Effect of carbon dioxide on cell growth and saponin production in suspension cultures of Panax ginseng

The effects of carbon dioxide supply within the range of 1–5 % (along with purified air), on cell culture of Panax ginseng were investigated in a balloon type bubble bioreactor containing 4 dm³ of Murashige and Skoog (MS) medium supplemented with 7.0 mg dm⁻³ indolebutyric acid, 0.5 mg dm⁻³ kinetin and 30 g dm⁻³ sucrose. A 1 % CO₂ supply was found beneficial for the production of cell mass; however, increasing CO₂ concentration to 2.5 and 5 % decreased the biomass accumulation. CO₂ enrichment was not beneficial for saponin production and 1, 2.5, and 5 % CO₂ supply resulted in decrease in saponin accumulation up to 11.6, 19.5, and 50.6 %, respectively.     

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.     

Effect of osmotic pressure on cell growth and production of ginseng saponin and polysaccharide in suspension cultures of Panax notoginseng

Summary The effects of initial osmotic pressure (IOP) on the production of ginseng polysaccharide and ginseng saponin were studied in suspension cultures of Panax notoginseng cells. At higher IOP, the specific saponin production and intracellular carbohydrate storage were increased, while the plant cell volume, the consumption rates of major medium components and the specific cell growth rate were decreased. The specific production of polysaccharide was reduced with an increase of IOP from 4.45 to 5.18 atm, and levelled off at an even higher IOP.     

Bioprocessing of plant cell cultures for mass production of targeted compounds

More than a century has passed since the first attempt to cultivate plant cells in vitro. During this time, plant cell cultures have become increasingly attractive and cost-effective alternatives to classical approaches for the mass production of plant-derived metabolites. Furthermore, plant cell culture is the only economically feasible way of producing some high-value metabolites (e.g., paclitaxel) from rare and/or threatened plants. This review summarizes recent advances in bioprocessing aspects of plant cell cultures, from callus culture to product formation, with particular emphasis on the development of suitable bioreactor configurations (e.g., disposable reactors) for plant cell culture-based processes; the optimization of bioreactor culture environments as a powerful means to improve yields; bioreactor operational modes (fed-batch, continuous, and perfusion); and biomonitoring approaches. Recent trends in downstream processing are also considered. This paper is dedicated to Prof. Dr. Mladenka P. Ilieva on the occasion of her 70th birthday.     

Improved production of ginseng polysaccharide by adding conditioned medium to Panax notoginseng cell cultures

By adding 50% (v/v) filtered culture broth to fresh MS medium, the specific growth rate of Panax notoginseng was increased from 0.046 d–1 to 0.068 d–1, and the polysaccharide production and productivity reached 1.21 g l–1 and 61 mg/(ld), respectively, which were 1.3- and 2.3-fold of the control. Further supplementation of the conditioned medium with sucrose, ammonium, nitrate and phosphate gave a cell density of 13.7 g l–1 and a specific growth rate of 0.086 d–1. Polysaccharide production was 1.65 g l–1 and the productivity was 78 mg/(ld).     

In vitro production of gymnemic acid from cell suspension cultures of Gymnema sylvestre R. Br

Gymnema sylvestre is an important medicinal plant that bears bioactive compound namely gymnemic acids. The present work deals with the optimization of a cell suspension culture system of Gymnema sylvestre for the production of biomass and gymnemic acid, which has anti‐diabetic properties. We investigated the effect of inoculum densities (2.5–20.0 g/L), the strength of the Murashige and Skoog (MS) medium (0.25–2.0), carbon source (sucrose, glucose, fructose, maltose), and the concentration of the sucrose (1–8% w/v) to determine their effects on biomass accumulation and production of gymnemic acid. Overall, 10 g/L of inoculum density, full‐strength MS medium supplemented with 2,4‐dichlorophenoxy acetic acid (2.0 mg/L) and Kinetin (0.1 mg/L), and 3% w/v sucrose was found best for the accumulation of biomass and gymnemic acid content (9.95 mg/g dry weight). The results of the current study will be useful for bioprocess and biochemical engineers for large‐scale production of gymnemic acid in cell culture.     

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.     

Effects of elicitation on the production of saponin in cell culture of Panax ginseng

This study was initiated to investigate the impacts of elicitor concentration and elicitor-adding time on the saponin synthesis and the cell growth of Panax ginseng cell suspensions. Both of the elicitors tested, yeast extract and methyl jasmonate, significantly improved saponin production. The highest additive level of the seven ginsenosides tested was 2.07% (dry weight basis), which was 28-fold higher than that in the control. The optimum time to add either elicitor was found to be on the day of inoculation. The addition of either elicitor did not show as significant an influence on cell growth as on saponin production. It was advisable to remove 2,4-dichlorophenoxyacetic acid (2,4-D) from the medium when methyl jasmonate was used as the elicitor as methyl jasmonate interacts antagonistically with 2,4-D. These results suggest that the addition of an elicitor to ginseng cell suspension cultures could stimulate saponin production.     

Shear stress effects on plant cell suspension cultures in a rotating wall vessel bioreactor

A rotating wall vessel, designed for growth of mammalian cells under microgravity, was used to study shear effects on Taxus cuspidata plant suspension cell cultures. Shear stress, as quantified by defined shear fields of Couette viscometers, improved specific cell growth rates and was detrimental to volumetric product formation rates. Received 5 January 1998/ Accepted in revised form 8 December 1998     

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.     

诱导人参发根的rolC基因植物表达载体构建及其在人参中的表达

根据Slightom等RiA₄TL-DNA序列分析结果 ,设计了一对引物 ,以R_i 质粒DNA为模板 ,利用PCR方法对rolC基因进行了扩增。利用pGEM-T载体对rolC基因进行了克隆和测序。结果 ,克隆的DNA片段序列与报道的ORF12阅读框内的rolC序列一致。将pGEM-T-rolC用限制性内切酶SacI酶切 ,与经SmaI酶切CIAP去磷酸化的pUC19质粒重组 ,经蓝白斑筛选得到正向重组的pUC19-rolC。再用Xbal-SacI双酶切pUC19-rolC与pBI121 ,将rolC基因定向克隆到具有CaMV35S启动子的pBI121表达质粒上 ,构建成植物表达载体pBI-rolC。用pBI-rolC转化农杆菌LBA4404构建成的LBA4404 (pBI-rolC)工程菌转化人参子叶 ,获得发根的表达。经PCR扩增分子检测 ,证明rolC基因确已整合到人参发根基因组中。经对转化的人参发根中单体皂苷含量测定 ,发现发根中含有所检测的 7种人参单体皂苷 ,总皂苷含量达 18.55mg/g。     

岩黄连细胞生长与营养物质消耗的动态学研究

在岩黄连细胞悬浮培养过程中,对培养液pH值,碳源、氮源和磷酸盐含量,以及细胞生物量和生物碱含量进行测定,分析其动态变化过程。结果显示培养液pH值在培养初期降低,后逐渐升高;碳源在培养过程中逐渐被利用,磷酸盐和氮源在培养中期几乎耗尽,其中磷酸盐的消耗速率最快;悬浮细胞的生长周期为20 d左右,第18天细胞鲜重和干重达最大,而第21天脱氢卡维丁和小檗碱的含量最高,分别为8.22mg/L和4.31mg/L。结果表明营养物质(碳、氮和磷)的吸收与细胞生长以及生物碱的合成密切相关,营养元素的相对消耗速率为磷>氮>碳,推测氮和磷是影响岩黄连细胞培养的主要因素。     

Effect of plant growth regulators and medium composition on cell growth and saponin production during cell-suspension culture of mountain ginseng (Panax ginseng C. A. mayer)

We have established cell-suspension cultures of mountain ginseng (Panax ginseng G A. Mayer), and have attempted to increase the yield of saponin by manipulating our processing method and culturing factors (e.g., media strengths; the presence of plant growth regulators or sucrose; ratios of NO⁺ ₃/ NH^- ₄). Maximum biomass yield was obtained in media containing 2,4-D. However, saponin productivity was much higher in a medium comprising either IBA or NAA; 7.0 mg/L IBA was optimal for promoting both cell growth (10.0 g/L dry weight) and saponin production (7.29 mg/g DW total ginsenoside). Although the addition of cytokinins (BA and kinetin) did not affect cell growth, the level of saponin (particularly in the Rb group) was enhanced when the media were supplemented with either 0.5 mg/L BA or 0.5 mg/L kinetin. Half- and full-strength MS media were equally suitable for inducing both biomass as well as saponin production. We also investigated the effect of various concentrations of sucrose and nitrogen, and found that 30 g/L sucrose enhanced biomass yield as well as saponin content However, further increases (i.e., up to 70 g/L) led to a decrease in saponin accumulation and biomass production. Maximum growth and saponin productivity were reported from treatments with an initial nitrogen concentration of 30 mM. In general, the amount of saponin increased when the test media had high NO⁺ ₃/ NH^- ₄ ratios; in fact, saponin production was greatest when nitrate was the sole nitrogen source.     

Towards high-yield production of pharmaceutical proteins with plant cell suspension cultures

“Molecular farming” in plants with significant advantages in cost and safety is touted as a promising platform for the production of complex pharmaceutical proteins. While whole-plant produced biopharmaceuticals account for a significant portion of the preclinical and clinical pipeline, plant cell suspension culture, which integrates the merits of whole-plant systems with those of microbial fermentation, is emerging as a more compliant alternative “factory”. However, low protein productivity remains a major obstacle that limits extensive commercialization of plant cell bioproduction platform. This review highlights the advantages and recent progress in plant cell culture technology and outlines viable strategies at both the biological and process engineering levels for advancing the economic feasibility of plant cell-based protein production. Approaches to overcome and solve the associated challenges of this culture system that include non-mammalian glycosylation and genetic instability will also be discussed.     

Large-scale rotating filter perfusion system for high-density growth of mammalian suspension cultures

Summary A system has been developed for growth and maintenance of mammalian cells in suspension culture at high density. In principle, the maintenance of constant levels of required nutrients coupled with the removal of toxic cell byproducts can support much higher suspension cell densities than may be obtained in conventional spinners. The system consisted of 4- or 40-liter reaction vessels equipped with a vertically supported rotating cylindrical filter. Agitation was provided by the magnetically driven, rotating filter. Fresh medium was supplied at a rate of 10 to 20 ml/h per 10⁹ cells and the expended medium free of cells was withdrawn through the rotating filter. Both pH and dissolved O₂ and CO₂ were monitored and regulated. Walker 256 carcinosarcoma cells have been grown in these reactors to densities 10-to 30-fold greater than that obtained in Bellco spinners. In addition to high cell densities, the yield of cells per liter of medium used was 2- to 3-fold that obtained in the conventional systems. Both 4-and 40-liter versions of this reactor have been operated without the use of antibiotics. The 40-liter reactor also has been modified for chemostat operation. In a single run, for example, the Walker cell density was maintained between 6 and 10×10⁶ cells/ml with a total yield of 8.7×10¹¹ cells from 360 liters of medium.     

The effects of cadmium chloride on secondary metabolite production in Vitis vinifera cv. cell suspension cultures

Background

Plant secondary metabolites are possess several biological activities such as anti-mutagenic, anti-carcinogenic, anti-aging, etc. Cell suspension culture is one of the most effective systems to produce secondary metabolites. It is possible to increase the phenolic compounds and tocopherols by using cell suspensions. Studies on tocopherols production by cell suspension cultures are seldom and generally focused on seed oil plants. Although fresh grape, grape seed, pomace and grape seed oil had tocopherols, with our best knowledge, there is no research on tocopherol accumulation in the grape cell suspension cultures. In this study, it was aimed to determine the effects of cadmium chloride treatments on secondary metabolite production in cell suspension cultures of grapevine. Cell suspensions initiated from callus belonging to petiole tissue was used as a plant material. Cadmium chloride was applied to cell suspension cultures in different concentration (1.0 mM and 1.5 mM) to enhance secondary metabolite (total phenolics, total flavanols, total flavonols, trans-resveratrol, and α-, β-, γ- δ-tocopherols) production. Cells were harvested at two days intervals until the 6^th day of cultures. Amounts of total phenolics, total flavanols and total flavonols; trans-resveratrol and tocopherols (α-, β-, γ- and δ-tocopherols) and dry cell weights were determined in the harvested cells.

Results

Phenolic contents were significantly affected by the sampling time and cadmium concentrations. The highest values of total phenolic (168.82 mg/100 g), total flavanol (15.94 mg/100 g), total flavonol (14.73 mg/100 g) and trans-resveratrol (490.76 μg/100 g) were found in cells treated with 1.0 mM CdCl₂ and harvested at day 2. Contents of tocopherols in the cells cultured in the presence of 1.0 mM CdCl₂ gradually increased during the culture period and the highest values of α, β and γ tocopherols (145.61, 25.52 and 18.56 μg/100 g) were detected in the cell cultures collected at day 6.

Conclusions

As a conclusion, secondary metabolite contents were increased by cadmium chloride application and sampling time, while dry cell weights was reduced by cadmium chloride treatments.     

Effects of non-frozen cold storage on the growth,organogenesis and secondary metabolism of callus cultures

Callus tissues derived from chilling-tolerant herbaceous plant, Atractylodes lancea, Atropa belladonna, Bupleurum falcatum, Dioscorea tokoro, Lithospermum erythrorhizon and Phytolacca americana could be cold-stored at 4°C for three months or more, whereas those from chilling-sensitive herbaceous plants such as Datura innoxia and Perilla frutescens var. crispa and a deciduous tree, Mallotus japonicus, could not survive after cold storage for two to three months. Tobacco callus cultures could be stored at 4°C for two or four months depending on a callus strain. The effect of cold storage on secondary metabolite production varied. Nicotine and betalain production suffered from cold storage of tobacco and Phytolacca americana callus cultures, respectively. However, production of anthocyanin in cultures of Mallotus japonicus and Bupleurum falcatum and shikonin derivatives in Lithospermum erythrorhizon callus was affected very little. Root-forming ability was retained for more than one year in cold-stored callus tissues of Bupleurum falcatum, while the control callus tissues maintained at 25°C completely lost the organogenetic ability six months after the first subculture.     

Alkaloid production by plant cell cultures of Holarrhena antidysenterica: II. Effect of precursor feeding and cultivation in stirred tank bioreactor

Precursor feeding strategy for increasing the yield of conessine, a steroidal alkaloid of Holarrhena antidysenterica, was established in cell suspension culture. A total of 50 mg/L added cholesterol was converted into 43 mg/L of alkaloid, 90% of which constituted the conessine. By applying the precursor feeding policy to the cell suspension culture in modified Murashige and Skoog (MS) medium, a total of 143 mg/L of alkaloid was produced in 8 days. In this way the alkaloid content of the cells was increased more than six times compared to that obtained in the standard MS medium. The steps leading to biotransformation of cholesterol into alkaloids were unaffected by phosphate. The shake flask data were successfully transferred to a bench scale 6-L stirred tank bioreactor in which the specific biosynthetic rate of alkaloid production was 110 mg/100 g dry cell weight per day, about 160 times higher than that of whole plant.