Kinetics of taxol production, growth, and nutrient uptake in cell suspensions of Taxus cuspidata

Cell culture of Taxus cuspidata may represent an alternative to extraction of bark as a source of taxol and related taxanes. Cell suspensions of a cell line of T. cuspidata were grown for 44 days in shake flasks containing B5C2 medium. Throughout the growth cycle, fresh and dry weight accumulation, taxol yield on a dry weight basis, taxol accumulation in the medium, pH and pigmentation variation in the medium, as well as the uptake of sucrose, glucose, fructose, nitrate, and inorganic phosphate from the culture medium were examined. The results showed that the growth was relatively slow (doubling times of 17 and 20 days for fresh and dry weight, respectively), and taxol accumulation in the cells was non-growth related (higher in the stationary phase) and at relatively low levels (up to 4 mug/g of the extracted dry weight). Taxol concentration in the medium had two peaks: one during the early (0.4mug/mL) and another during the late (0.1-mug/mL) parts of the growth cycle. On a volumetric basis, the average total amount of taxol produced during the stationary phase (day 38) was 0.15 mug/mL, of which approximately 66% was in the medium and 34% was in the cells. Total carbohydrate uptake was closely associated with the increase in dry biomass. Sucrose was apparently extracellularly hydrolyzed after the first 6 days of culture; glucose was used before fructose. Nitrate was assimilated throughout the growth cycle, but phosphate was absorbed within the first week of culture. The pH variation showed an initial drop followed by a trend toward alkalinization for most of the growth period. Dark pigmentation in the medium increased progressively, particularly during the stationary phase. (c) 1994 John Wiley & Sons, Inc.     

Azadirachtin production in stirred tank reactors by Azadirachta indica suspension culture

Successful scale-up of Azadirachta indica suspension culture for azadirachtin production was done in stirred tank bioreactor with two different impellers. The kinetics of biomass accumulation, nutrient consumption and azadirachtin production of A. indica cell suspension culture were studied in a stirred tank bioreactor equipped with centrifugal impeller and compared with similar bioreactor with a setric impeller to investigate the role of O₂ transfer efficiency of centrifugal impeller bioreactor on overall culture metabolism. The maximum cell mass for centrifugal impeller bioreactor and stirred tank bioreactor (with setric impeller) were 18.7 and 15.5 g/L (by dry cell weight) and corresponding azadirachtin concentrations were 0.071 and 0.05 g/L, respectively. Glucose and phosphate were identified as the major growth-limiting nutrients during the bioreactor cultivation. The centrifugal impeller bioreactor demonstrated less shearing and improved O₂ transfer than the stirred tank bioreactor equipped with setric impeller with respect to biomass and azadirachtin production.     

补料培养与溶氧控制联合应用对红豆杉细胞培养的影响

为进一步提高红豆杉 (Taxuschinensis (Pilg.)Rehd .)细胞培养过程中紫杉醇的产量 ,采用细胞悬浮培养方法研究了补料培养与溶氧控制联合应用对紫杉醇产量的影响。 5L反应器中补料培养研究表明 ,培养过程中第 16天添加含 2 0g/L蔗糖的补料培养液有利于细胞的生长及紫杉醇的合成。 2 0L反应器中补料培养的研究结果表明 :2 0 %饱和度培养时紫杉醇含量最高 (0 .98mg/gDW) ,但 4 0 %～ 6 0 %溶氧饱和度能提高紫杉醇的产量。进一步研究表明 ,细胞在 6 0 %溶氧饱和度培养 2 0d后转入 2 0 %溶氧饱和度继续培养 12d ,能显著提高紫杉醇产量。补料培养与溶氧控制联合应用时 ,2 0L反应器中红豆杉细胞培养紫杉醇产量可达 18.7mg/L。     

Elicitation kinetics of taxane production in suspension cultures of Taxus baccata Pendula

Methyl jasmonate increased taxane production in suspension cultures of Taxus baccata Pendula. Time course changes of taxane production after methyl jasmonate addition were different from normal kinetics without elicitation. Baccatin III and 10-deacetyl baccatin III were detected first and paclitaxel, 10-deacetyl taxol and cephalomanine followed each other in sequence. Paclitaxel was not a dead-end metabolite.     

Ajmalicine production by cell cultures of Catharanthus roseus: from shake flask to bioreactor

The productivity of a cell culture for the production of a secondary metabolite is defined by three factors: specific growth rate, specific product formation rate, and biomass concentration during production. The effect of scaling-up from shake flask to bioreactor on growth and production and the effect of increasing the biomass concentration were investigated for the production of ajmalicine by Catharanthus roseus cell suspensions. Growth of biomass was not affected by the type of culture vessel. Growth, carbohydrate storage, glucose and oxygen consumption, and the carbon dioxide production could be predicted rather well by a structured model with the internal phosphate and the external glucose concentration as the controlling factors. The production of ajmalicine on production medium in a shake flask was not reproduced in a bioreactor. The production could be restored by creating a gas regime in the bioreactor comparable to that in a shake flask. Increasing the biomass concentration both in a shake flask and in a stirred fermenter decreased the ajmalicine production rate. This effect could be removed partly by controlling the oxygen concentration in the more dense culture at 85% air saturation.     

Enhanced production of podophyllotoxin by Podophyllum hexandrum using in situ cell retention bioreactor

The rhizomes of the rare plant Podophyllum hexandrum contain podophyllotoxin, which is a precursor of the anticancer drugs etoposide and teniposide. Batch cultivation of Podophyllum hexandrum was conducted using optimized medium in a 3 L bioreactor, which resulted in biomass and podophyllotoxin concentrations of 21.4 g/L and 13.8 mg/L in 24 and 26 days, respectively. The batch kinetics was used to identify the mathematical model. The model was extrapolated to identify the nutrient feeding rate (150 mL/d) and substrate concentration (105 g/L) in the incoming feed for nonlimiting and noninhibitory glucose concentration in the cell retention bioreactor. An improvement in cell growth to 53 g/L and intracellular podophyllotoxin accumulation of 48.8 mg/L was achieved in 60 days, when the bioreactor was operated in continuous cell retention cultivation mode.     

Growth of hairy root cultures of strawberry (Fragaria ¥ ananassa Duch.) in three different types of bioreactors

Hairy roots of strawberry were cultivated in three different types of bioreactors: an air-sparged bioreactor (control), a droplet bioreactor and a mist bioreactor. The highest biomass yields (3.7 g dry wt/l) were achieved in the air-sparged and in the mist bioreactor. In the droplet bioreactor the cultivation medium was insufficiently atomized into droplets and nutrient uptake and growth were slower due to uneven wetting of hairy roots.     

Application of self-cycling fermentation technique to the production of poly-beta-hydroxybutyrate

The production of poly-beta-hydroxybutyrate (PHB) by Alcaligenes eutrophus DSM 545 in a cyclone bioreactor was compared using various culture methods: batch, fed-batch, and self-cycling fermentation (SCF) with and without extended periods of nutrient deprivation. SCF is a semi-continuous method that results in a nutrient limitation for every successive generation of cells and, therefore, may have advantages for products whose formation follow secondary metabolite kinetics. Use of the SCF technique without extended nutrient deprivation produced a PHB concentration of 1.2 g L(-1) as 40% of the biomass dry weight. With nitrogen deprivation for 4 or 6 h, the concentration of PHB decreased when compared to the standard SCF technique. However, nitrogen deprivation periods of 8 h resulted in an increase in PHB concentration to 2.7 g L(-1) or 59% of the biomass dry weight. The nutrient cycling may act to repress PHB accumulation during periods of nitrogen deprivation, unless a time threshold has been reached, after which PHB accumulation occurs as in normal batch culture. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 815-820, 1997.     

溶氧水平对红豆杉细胞悬浮培养的影响研究

紫杉醇 (Ｔａｘｏｌ)是源自红豆杉提取物的一种高度衍生化的二萜类化合物 ,临床实验结果表明紫杉醇对于卵巢癌、乳腺癌、胃肠道癌等具有明显的抗肿瘤活性[1] ,因而受到世界各国的广泛关注 ,并已被美国食品与药品管理局 (ＦＤＡ)批准用于卵巢癌与乳腺癌的治疗[2 ] 。到目前为止紫杉醇仍然主要从树皮中提取 ,但由于红豆杉生长缓慢 ,天然资源非常有限 ,加快其替代来源的研究势在必行。利用植物细胞悬浮培养生产紫杉醇作为一种可行的选择 ,近年来取得了较大的进展[3 ,4 ] 。本文研究了摇瓶及 2 0 Ｌ反应器培养过程的溶氧水平对细胞生长及紫杉醇…     

Production of somatic embryos in a helical ribbon impeller bioreactor

Embryogenic cultures of a transformed Eschscholtzia californica cell line were carried out in a 11-L helical ribbon impeller bioreactor operated under various conditions to evaluate the performance of this equipment for somatic embryo (SE) production. All bioreactor cultures produced SE suspensions with maximum concentrations at least comparable to those obtained from flask control cultures ( approximately 8-13 SE . mL(-;1)). However, an increase of the mixingspeed, from 60 to 100 rpm, and low sparging rate ( approximately 0.05 VVM, k(L) a approximately 6.1 h(-;1)) for dissolved oxygen concentration (DO) control yielded poorer quality embryogenic cultures. The negative effects on SE production were attributed mainly to the low but excessive shear experienced by the embryogenic cells and/or embryoforming aggregates. High DO ( approximately 60% of air saturation) conditions favored undifferentrated biomass production and high nutrient uptake rates at the expense of the slower SE differentiation process in both flask and bioreactor cultures. Too low DO (-5-10%) inhibited biomass and SE production. The best production of SE ( approximately 44 SE . mL(-1) or approximately 757 SE . g dw(-1) . d(-1)) was achieved by operating the bioreactor at 60 rpm while controlling DO at approximately 20%by surface oxygenation only (0.05 VVM, k(L) a approximately 1.4 h(-;1)). This production was found to be a biomass production/growth-associated process and was mainly limited by the availability of extracellular phosphate, magnesium, nitrogen salts, and carbohydrates. (c) 1994 John Wiley & Sons, Inc.     

Effect of aggregate size in cell cultures of<Emphasis Type="Italic"> Saussurea medusa</Emphasis> on cell growth and jaceosidin production

Cell suspension cultures of Saussurea medusa were grown in shake flasks and a 5-l stirred tank bioreactor. Biomass and jaceosidin distribution in cell aggregates of different sizes were investigated during the cultivation period. The results showed that on day 10, jaceosidin accumulation showed an increase with increasing size of the cell aggregate to 4 mm in diameter, with the highest jaceosidin accumulation being 12.2 mg/g. An inverse tendency was observed with cell aggregates larger than 4 mm in diameter, with the lowest accumulation being 3.1 mg/g. However, all of the cell aggregates, despite their size, synthesized almost the same amount of jaceosidin at day 12. Oxygen diffusion limitation and cell-cell contact may explain this behavior. In comparison with cells cultivated in shake flasks, decreased biomass and decreased jaceosidin concentration were observed when the cells were cultivated in a stirred tank bioreactor. The sublytic effects caused by the hydrodynamic stress in combination with insufficient nutrients in the bioreactor may cause cell damage.     

Design of a large-scale surface-aerated bioreactor for biomass production using a VOC substrate

The design of a large-scale bioreactor for the production of bacterial biomass adapted to the biodegradation of volatile organic compounds was carried out. The bioreactor model used integrated the microbial kinetics and fluid dynamics described by the compartment model approach. The process conditions and kinetic parameters were adopted from the laboratory experimental study of (León, E., Seignez, C., Adler, N., Péringer, P., 1999. Growth inhibition of biomass adapted to the degradation of toluene and xylenes in mixture in a batch reactor with substrates supplied by pulses. Biodegradation 10, 245-250). The performance of the pulsed-batch stirred bioreactor under surface aeration conditions was simulated for different mixing configurations and conditions such as the impeller diameter, number of impellers, stirring speed, and oxygen pressure. The simulations were used for the cost analysis which resulted in the optimal design of the bioreactor.     

Unstructured models for suspension cultures of Taxus media cells in a bioreactor under substrate-sufficient conditions

For a better understanding of the simulation, optimization, and process control in cell cultures, good kinetic models are necessary for large scale plant cell culture. In this paper, the systematic kinetics of taxol production by Taxus media cell suspension cultures in a stirred 15-L bioreactor under substrate-sufficient conditions and the absence of inducer intervention were studied. A kinetic model of cell growth was established by logistic equation, and kinetic unstructured models of substrate consumption, product synthesis and rheological behavior were constituted, which incorporated energy spilling. These models were verified by comparing the simulation results with those obtained experimentally. These results showed that energy spilling was a key factor that must be considered in constructing unstructured kinetic models of Taxus media cell suspension cultures in a stirred bioreactor under substrate-sufficient conditions. Besides, an optimized operation measure of decreasing energy spilling was proposed. An increase of 17.64% in cell biomass and 14.88% in taxol concentration were obtained when the strategy of limiting added carbon several times was experimentally implemented in a 15-L bioreactor. Results demonstrated that these established models should be helpful in the process prediction and operation optimization to guide the production and amplification of Taxus media cell suspension cultures in a bioreactor.     

Kinetics of xanthan production when NH3-N limits biomass synthesis and glucose limits polysaccharide synthesis

The bacterium Xanthomonas campestris, which synthesizes the commercially important polysaccharide xanthan, was grown aseptically in 1.2 L fermenters using semicontinuous cell culture technique (d' = 0.0035 h-1). The effects of carbon-substrate concentration on xanthan production were investigated at three initial glucose concentrations (Go = 15, 20, 25 g/L). Cell biomass synthesis was nitrogen-limited by use of a chemically defined medium that contained NH3-N as the sole nitrogen source at a concentration where it was exhausted before glucose. A linear relationship between biomass synthesis and NH3-N depletion was observed. This relationship remained valid only until NH3-N exhaustion, after which biomass concentration slowly rose another 20 percent before declining. Another linear relationship was found between xanthan synthesis and glucose uptake. This relationship was unaffected by the disappearance of NH3-N and held through glucose exhaustion. The quasi-stoichiometric yield coefficients obtained for each linear relationship were not affected by G0-. Biomass synthesis kinetics showed no variation with G0 before NH3-N exhaustion; afterwards, cell biomass decline was delayed by increasing G0. Xanthan synthesis kinetics displayed no detectable response to depletion of NH3-N and plateauing of biomass concentration; however, there was a marked slow down in the net rate of xanthan synthesis and a drop in xanthan yield after cell biomass decline became noticeable.     

Enhanced taxol production and release in Taxus chinensis cell suspension cultures with selected organic solvents and sucrose feeding

Suspension culture of Taxus chinensis cells was carried out in aqueous-organic two-phase systems for the production and in situ solvent extraction of taxol (paclitaxel). Three organic solvents, hexadecane, decanol, and dibutylphthalate, were tested at 5-20% (v/v) in the culture liquid. All of these solvents stimulated taxol release and the yield per cell, though decanol and higher concentrations of the other two solvents depressed biomass growth significantly. Ten percent dibutylphthalate was the optimal solvent for improving taxol production and release with minimal cell growth inhibition. The time of solvent addition to the culture also affected taxol production, with the addition during the late-log growth phase being most favorable. By feeding sucrose to the culture near the stationary growth phase, the cell growth and taxol production period was extended from 27 to 42 days. The combining of the two-phase culture and sucrose feeding increased the taxol yield by about 6-fold compared with the single-phase batch culture, to 36.0 +/- 3.5 mg/L, with up to 63% taxol released. This study shows that in situ solvent extraction combined with nutrient feeding is an effective process strategy for production and recovery of secondary metabolites in plant cell suspension culture.     

Improved taxol yield by aromatic carboxylic acid and amino acid feeding to cell cultures of taxus cuspidata

Cell culture of Taxus cuspidata represents an alternative to whole plant extraction as a source of taxol and related taxanes. Feeding phenylalanine to callus cultures was previously shown to result in increased taxol yields, probably due to the involvement of this amino acid as a precursor for the N-benzoylphenylisoserine side chain of taxol. Inthis study, we have examined the effect of various concentrations of phenylalanine, benzoic acid, N-benzoylglycine, serine, glycine, alanine, and 3-amino-3-phenyl-propionic acid on taxol accumulation in 2-year-old cell suspensions of Taxus cuspidata, cell line FCL1F, and in developing callus cultures of T. cuspidata. All compounds tested were included in media at stationary phase (suspensions) or after the period of fastest growth (calli). Alanine and 3-amino-3-phenyl-propionicacid were tested only in callus cultures and did not affect taxol accumulation. Significant increases or trends toward increases in taxol accumulationin callus and suspensions were observed in the presence of phenylalanine, benzoic acid, N-benzoylglycine, serine, and glycine. The greatest increases in taxol accumulation were observed in the presence of various concentrations of phenylalanine (1 mM for callus; 0.05, 0.1, and 0.2 mM for suspensions) and benzoic acid (0.2 and 1 mM for callus and 0.05, 0.1, and 0.2 mM for suspensions). Increases in taxol yields of cell suspensions in the presence of the most effective precursors brought taxol amounts at stationary phase from 2 mug . g(-1) to approximately 10 mug . g(-1) of the extracted dry weight. The results are discussed in termsof possible implications to taxol biosynthesis and in terms of practical applications to large-scale cell culture systems for the production ofthis drug. (c) 1994 John Wiley & Sons, Inc.     

Enhanced production of taxol in suspension cultures of Taxus chinensis by controlling inoculum size

Inoculum size (1.5-6.0g dry weight/l) significantly affected cell growth and accumulation of intracellular and extracellular taxol in Taxus chinensis. A shorter cultivation time and a higher biomass productivity were achieved using inoculum size of 6.0g DW/l. Both the intracellular content and total production of taxol were increased almost 30% with an increase of inoculum size from 1.5 to 3.0g DW/l, while an even higher inoculum size decreased taxol formation. The extracellular taxol concentration was relatively higher (0.091mg/l) at low inoculum sizes of 1.5 and 2.0g DW/l; and in various cases it was less than 25% of the total amount of taxol produced.     

Application of image analysis in the fungal fermentation of Trichoderma reesei RUT-C30

Trichoderma reesei was grown in a stirred-tank bioreactor (STB) and a reciprocating plate bioreactor (RPB) at four different agitation speeds. A semiautomatic image analysis protocol that was developed to characterize the mycelium morphology during the fermentation process based on four morphological types (unbranched, branched, entangled, and clumped microorganisms) was applied to study the effect of agitation on the morphology of T. reesei. It was shown via statistical validation that broth samples used for image analysis represented the whole population of the fungi in the bioreactor. High shear was found to be damaging to T. reesei grown in the STB. The gentler shear produced in the RPB was not detrimental to the microorganism even at higher agitation speed. Better productivity was obtained for T. reesei grown in the STB and the highest productivity, 0.121 IU/mL h, was obtained at 400 rpm. The morphological parameter, the hyphal growth unit, was found to be correlated to the productivity. Understanding the effect of agitation on the morphology and productivity of T. reesei could lead to the design of better bioreactors and the selection of operating conditions of bioreactors to optimize the production of cellulase.     

An integrated bioreactor-expanded bed adsorption system for the removal of acetate to enhance the production of alpha-interferon-2b by Escherichia coli

A stirred tank bioreactor (STB) integrated with an expanded bed adsorption (EBA) system containing anion-exchange resin (Diaion WA30) was developed for in situ removal of acetate to increase the production of α-interferon-2b (α-PrIFN-2b) by Escherichia coli (E. coli). Although the total acetate (9.79 g/L) secreted by E. coli in the integrated STB/EBA system was higher than that in a bioreactor with dispersed resin or a conventional batch bioreactor, cell growth (14.97 g/L) and α-PrIFN-2b production (867.4 μg/L) were significantly improved owing to the high efficiency of acetate removal from the culture. The production of α-PrIFN-2b in the integrated STB/EBA system was improved by 3-fold and 1.4-fold over that obtained in a conventional batch bioreactor and a bioreactor containing dispersed resins, respectively.     

Economized large-scale production of high yield of rAAV for gene therapy applications exploiting baculovirus expression system

BACKGROUND: The versatility of recombinant adeno-associated vector (rAAV) as a gene delivery system is due to the vector's ability to transduce different cell types as well as dividing and non-dividing cells. Large-scale production of rAAV remains one of the major challenges for continued development of pre-clinical and clinical studies, and for its potential commercialization. The baculovirus expression vectors (BEVS) and insect cells represent a potential method to produce rAAV economically at large scale. This technology uses three different BEVs (Bac-Rep, Bac-GFP, and Bac-VP) each at a multiplicity of infection (MOI) of 3. We reported previously the production of rAAV at 40 L scale using a stirred-tank bioreactor (STB). However, production in larger volumes is limited by the stability of the BEVs and amount of BEVs needed to achieve the target MOI of 3 per BEV. Here, the production parameters were optimized and the baculovirus stability was determined. METHODS: The stability of the three types of baculovirus used to produce rAAV was determined for six expansion passages by protein expression analysis. To economize baculovirus, MOI and cell density at time of infection (TOI) were evaluated initially at small scale and then applied to the 10 L scale. RESULTS: An MOI = 0.03 and TOI cell density of 1 x 10(6) cells/mL produced high titer rAAV without comprising yield. To confirm the scalability of the process, rAAV was produced in a 10 L STB using the optimized parameters obtaining a 10x increase in yield ( approximately 1 x 10(14) rAAV DNAse-resistant particles per liter). CONCLUSION: These findings contribute to the process development for large-scale production of rAAV for gene therapy applications and its commercialization.