evaluation of modified bioreactors for enhancement of growth and secondary metabolite biosynthesis usingPanax ginseng hairy roots

Hairy root cultures have demonstrated great promise in terms of their biosynthetic capability toward the production of secondary metabolites, but continue to constitute a major challenge with regard to large-scale cultures. In order to assess the possibility of conducting mass production of biomass, and the extraction of useful metabolites fromPanax ginseng. P. ginseng hairy roots, transformed byRhizobium rhizogenes KCTC 2744, were used in bioreactors of different types and sizes. The most effective mass production of hairy roots was achieved in several differently sized air bubble bioreactors compared to all other bioreactor types. Hairy root growth was enhanced by aeration, and the production increased with increasing aeration rate in a 1 L bioreactor culture. It was determined that the hairy root growth rate could be substantially enhanced by increases in the aeration rate upto 0.5 wm, but at aeration rates above 0.5 wm, only slight promotions in growth rates were observed. In 20 L air bubble bioreactors, with a variety of inoculum sizes, the hairy roots exhibited the most robust growth rates with an inoculum size of 0.1% (w/v), within the range 0.1 to 0.7% (w/v). The specific growth rates of the hairy roots decreased with increases in the inoculum size.     

Batch and fed-batch production of betalains by red beet (Beta vulgaris) hairy roots in a bubble column reactor

Hairy root cultures from red beet (Beta vulgaris L.), which could be used for the commercial production of biologically active betalain pigments, were cultivated in a 3 L bubble column bioreactor in batch mode with various rates of air supply. Both the growth of the roots and betalain volumetric yields were highest (12.7 g accumulated dry biomass/L and 330.5 mg/ L, respectively) with a 10 L/h (0.083 vvm) air supply. The air flow rate also influenced the betacyanins/betaxanthins ratios in the cultures. Growth and betalains production were then examined in two fed-batch regimes (with a 10 L/h air supply), in which nutrient medium was fed just once or on five occasions, designated FBI and FBII, respectively. The root mass accumulation was increased in the FBI feeding regime (to 13.3 g accumulated dry biomass/ L), while in FBII the betalains content was ca. 11% higher (15.1 mg betacyanins/g dry weight and 14.0 mg betaxanthins/g dry weight) than in the most productive batch regime. Data on the time course of the utilization of major components in the medium during both operational modes were also collected. The implications of the information acquired are discussed, and the performance of the hairy roots (in terms of both growth and betalains production) in the bubble column reactor and previously investigated cultivation systems is compared.     

Polyamine and methyl jasmonate-influenced enhancement of betalaine production in hairy root cultures of Beta vulgaris grown in a bubble column reactor and studies on efflux of pigments

Hairy root cultures of red beet (Beta vulgaris) were grown in 3 l bubble column reactor for studying growth and pigment production under the influence of polyamines (PA) and elicitor treatment. Earlier studies with shake flask cultures had shown that combined feeding of spermidine (spd) and putrescine (put) (each 0.75 mM) significantly enhanced betalaine productivity in hairy root cultures of red beet. The present study has been focused on betalaine production in 3 l bubble column bioreactor where the growth pattern and betalaine synthesis under the influence of similar levels of polyamines were followed. A combination of spermidine and putrescine fed to the roots each at levels of 0.75 mM efficiently increased growth and pigment production resulting in 1.23-fold higher biomass (39.2 g FW l⁻¹) and 1.27-fold higher betalaine content (32.9 mg g⁻¹ DW) than control. Treatments with various levels of elicitor-methyl jasmonate (MJ), though progressively retarded biomass, at 40 μM level resulted in a significant increase in betalaine content resulting in 36.13 mg g⁻¹ DW which was 1.4-fold higher than the control. Further higher concentrations of methyl jasmonate treatments supported high as well as rapid accumulation of betalaines, the overall betalaine productivity was hampered mainly because of the inhibitory action on biomass. Pigment release studies with cetyl trimethyl ammonium bromide (CTAB) resulted in optimization of concentration for better efflux of betalaines without showing any inhibitory effect on hairy root viability. These studies on product enhancement and on-line extraction of pigment are useful for developing a bioreactor system for betalaine production using B. vulgaris hairy root cultures. In particular the use of elicitors and efflux studies provide an insight for integrating unit operations and developing a process for continuous operation and higher production of phytochemicals.     

Computational fluid dynamics modeling of mass transfer behavior in a bioreactor for hairy root culture. I. Model development and experimental validation

A two-dimensional axisymmetric computational fluid dynamics (CFD) model based on a porous media model and a discrete population balance model was established to investigate the hydrodynamics and mass transfer behavior in an airlift bioreactor for hairy root culture.During the hairy root culture of Echinacea purpurea, liquid and gas velocity, gas holdup, mass transfer rate, as well as oxygen concentration distribution in the airlift bioreactor were simulated by this CFD model. Simulative results indicated that liquid flow and turbulence played a dominant role in oxygen mass transfer in the growth domain of the hairy root culture. The dissolved oxygen concentration in the hairy root clump increased from the bottom to the top of the bioreactor cultured with the hairy roots, which was verified by the experimental detection of dissolved oxygen concentration in the hairy root clump. This methodology provided insight understanding on the complex system of hairy root culture and will help to eventually guide the bioreactor design and process intensification of large-scale hairy root culture.     

青蒿毛状根生长、青蒿素合成以及 营养物消耗的动力学

诱导产生的青蒿毛状根培养物置于MS培养基(含30 g/L蔗糖)进行悬浮培养,并对悬浮培养过程中毛状根生长、青蒿素合成、蔗糖、磷酸盐和不同氮源的消耗、pH和电导率的动力学过程进行分析。经30 d培养,生物量干重和青蒿素产量分别达到13.7 g/L和0.23 g/L,碳源和氮源在培养过程中被逐渐利用,而磷酸盐的利用速率最快,培养至15 d所有的磷酸盐均被吸收,pH在培养初期降低,后又逐渐上升,电导率由于毛状根生长对无机离子的吸收而逐渐减低。     

Growth and betacyanin production by hairy roots of Beta vulgaris in airlift bioreactors

Hairy roots of red beet (Beta vulgaris L.) were cultivated in different types of airlift bioreactors (cone, balloon, bulb, drum and column bioreactors of 5 l capacity and containing 3 l of half strength Murashige & Skoog medium). The cone type of airlift bioreactor gave the highest biomass of hairy roots and betacyanin accumulation. Betacyanin accumulation was 27 mg g^–1 dry wt in cultures aerated at 0.3 vvm. Light irradiation of 20 mol m^–2 s^–1 promoted hairy root growth but optimum betacyanin (34 mg g^–1 dry wt) accumulation was with the cultures grown under 60 mol m^–2 s^–1.     

Production of glomus intraradices propagules, an arbuscular mycorrhizal fungus, in an airlift bioreactor

This work addresses the symbiotic culture of the arbuscular mycorrhizal (AM) fungus Glomus intraradices with Daucus carota hairy roots transformed by Agrobacterium rhizogenes, in two submerged culture systems: Petri dish and airlift bioreactor. AM fungi play an active role in plant nutrition and protection against plant pathogens. These fungi are obligate biotrophs as they depend on a host plant for their needs in carbohydrates. The effect of the mycorrhizal roots inoculum-to-medium volume ratio on the growth of both symbionts was studied. A critical inoculating condition was observed at approximately 0.6 g dry biomass (DW). L-1 medium, above which root growth was significantly reduced when using a low-salt minimal (M) liquid medium previously developed for hairy root-AM fungi co-culture. Below critical inoculum conditions the maximum specific root growth and specific G. intraradices spore production rates of 0.021 and 0.035 d-1, respectively, were observed for Petri dish cultures. Maximum spore production in the airlift bioreactor was ten times lower than that of Petri dish cultures and obtained with the lowest inoculum assessed (0.13 g DW. L-1 medium) with 1.82 x 10(5) +/- 4.05 x 10(4) (SEM) spores (g DW inoculum)-1 (L medium)-1 in 107 d. This work proposes a second-generation bioprocess for AM fungi propagule production in bioreactors. Copyright 1999 John Wiley & Sons, Inc.     

Improvement of artemisinin accumulation in hairy root cultures of Artemisia annua L by fungal elicitor

The effect of fungal elicitor, derived from mycelial extracts of Penicillium chysogenum 3446, on artemisinin production in hairy root cultures of Artemisia annua L was studied. Various concentrations of elicitor were added to the culture medium after 18 days. Time course experiments were carried out using a defined concentration of elicitor after 18 days. Various ages of hairy root cultures were elicited using a defined concentration of elicitor for 3 days. Artemisinin production in 21-day hairy root cultures treated with 0.3 mg total sugar/ml medium elicitor for 3 days reached to 549.1 mg/l.     

Improved production of phenylethanoid glycosides by Cistanche deserticola cells cultured in an internal loop airlift bioreactor with sifter riser

An internal loop airlift bioreactor with sifter riser (ILABSR) was composed of a bubble column and a draught-tube rolled with 40-mesh sifter that placed 5 cm above the bottom at the center of the column. A 2 L ILABSR was used for the suspension cultivation of Cistanche deserticola cells and its performance was compared with shake flask culture and a bubble column. Under the optimum culture conditions with the air flowrate of 0.075 m³/h and the inoculation size of 4.7%, about one-fifth cells were attached to the sifter draught-tube. PeG content in these cells was 16.3%, which was 104% higher than that of suspension cells. The production of phenylethanoid glycosides reached 0.85 g/L, which was 102 and 4% higher than those cultured in a 2 L bubble column and shake flasks respectively under their optimal culture conditions.