Release of rosmarinic acid by Lavandula vera MM cell suspension in two-phase culture systems

Studies were conducted on the cultivation of Lavandula vera MM cell suspensions in different culture systems for the release of extracellular rosmarinic acid (RA). It was established that during cultivation with Amberlite XAD-4 as a second phase, 6.4% of the total content of RA was adsorbed. When L. vera MM cell suspension was cultivated in an aqueous two-phase system formed by adding 4% polyethylene glycol (MW 20,000) and 7.5% dextran (MW 70,000), 11.8% of the total RA content was released into the top polyethylene glycol phase.     

Enhanced rosmarinic acid production by Lavandula vera MM cell suspension culture through elicitation with vanadyl sulfate

The influence of elicitation on rosmarinic acid biosynthesis by Lavandula vera MM cell suspension culture was investigated using vanadyl sulfate as an abiotic elicitor. It was established that 12 h after treatment with 25 mg/l vanadyl sulfate the rosmarinic acid production was increased up to 3.92 g/l (2.8 times higher compared to the control cultivation). No significant amounts of rosmarinic acid were detected in the culture medium in comparison with its intracellular content. However, it was observed that the extracellular content of rosmarinic acid is 3.3 times higher compared to the control variant (4 h after treatment at elicitor concentration 25 mg/l).     

Radical quenching by rosmarinic acid from Lavandula vera MM cell culture

This study was conducted to evaluate the radical scavenging capacities of extracts and preparations from a Lavandula vera MM plant cell culture with different rosmarinic acid content and to compare them with pure rosmarinic and caffeic acids as well. The methods, which were used are superoxide anion and 2,2'-azino-bis(3-ethylbenzothiazoline-6-sulfonic acid) diammonium salt radicals scavenging assays. Results showed that extracts and preparations from Lavandula vera MM possess strong radical scavengers, as the best both radical scavengers appeared to be the fractions with enriched rosmarinic acid content, obtained after ethylacetate fractioning (47.7% inhibition of superoxide radicals and 14.2 microM 6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid equivalents, respectively). These data reveal the possibilities for application of these preparations as antioxidants.     

Rosmarinic acid production by Lavandula vera MM cell suspension culture: nitrogen effect

The growth of Lavandula vera MM cell suspension and the biosynthesis of rosmarinic acid (RA) were followed during its cultivation in Linsmayer–Skoog media, containing different concentrations of ammonium and nitrate ions. The results showed that cultivation in a medium with 0.09g ammonium ions/l (1/4 of standard medium) ensured intensive growth (16g dry biomass/l) and enhanced biosynthesis of RA (15mg/g dry biomass). Cultivation of L. vera MM cell culture in a medium with 1.2-fold concentration of nitrate ions led to accumulation of 11mg RA/g dry biomass which was twice as much as in the standard Linsmayer–Skoog medium.     

Rosmarinic acid production by Lavandula vera MM cell suspension: the effect of temperature

Lavandula vera MM cell suspension, grown at 28 degrees C in a 3-l bioreactor, produced rosmarinic acid maximally at 3 g l(-1)) though most biomass (33.2 g dry wt l(-1)) was at 30 degrees C.     

Rosmarinic acid by Lavandula vera MM cell suspension: Phosphorus effect

Summary The growth of Lavandula vera MM cell suspension and biosynthesis of rosmarinic acid were followed during its cultivation in Linsmayer - Skoog (LS) medium (containing 170 mg/L KH₂PO₄, control cultivation) and in modified LS media, containing different concentration of KH₂PO₄. Doubled concentration of KH₂PO₄ (340 mg/L) caused an increase in the amount of biosynthesised cell biomass (17 g/L vs 13 g/L for control cultivation) and rosmarinic acid (140 mg/L vs 68 mg/L for control cultivation).     

Rosmarinic acid production by Lavandula vera MM cell-suspension culture

The time courses of growth and rosmarinic acid production by Lavandula vera MM cell suspension were investigated. The uptake of the main nutrients (sucrose, nitrogen, phosphorus, K, Ca, Mg) was followed during cultivation and the data on the physiology of the L. vera MM cell culture are presented. It was established that the cell culture synthesizes rosmarinic acid during the linear phase of growth for a relatively short period (between the 4th and 8th days of cultivation). The influence of sucrose concentration in the nutrient medium on cell growth and accumulation of rosmarinic acid by L. vera MM cell culture was investigated. The results showed that 7% sucrose in the nutrient medium ensured a steady growth of the cell suspension and increased the yield of rosmarinic acid (29.2 g/l dry biomass and 507.5 mg/l rosmarinic acid compared to 13.0 g/l dry biomass and 68.6 mg/l rosmarinic acid for the control cultivation with 3% sucrose). Received: 17 September 1996 / Received revision: 31 January 1997 / Accepted: 1 February 1997     

The influence of phenylalanine on accumulation of rosmarinic and caffeic acids by Lavandula vera MM cell culture

Lavandula vera MM cell suspension culture was grown in Linsmayer-Skoog medium with different concentrations of phenylalanine. Adding phenylalanine to the medium (0.1–0.5 g/l) enhanced accumulation of caffeic acid in parallel with rosmarinic acid. When 0.3 g phenylalanine/l was added, the yield of rosmarinic and caffeic acids reached 87 mg/l and 60 mg/l respectively, compared with 68 mg/l and 4 mg/l in controls (without phenylalanine).     

Production of rosmarinic acid by<Emphasis Type="Italic">Lavandula vera</Emphasis> MM cell suspension in bioreactor: effect of dissolved oxygen concentration and agitation

The relationship between dissolved oxygen (DO) concentration, agitation rate and growth of Lavandula vera MM and rosmarinic acid biosynthesis was investigated in 3 l laboratory bioreactor. Lavandula vera MM cell suspension accumulated the highest amounts of biomass (34.8 g/l) and rosmarinic acid (1870.6 mg/l) on day 12 of cultivation at 50% dissolved oxygen and agitation speed 100 rpm and at 30% dissolved oxygen and agitation speed 300 rpm, respectively.     

Elicitation of rosmarinic acid by <Emphasis Type="Italic">Lavandula vera</Emphasis> MM cell suspension culture with abiotic elicitors

The growth of Lavandula vera MM plant cell suspension culture and rosmarinic acid biosynthesis under elicitation with benzothiadiazole and methyl jasmonate were investigated. Upon elicitation with 50 μM methyl jasmonate, the production of rosmarinic acid was enhanced 2.4-fold (3348 mg/l) compared to the non-elicited cells. The influence of benzothiadiazole on rosmarinic acid biosynthesis was weaker and 12 h after its addition the achieved yields were 20–30% higher compared to the control variant at this time. The influence of both elicitors on rosmarinic acid secretion into the culture medium was also discussed.     

Methyl jasmonate enhanced production of rosmarinic acid in cell cultures of Satureja khuzistanica in a bioreactor

The growing interest in rosmarinic acid (RA), an ester of caffeic acid and 3,4‐dihydroxyphenyl lactic acid, is due to its biological activities, which include cognitive‐enhancing effects, slowing the development of Alzheimer's disease, cancer chemoprotection, and anti‐inflammatory activity. Inspired by the challenge of meeting the growing demand for this plant secondary metabolite, we developed a biotechnological platform based on cell suspension cultures of Satureja khuzistanica. The high amounts of RA produced by this system accumulated mainly inside the cells. To further improve production, two elicitors, 100 μM methyl jasmonate (MeJA) and 40 mM cyclodextrin (CD), were tested, separately and together. MeJA increased RA productivity more than 3‐fold, the elicited cultures achieving an RA production of 3.9 g L^?1 without affecting biomass productivity. CD did not have a clear effect on RA production, and under the combined treatment of MeJA + CD only a small amount of RA was released to the medium. When the cell culture was transferred from a shake flask to a wave‐mixed bioreactor, a maximum RA production of 3.1 g L^?1 and biomass productivity of 18.7 g L^?1 d^?1 was achieved under MeJA elicitation, demonstrating the suitability of S. khuzistanica cell suspensions for the biotechnological production of this bioactive plant secondary metabolite.     

Growth and rosmarinic acid production in cell suspension cultures of Salvia officinalis L.

Rosmarinic acid (RA) is a natural antioxidant produced by cell suspension cultures of sage (Salvia officinalis L.). The growth and production of RA by these cells can be modified by the type of culture medium. Production can be increased 10-fold to attain 6.4 g.1^-1 under optimal conditions. Investigation of kinetics showed that a change in the medium caused shifts in peaks of growth and production, and modifications of the cell metabolism. RA production can be correlated with growth or begins only when growth has stopped.     

Selection of cell lines for the production of rosmarinic acid from cell suspension cultures of Orthosihon stamineus benth

Summary Cell suspension cultures of Orthosiphon stamineus were established from friable calluses produced from leaf pieces of in vitro plantlets that were derived from nodal segments of the mother plants collected from three different geographical locations. Eight lines were eventually selected after seven subculture cycles based on the growth characteristic (plant height) of the plantlets from the three locations: two fast-growing lines (>5.1 cm tall), three intermediate-growing lines (3.1–5.0 cm tall), and three slow-growing lines (<3.0 cm tall). All eight lines grew well in liquid Murashige and Skoog medium supplemented with 4.5 μM 2,4-dichlorophenoxyacetic acid (2,4-D) and 5.4 μM 1-naphthaleneacetic acid (NAA). All cell lines exhibited the same growth pattern but produced different maximum cell biomass when cultured in this medium. The time of harvesting the plant cells from the culture medium and the geographical source of the original plant material were both found to affect the production of rosmarinic acid (RA) in cell cultures. Two cell lines were successfully selected and identified to produce high amounts of RA. These cell lines were a fast-growing cell line from Air Itam, Penang and an intermediate-growing cell line from Relau Agriculture Research Centre, Penang which could produce 5% [(w/w) dry weight] and 4.5% [(w/w) dry weight] of RA, respectively.     

Methyl jasmonate-induced rosmarinic acid biosynthesis in Lithospermum erythrorhizon cell suspension cultures

Summary A dramatic increase in rosmarinic acid (RA) content in cultured cells of Lithospermum erythrorhizon was observed after their exposure to methyl jasmonate (MJ). Preceding the induced RA accumulation, phenylalanine ammonia-lyase (PAL) and 4-hydroxyphenylpyruvate reductase (HPR) activities increased rapidly and transiently, whereas tyrosine aminotransferase (TAT) activity showed only a slight increase. The elicitation activity of MJ was much higher than that of yeast extract (YE) in terms of the induction of PAL and HPR activities, RA accumulation and incorporation of both ¹⁴C-phenylalanine and ¹⁴C-tyrosine into RA. However, the response of the cultured cells to MJ-treatment was slower than that to YE-treatment.Abbreviations 2,4-D 2,4-dichlorophenoxyacetic acid - LS Linsmaier and Skoog - HPR 4-hydroxyphenylpyruvate reductase - PAL phenylalanine ammonia-lyase - TAT tyrosine aminotransferase - MJ methyl jasmonate - YE yeast extract     

Induction of rosmarinic acid biosynthesis in Lithospermum erythrorhizon cell suspension cultures by yeast extract

Summary A transient increase in rosmarinic acid (RA) content in cultured cells of Lithospermum erythrorhizon was observed after addition of yeast extract (YE) to the suspension cultures, reaching a maximum at 24 hr. The highest increase of the RA content (2.5-fold) was obtained when 6-day-old cells in the exponential growth phase were treated with YE. Preceding the induced RA accumulation, phenylalanine ammonia-lyase (PAL) activity increased rapidly, whereas tyrosine aminotransferase (TAT) activity was largely unaffected by the treatment. The incorporation of both ¹⁴C-phenylalanine and ¹⁴C-tyrosine into RA was enhanced in the YE-treated cells, consistent with increased synthesis of the ester.Abbreviations 2,4-D 2,4 dichlorophenoxyacetic acid - PAL phenylalanine ammonia-lyase - TAT tyrosine aminotransferase - RA rosmarinic acid - YE yeast extract     

Development of a helical-ribbon impeller bioreactor for high-density plant cell suspension culture

A double helical-ribbon impeller (HRI) bioreactor with a 11-L working volume was developed to grow high-density Catharanthus roseus cell suspensions. The rheological behavior of this suspension was found to be shear-thinning for concentrations higher than 12 to 15 g DW . L(-1). A granulated agar suspension of similar rheological properties was used as a model fluid for these suspensions. Mixing studies revealed that surface baffling and bottom profiling of the bioreactor and impeller speeds of 60 to 150 rpm ensured uniform mixing of suspensions. The HRI power requirement was found to increase singnificantly for agar suspensions higher than 13 g DW . L(-1), in conjunction with the effective viscosity increase. Oxygen transfer studies showed high apparent surface oxygen transfer coefficients (k(L)a approximately 4 to 45 h(-1)) from agar suspensions of 30 g DW . L(-1) to water and for mixing speeds ranging from 120 to 150 rpm. These high surface k(I)a values were ascribed to the flow pattern of this bioreactor configuration combined with surface bubble generation and entrainment in the liquid phase caused by the presence of the surface baffles. High-density C. roseus cell suspension cultures were successfully grown in this bioreactor without gas sparging. Up to 70% oxygen enrichment of the head space was required to ensure sufficient oxygen supply to the cultures so that dissolved oxygen concentration would remain above the critical level (>/=10% air saturation). The best mixing speed was 120 rpm. These cultures grew at the same rate ( approximately 0.4 d(-1)) and attained the same high biomass concentrations ( approximately 25 to 27 g DW . L(-1), 450 to 500 g filtered wet biomass . L(-1), and 92% to 100% settled wet biomass volume) as shake flask cultures. The scale-up potential of this bioreactor configuration is discussed.     

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     

Production of rosmarinic acid from perfusion culture ofAnchusa officinalis in a membrane-aerated bioreactor

Summary In this study, a perfusion fermentation ofAnchusa officinalis was carried out in a stirred tank bioreactor integrated with an internal cross-flow filter. Bubble-free aeration via microporous membrane fibers was used to provide oxygen. A two-stage culture was successfully conducted in this reactor without filter fouling. In a 17 day fermentation, a cell density of 26 g dw/I and a rosmarinic acid productivity of 94 mg/l day were achieved. This productivity is three times that obtained in a batch culture.     

Continuous production of gluconic acid by immobilized Gluconobacter oxydans cell bioreactor

Summary Living Gluconobacter oxydans cells were attached on fibrous nylon carrier. Free gluconic acid was directly continuously produced in an aerated tubular immobilized-cell bioreactor for at least 6 months, with a volumetric productivity of at least 5 g/lh at 100 g/l substrate glucose and about 80 g/l product gluconic acid concentrations. The highest volumetric productivity in respect to glucose concentration was obtained with 175 g/l glucose, with about 120 g/l product gluconic acid level. With self-directing optimization procedure in respect to maximum product gluconic acid level, productivities as high as about 12–15 g/lh were obtained at relatively high substrate feed rate of 0.166 l/lh and relatively low aeration rate of 0.5 l/lmin. The highest glucose conversion of about 96% was obtained with a long residence time, at the lowest substrate feed rate used at a relatively low aeration rate, resulting however in a significant increase in ketogluconic acid production.