Biotransformation of mulberroside A from <Emphasis Type="Italic">Morus alba</Emphasis> results in enhancement of tyrosinase inhibition

Mulberroside A, a glycosylated stilbene, was isolated and identified from the ethanol extract of the roots of Morus alba. Oxyresveratrol, the aglycone of mulberroside A, was produced by enzymatic hydrolysis of mulberroside A using the commercial enzyme Pectinex^®. Mulberroside A and oxyresveratrol showed inhibitory activity against mushroom tyrosinase with an IC₅₀ of 53.6 and 0.49 μM, respectively. The tyrosinase inhibitory activity of oxyresveratrol was thus approximately 110-fold higher than that of mulberroside A. Inhibition kinetics showed mulberroside A to be a competitive inhibitor of mushroom tyrosinase with l-tyrosine and l-DOPA as substrate. Oxyresveratrol showed mixed inhibition and noncompetitive inhibition against l-tyrosine and l-DOPA, respectively, as substrate. The results indicate that the tyrosinase inhibitory activity of mulberroside A was greatly enhanced by the bioconversion process.     

Evaluation of the inhibition of mushroom tyrosinase and cellular tyrosinase activities of oxyresveratrol: comparison with mulberroside A

The inhibitory effects of oxyresveratrol, the aglycone of mulberroside A, on mushroom and cellular tyrosinase activities and melanin synthesis were evaluated. Mulberroside A and oxyresveratrol showed inhibitory activity against mushroom tyrosinase, with oxyresveratrol demonstrating a greater inhibitory effect than that of mulberroside A. Oxyresveratrol and mulberroside A strongly inhibited melanin production in Streptomyces bikiniensis and exhibited dose-dependent inhibition of tyrosinase activity and inhibition of melanin synthesis in B16F10 melanoma cells. However, the compounds exhibited nearly similar inhibitory effects on the activity of cellular tyrosinase and melanin synthesis in murine melanocytes. The inhibition of melanin synthesis by mulberroside A and oxyresveratrol was involved in suppressing the expression level of melanogenic enzymes, tyrosinase, tyrosinase-related protein-1 (TRP-1), and tyrosinase-related protein-2 (TRP-2). These results indicate that the inhibition rate of mushroom tyrosinase might not provide an accurate estimate of the inhibition rate of melanin synthesis in melanocytes.     

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.     

Application of bioreactor systems for large scale production of horticultural and medicinal plants

Automation of micropropagation via organogenesis or somatic embryogenesis in a bioreactor has been advanced as a possible way of reducing costs. Micropropagation by conventional techniques is typically a labour-intensive means of clonal propagation. The paper describes lower cost and less labour-intensive clonal propagation through the use of modified air-lift, bubble column, bioreactors (a balloon-type bubble bioreactor), together with temporary immersion systems for the propagation of shoots, bud-clusters and somatic embryos. Propagation of Anoectochilus, apple, Chrysanthemum, garlic, ginseng, grape, Lilium, Phalaenopsis and potato is described. In this chapter, features of bioreactors and bioreactor process design specifically for automated mass propagation of several plant crops are described, and recent research aimed at maximizing automation of the bioreactor production process is highlighted.     

Effect of scale-up on serpentine formation by Catharanthus roseus suspension cultures

A culture of Catharanthus roseus has been developed that is capable of growth-linked serpentine formation. Two separate cell lines of this culture, C87 and C87N, were grown in air-lift bioreactors of 7, 30, and 80 liter working volume. Good growth was obtained with both cell lines in all vessels, with better growth rates at the higher volumes. In contrast, serpentine formation was very low when either cell line was grown in any of the vessels when compared with shake flasks. The reason for this loss of alkaloid formation does not appear to be associated with either bioreactor type or cell line.     

Customized design of electronic noses placed on top of air-lift bioreactors for in situ monitoring the off-gas patterns

A specially designed electronic nose was coupled to an air-lift bioreactor in order to perform on-line monitoring of released vapors. The sensor array was placed at the top of the bioreactor sensing the headspace in equilibrium with the evolving liquor at any time without the need of aspiration and pumping of gases into a separated sensor chamber. The device was applied to follow the off-gas of a bioreactor with Acidithiobacillus thiooxidans grown on beds of elemental sulfur under aerobic conditions. Evolution was monitored by acid titration, pH and optical density measurements. The electronic nose was capable to differentiate each day of reactor evolution since inoculation within periods marked off culture medium replacements using multivariate data analysis. Excellent discrimination was obtained indicating the potentiality for on-line monitoring in non-perturbed bioreactors. The prospects for electronic nose/bioreactor merging are valuable for whatever the bacterial strain or consortium used in terms of scent markers to monitor biochemical processes.     

Evaluation of the inhibition of mushroom tyrosinase and cellular tyrosinase activities of oxyresveratrol: comparison with mulberroside A

The inhibitory effects of oxyresveratrol, the aglycone of mulberroside A, on mushroom and cellular tyrosinase activities and melanin synthesis were evaluated. Mulberroside A and oxyresveratrol showed inhibitory activity against mushroom tyrosinase, with oxyresveratrol demonstrating a greater inhibitory effect than that of mulberroside A. Oxyresveratrol and mulberroside A strongly inhibited melanin production in Streptomyces bikiniensis and exhibited dose-dependent inhibition of tyrosinase activity and inhibition of melanin synthesis in B16F10 melanoma cells. However, the compounds exhibited nearly similar inhibitory effects on the activity of cellular tyrosinase and melanin synthesis in murine melanocytes. The inhibition of melanin synthesis by mulberroside A and oxyresveratrol was involved in suppressing the expression level of melanogenic enzymes, tyrosinase, tyrosinase-related protein-1 (TRP-1), and tyrosinase-related protein-2 (TRP-2). These results indicate that the inhibition rate of mushroom tyrosinase might not provide an accurate estimate of the inhibition rate of melanin synthesis in melanocytes.     

Improved indirubin production in a two-phase suspension culture of Polygonum tinctorium using dimethylpolysiloxane

Dimethylpolysiloxane (DMPS), used as a second phase in a suspension culture of Polygonum tinctorium, increased indirubin production by up to 259% and 16% in shake flask and air-lift bioreactors, respectively. In the shake flask culture, indirubin production increased by up to 248 mg/l using 90% v/v DMPS (volume of DMPS/volume of medium). In an air-lift bioreactor culture grown at a perfusion rate of 0.05 day–1 the indirubin concentration reached a maximum of 130 mg/l using 50% (v/v) DMPS. For the same DMPS content, the lower indirubin production in an air-lift bioreactor was probably due to the mass transfer limitation of indirubin between the two phases. © Rapid Science Ltd. 1998     

Continuous suspended cell culture of Mentha piperita in cell-recycled air-lift bioreactor

Summary A cell-recycled air-lift bioreactor was studied for its performance in cultivation of Mentha piperita cells producing essential oils. The reactor system sustained a stable operation over 30 days with the aid of a cell settler. The maximum cell concentration reached 50% packed cell volume and it occurred at the dilution rate of 0.27 day^-1. Volumetric productivity of essential oils in this system was substantially higher than that obtainable from batch culture.     

Itaconic acid production using an air-lift bioreactor in repeated batch culture of Aspergillus terreus

Repeated itaconic acid production using an air-lift bioreactor was carried out by three methods—two with cell recycling by means of centrifugation and filtration by a stainless steel filter set inside the bioreactor and one by repeated batch culture without cell recycling. In a flask culture, repeated itaconic acid production was stable for 9 cycles (45 d) and the production rate was 0.47 g/l/h. However, in the air-lift bioreactor, it was difficult to produce itaconic acid in the repeated batch culture with cell recycling for a long period due to a decrease in fluidity resulting from an increase in mycelium concentration. In the method without cell recycling, however, repeated itaconic acid production was stable for 4 cycles (21 d) and the production rate was 0.37 g/l/h.     

Continuous production of human erythropoietin by immobilized recombinant L-929 cells

Recombinant L-929 cells transfected with the human erythropoietin (EPO) gene were immobilized in a macroporous cellulosic support and its derivatives in which charged groups or cell attachment factors were introduced. The immobilized cells were cultured in serum-containing and serum-free media. Comparable production of EPO was observed even in the serum-free medium when a support modified by polyethyleneimine was used for immobilization. The cells immobilized on the supports were cultured in fluidized-bed and inner-loop type air-lift bioreactors for continuous production of EPO. A high cell density of more than 2 × 10⁷ cells/cm³-support and high EPO productivity were achieved and maintained for 50 d through the use of the inner-loop type air-lift bioreactor. The productivity was 13.4-fold higher than that of conventional static cultures in petri-dishes.     

Evaluation of criteria for bioreactor comparison and operation standardization for mammalian cell culture

Development of bioprocesses with mammalian cell culture deals with different bioreactor types and scales. The bioreactors might be intended for generation of cell inoculum and production, research, process development, validation, or transfer purposes. During these activities, not only the difficulty of up and downscaling might lead to failure of consistency in cell growth, but also the use of different bioreactor geometries and operation conditions. In such cases, criteria for bioreactor design and process transfer should be carefully evaluated in order to select appropriate cultivation parameters. In this work, power input, mixing time, impeller tip speed, and Reynolds number have been compared systematically for the cultivation of the human cell line AGE1.HN within three partner laboratories using five different bioreactor systems. Proper operation ranges for the bioreactors were identified using the maximal cell‐specific growth rate (μ_max) as indicator. Common optimum values for process transfer criteria were found in these geometrically different bioreactors, in which deviations of μ_max between cultivation systems can be importantly reduced. The data obtained in this work are used for process standardization and comparability of results obtained in different bioreactor systems, i.e. to guarantee lab‐to‐lab consistency for systems biology approaches using mammalian cells.     

A hybrid bioreactor for high density cultivation of plant cell suspensions

Summary A hybrid bioreactor was developed for the production of secondary metabolites from high density cultivation of plant cell suspensions. Some of the advantages of both air-lift and cell-lift by agitation were combined. The addition of a decanting column also made it possble to run a perfusion system for high density culture or to run a two-stage culture efficiently. Cell growth and the production of berberine from Thalictrum rugosum in the hybrid bioreactor are reported in this paper. A cell density up to 31 g/l was obtained by perfusion without any problems in mixing or loss of cell viability and the specific berberine productivity was comparable to that in shake flasks. The maximum berberine concentration was 88 mg/l at 3 weeks operation and declined thereafter.Offprint requests to: D.-I. Kim     

Application of an airlift bioreactor system for the production of adventitious root biomass and caffeic acid derivatives of Echinacea purpurea

In this study, we evaluated the feasibility of using mass cultivation of the adventitious roots of Echinacea purpurea in balloon type bubble (air-lift) bioreactors to produce caffeic acid derivatives, which have pharmaceutical and therapeutic values. An approximately 10 fold increase in biomass and secondary compounds was observed after 4 weeks of culture in balloon type bubble bioreactors (5 L capacity containing 4 L of half strength MS medium). In addition, a linear relationship was observed between the concentration of biomass and the sucrose and ion consumption rate. Furthermore, the concentration of biomass in the bioreactor culture was found to increase as the conductivity decreased. An inoculum density of 7 g/L FW and an aeration rate of 0.1 vvm were found to be suitable for inducing the accumulation of biomass and secondary metabolites. Of the three caffeic acid derivatives evaluated (caftaric acid, chlorogenic acid, and cichoric acid), the concentration of cichoric acid was the highest (26.64 mg/g DW).     

Itaconic acid production from xylose in repeated-batch and continuous bioreactors

Summary Itaconic acid production from xylose by immobilized Aspergillus terreus TKK 200-5-2 mycelia was optimized both in repeated shake-flask fermentations and in continuous column bioreactors using statistical experimental design and empirical modelling. Using continuous 9-1 scale air-lift bioreactors, a pH of 2.5, aeration rate of 0.6 v/v per minute and residence time of 160 h gave the highest itaconic acid concentration. In air-lift bioreactors a cubic carrier size of 0.5 cm gave a 3.3-fold higher product concentration than 1-cm cubes. Packed-bed column reactors had a higher production rate than air-lift reactors. Offprint requests to: H. Kautola     

新型生物反应器结构研究进展

生物反应器是生物工程的核心设备,其结构的合理性直接决定反应器生物加工的效率。生物反应器的研究一直是生物工程的核心问题之一。随着青霉素的工业化生产,机械搅拌式生物反应器应运而生,此后,随着动植物细胞培养,高等真菌培养,藻类培养等生物过程的发展,人们相应开发了大量的生物反应器,其中以机械搅拌式生物反应器和气升式样生物反应器尤为突出,本文总结了近年来文献报道的新型生物反应器,主要阐述了机械搅拌式和气升式两类生物反应器结构的研究进展,对目前国内外报道的11种新型反应器典型结构进行了总结与分析。     

动物细胞培养用生物反应器及相关技术

动物细胞大量培养是生产生物制品的重要途径,它用到的关键设备是生物反应器。根据培养细胞、培养载体、培养液混合方式的不同,生物反应器主要有搅拌式、气升式、中空纤维式、回转式等,其中搅拌式规模最大。回转式是NASA于20世纪90年代中期开发的一种新型生物反应器,被誉为空间生物反应器,可用于组织工程研究。与生物反应器配套的技术主要有灌注、微载体、多孔微球、转入抗凋亡基因等,可以有效地提高细胞密度,增加生物制品产量,提高质量。今后生物反应器研制主要朝两个方向发展:一是,以高密度培养动物细胞生产蛋白质药物为目的,二是以三维培养动物细胞(主要是人类细胞)再生组织或器官为目的。     

Space bioreactors: their use,their future

The use of bioreactors during space flight is discussed. The major elements of a bioreactor are a culture chamber, sensors, a control unit with feedback, as gas exchange system, a pump, fresh culture medium, and a waste reservoir. Types of bioreactors developed for use in space include the Woodlawn Wanderer 9 apparatus, the Space tissue loss system, rotating wall vessel, dynamic cell culture system and the SBR I. Future development for space bioreactors include improvements for cultivation of mammalian cells and tissue engineering and the transfer of bioreactor technology for earth-bound instruments.     

Using CFD simulations and statistical analysis to correlate oxygen mass transfer coefficient to both geometrical parameters and operating conditions in a stirred-tank bioreactor

Optimization of a bioreactor design can be an especially challenging process. For instance, testing different bioreactor vessel geometries and different impeller and sparger types, locations, and dimensions can lead to an exceedingly large number of configurations and necessary experiments. Computational fluid dynamics (CFD), therefore, has been widely used to model multiphase flow in stirred-tank bioreactors to minimize the number of optimization experiments. In this study, a multiphase CFD model with population balance equations are used to model gas–liquid mixing, as well as gas bubble distribution, in a 50 L single-use bioreactor vessel. The vessel is the larger chamber in an early prototype of a multichamber bioreactor for mammalian cell culture. The model results are validated with oxygen mass transfer coefficient (k_La) measurements within the prototype. The validated model is projected to predict the effect of using ring or pipe spargers of different sizes and the effect of varying the impeller diameter on k_La. The simulations show that ring spargers result in a superior k_La compared to pipe spargers, with an optimum sparger-to-impeller diameter ratio of 0.8. In addition, larger impellers are shown to improve k_La. A correlation of k_La is presented as a function of both the reactor geometry (i.e., sparger-to-impeller diameter ratio and impeller-to-vessel diameter ratio) and operating conditions (i.e., Reynolds number and gas flow rate). The resulting correlation can be used to predict k_La in a bioreactor and to optimize its design, geometry, and operating conditions.     

生物反应器与药用植物毛状根的大规模培养

利用药用植物毛状根培养生产次生代谢产物具有极大的生产潜力,而开发适合毛状根培养的反应器,又是毛状根生产天然产物工业化的关键。本文系统地介绍了各种用于毛状根培养的生物反应器,对通气搅拌式、气升式、超声雾化式等生物反应器各自的特点及优势进行了详细阐述,进一步讨论了各种反应器对于毛状根生长和次生代谢物积累的影响,并提出药用植物毛状根大规模培养的生物反应器在今后的发展方向。