Uptake of phosphate and its effect on phenylalanine ammonia-lyase activity and cinnamoyl putrescine accumulation in cell suspension cultures of Nicotiana tabacum

The influence of phosphate on the medium-induced formation of cinnamoyl putrescines in cell cultures of Nicotiana tabcum was investigated. Phosphate added to a phosphate-free production medium was completely accumulated in the cells within 24h after inoculation at initial concentrations up to 2 mM. At higher concentrations phosphate was partly accumulated with an intracellular saturation at approx. 0.65 mmol/g dr. wt. equivalent to approx. 45 mM intracellular concentration. Enhanced activities of phenylalanine ammonialyase and increased product levels of cinnamoyl putrescines, induced by cell transfer into phosphatefree medium were suppressed similarly at initial phosphate concentrations of 0.02–0.5 mM. At the same time growth was stimulated.Abbreviations 2,4-D 2,4-dichlorophenoxyacetic acid - fr. wt. fresh weight - dr. wt. dry weight - MS-medium Murashige-Skoog-medium (Murashige and Skoog 1962)     

Influence of accumulated phosphate on culture growth and formation of cinnamoyl putrescines in medium-induced cell suspension cultures of Nicotiana tabacum

The inorganic phosphate of the liquid nutrient medium was completely taken up by freshly inoculated cells of Nicotiana tabacum L. within the first 2 d of culture. Thus intracellular ortho-phosphate concentrations of approx. 0.06 M were accumulated, which upon growth of the cultures were diluted by cell division and subsequent cell growth. Cells from different stages of the growth cycle containing progressively decreasing levels of phosphate were transferred to a phosphate-free medium which normally stimulates the formation of cinnamoyl putrescines. The resulting accumulation of these compounds was inversely correlated with the intracellular phosphate level, whereas a direct linear relationship in the phosphate concentration was found with further growth in the phosphate-free medium.Abbreviations 2,4D 2,4-dichlorophenoxyacetic acid - FW fresh weight - DW dry weight - MS-medium Murashige-Skoog-medium (Murashige and Skoog 1962)     

Formation of putrescine and cinnamoyl putrescines in tobacco cell cultures

A p-fluorophenylalanine- (PFP) resistant cell line of Nicotiana tabacum and wild type cells accumulating high and low levels of cinnamoyl putrescines, respectively, were used to study the formation of putrescine in the biosynthesis of cinnamoyl putrescines. Labelled arginine and ornithine were equally well incorporated into the main conjugates caffeoyl and feruloyl putrescine. Trapping experiments indicated that both amino acids were decarboxylated for putrescine biosynthesis. Nearly all alcohol-extractable radioactivity from the labelled amino acids was found as cinnamoyl putrescines in the PFP-resistant cell line, whereas wild type cells retained significant radioactivity in the amino acids. The enzyme activities of arginine and ornithine decarboxylases in the resistant cell line were increased 3- to 6-fold.     

A novel feeding strategy for enhanced plasmid stability and protein production in recombinant yeast fedbatch fermentation

A novel feeding strategy in fedbatch recombinant yeast fermentation was developed to achieve high plasmid stability and protein productivity for fermentation using low-cost rich (non-selective) media. In batch fermentations with a recombinant yeast, Saccharomyces cerevisiae, which carried the plasmid pSXR125 for the production of beta-galactosidase, it was found that the fraction of plasmid-carrying cells decreased during the exponential growth phase but increased during the stationary phase. This fraction increase in the stationary phase was attributed to the death rate difference between the plasmid-free and plasmid-carrying cells caused by glucose starvation in the stationary phase. Plasmid-free cells grew faster than plasmid-carrying cells when there were plenty of growth substrate, but they also lysed or died faster upon the depletion of the growth substrate. Thus, pulse additions of the growth substrate (glucose) at appropriate time intervals allowing for significant starvation period between two consecutive feedings during fedbatch fermentation should have positive effects on stabilizing plasmid and enhancing protein production. A selective medium was used to grow cells in the initial batch fermentation, which was then followed with pulse feeding of concentrated non-selective media in fedbatch fermentation. Both experimental data and model simulation show that the periodic glucose starvation feeding strategy can maintain a stable plasmid-carrying cell fraction and a stable specific productivity of the recombinant protein, even with a non-selective medium feed for a long operation period. On the contrary, without glucose starvation, the fraction of plasmid-carrying cells and the specific productivity continue to drop during the fedbatch fermentation, which would greatly reduce the product yield and limit the duration that the fermentation can be effectively operated. The new feeding strategy would allow the economic use of a rich, non-selective medium in high cell density recombinant fedbatch fermentation. This new feeding strategy can be easily implemented with a simple IBM-PC based control system, which monitors either glucose or cell concentration in the fermentation broth.     

Effect of Hormone Treatment on Growth Bud Formation and Free Amine and Hydroxycinnamoyl Putrescine Levels in Leaf Explant of Nicotiana tabacum Cultivated in Vitro

Foliar explants of Nicotiana tabacum cv Xanthi n.c. were cultured on four different media: a basal medium, basal medium plus benzyladenine, basal medium plus 2,4-dichlorophenoxyacetic acid (2,4-D), and the basal medium containing both hormones. No differentiation or cell division occurred in leaf explants cultured on the basal medium. Addition of benzyladenine caused the formation of buds on the explants, while 2,4-D caused callus formation and proliferation. Likewise, only callus was formed when explants were cultured on medium containing both hormones, but growth was significantly greater than that of callus grown on a medium containing 2,4-D alone. The levels of amines and hydroxycinnamoyl putrescines were determined in the four types of explants. In nongrowing explants, amines (except an aromatic amine, tyramine) and hydroxycinnamoyl putrescines were always at a low level and only small changes in their concentrations were observed. In callus cultures, amine (except an aromatic amine, phenethylamine) and hydroxycinnamoyl putrescine levels were higher than those found in bud cultures. In all the media, transitory accumulation of aromatic amines occurred after a few days of culture. Higher levels of hydroxycinnamoyl putrescines were attained in callus cultures with a slow growth rate (2,4-D alone) than in callus cultures with a fast growth rate (benzyladenine + 2,4-D). The formation of buds was accompanied by significant changes in putrescine and hydroxycinnamoyl putrescine levels. Increasing levels were found during the first 14 days in culture when cell multiplication was rapid, followed by a sharp decline after 20 days in culture as the rate of cell division decreased and differentiation took place. The relationship among amines, hydroxycinnamoyl putrescines, and cell division and bud formation is discussed.     

Selection for Hyoscyamine and Cinnamoyl Putrescine Overproduction in Cell and Root Cultures of Hyoscyamus muticus

Hairy root cultures of Hyoscyamus muticus have been shown to produce stable levels of tropane alkaloids comparable to those found in whole plants. In contrast, cell cultures of this and other solanaceous species produce only trace amounts of alkaloids but can be used for selection of metabolic variants. We have taken advantage of both systems and the ability to convert between them in vitro in an effort to select for increased production of the tropane alkaloid hyoscyamine. Hairy roots were converted into cell suspensions by addition of 1 mg/L 2,4-dichlorophenoxyacetic acid to Murashige-Skoog medium (T. Murashige and F. Skoog [1962] Physiol Plant 15: 473-497) and screened for resistance to the amino acid analog p-fluorophenylalanine (PFP). Cells that could grow in media containing 400 [mu]M PFP were selected and cloned from single cells. The resistant cells accumulated high levels of cinnamoyl putrescines, which share the same biosynthetic precursors as hyoscyamine. Hairy root cultures were regenerated from both PFP-sensitive and PFP-resistant cells by removing 2,4-dichlorophenoxyacetic acid from the medium. Resistance to PFP continued to be expressed in regenerated roots. Higher levels of hyoscyamine were found in hairy roots regenerated from PFP-resistant cells than were found in controls. We suggest that the precursors overproduced by the PFP-resistant cells can be diverted into the hyoscyamine pathway upon the regeneration of root cultures.     

Albomycin: Studies on fermentation,isolation and quantitative determination

Summary Streptomyces griseus TÜ 6 produces the sideromycin antibiotic albomycin ₂ in concentrations of approximately 1 mg/l. The production depends on the phosphate, iron, and ornithine concentrations in the medium. In optimized conditions, the production of albomycin could be increased to 25 mg/l in a fedbatch fermentation. Isolation and purification could be achieved by reversed-phase and size-exclusion chromatography and preparative high-performance liquid chromatography (HPLC). The detection limit in quantitative determination of albomycin by HPLC was reached at a concentration of 1 g/ml, which was 100 times less sensitive than biological testing, but this method, although time-consuming, was more selective.     

重组尿酸氧化酶发酵工艺优化

目的:优化并获得重组尿酸氧化酶(rUOX)基因工程大肠杆菌BL21(DE3)/pET-32a-uox高密度发酵的工艺参数。方法:在三角摇瓶中进行培养条件的优化实验,分别考察了pH值、接种量、无机盐、碳源、诱导强度等对工程菌生长和重组蛋白表达的影响,得到了优化的发酵条件;在此基础上放大至NBS BIOFLO 110 14 L发酵罐,通过对诱导时机的优化,利用分批补料发酵的方式,使rUOX在高密度培养的条件下得到高表达。结果:在优化的发酵条件下,菌体密度(D600nm)最终达到50以上,相当于20 g/L干重;可溶性rUOX占菌体总蛋白量的45%,其含量达到3.45 g/L。结论:为规模化制备重组黄曲霉尿酸氧化酶奠定了基础。     

Acetate production from lactate and glucose fermentation by Gluconobacter oxydans

Summary The production of acetate from the fermentation of lactate by Gluconobacter oxydans was studied. Batch experiments showed that glucose was the preferred substrate compared to lactate. A fed-batch culture was fed with a mixture of glucose and lactate followed by periodic addition of lactate. The maximum productivity of acetate was 0.16 g/l h but this value decreased during the fedbatch culture due to growth inhibition by acetate.     

Pullulan from peat hydrolyzate fermentation kinetics

The Luedeking-Piret equation was used to fit the kinetic data of pullulan fermentations from peat hydrolyzate substrate. In batch mode, the kinetic parameters m, n, alpha, and beta varied as a function of fermentation conditions: aeration rate, agitation speed, and temperature. In constant-feed fed-batch mode, the parameters Varied according to the feed rates. In peat hydrolyzate medium, the polysaccharide synthesis was strongly growth associated in batch and continuous fermentations but entirely growth associated in fedbatch fermentations. The fed-batch mode of fermentation with an appropriate feed rate is more advantageous with respect to batch and continuous fermentations. Therefore, if the fermentation is started batchwise and then followed by fed-batch mode at a constant feed rate, the overall polysaccharide productivity (g pullulan/L h) is significantly higher than those obtained with batch or continuous fermentations using the same total medium volume.     

Growth monitoring and control in complex medium: a case study employing fed-batch penicillin fermentation and computer-aided on-line mass balancing

To broaden the practicality of on-line growth monitoring and control, its application in fedbatch penicillin fermentation using high corn steep liquor (CSL) concentration (53 g/L) is demonstrated. By employing a calculation method that considers the vagaries of CSL consumption, overall and instantaneous carbon-balancing equations are successfully used to calculate, on-line, the cell concentration and instantaneous specific growth rate in the penicillin production phase. As a consequence, these equations, together with a feedback control strategy, enable the computer control of glucose feed and maintenance of the preselected production-phase growth rate with error less than 0.002 h(-1).     

黑曲霉解磷能力的影响因素及培养条件优化

本文探讨了培养条件下黑曲霉解磷能力的主要影响因素。通过单孢株筛选得到解磷能力较强的菌株Xj-2,其在液体培养基中的解磷能力达到539.90 mg·L^-1。解磷发酵动力学模型模拟发现,其解磷能力在培养的第4 天达到平稳,可作为终止发酵时间。不同磷源培养液中菌株Xj-2的解磷量依次为磷酸钙(539.90 mg·L^-1)>磷酸锌(238.45 mg·L^-1)>磷酸铁(182.64 mg·L^-1)>磷矿粉(71.80 mg·L^-1)>磷酸铝(24.40 mg·L^-1)。通过单因素试验并结合响应面优化,研究了其解磷最佳条件。结果表明: 碳源对Xj-2的解磷能力影响最大,其次是菌群密度和培养液pH。当培养温度35 ℃、转速160 r·min^-1、培养液pH 6.0、氮源(尿素)浓度0.79 g·L^-1、碳源(葡萄糖)浓度10.00 g·L^-1、菌群密度3.8%、培养时间为4 d时,Xj-2的解磷能力最高,为616.81 mg·L^-1。     

Effects of oxygen and ethanol on recombinant yeast fermentation for hepatitis B virus surface antigen production: modeling and simulation studies

A model was formulated to examine the competitive growth of two phenotypes (Leu(+) and Leu(-)) and the product formation with recombinant Saccharomyces cerevisiae strain DBY-745, which contains the shuttle vector pYGH3-16-s with the foreign gene HBsAg (hepatitis B virus surface antigen) as well as experimental fedbatch fermentation data. The important state variables and the process parameters evaluated include (1) the ratio of the plasmid-free cell concentration to the plasmid-containing cell concentration (rho = X(-)X(+)), (2) the expression of human hepatitis B surface antigen g (CH), (3) the glucose consumption (S), (4) the ethanol production (/), (5) the change of working volume (V) in the fermentor, (6) the different specific growth rates of two phenotype cells, and (7) the plasmid loss frequency coefficient (alpha ). These variables and other parameters were carefully defined, their correlations were studied, and a mathematical model using a set of nonlinear ordinary differential equations (ODEs) for fed-batch fermentation was then obtained based on the theoretical considerations and the experimental results. The extended Kalman filter (EKF) methods was applied for the best estimate of these variables based on the experimentally observable variables: rhoV, and g (CH). Each of these variable was affected by random measuring errors under the different operating conditions. Simulation results presented for verification of the model agreed with our observations and provided useful information relevant to the operation and the control of the fedbatch recombinant yeast fermentation. The method of predicting an optimal profile of the cell growth was also demonstrated under the different dissolved oxygen concentrations. (c) 1993 John Wiley & Sons, Inc.     

何首乌愈伤组织的诱导

研究了外植体、光暗条件、植物激素等因子对何首乌愈伤组织诱导的影响 ,以及 6 -BA和何首乌组织提取液对愈伤组织增殖的影响。结果表明 :茎段的愈伤组织诱导优于带侧芽茎段和叶片 ;光照有利于愈伤组织的诱导 ;4因子 4水平的正交实验表明 ,对何首乌茎段愈伤组织诱导的影响 2 ,4 -D >6 -BA >IBA >IAA ,最佳激素搭配是 :MS +2 ,4 -D 2mg L +6 -BA 1mg L +IBA1mg L或MS +2 ,4 -D 2mg L +6 -BA 2mg L +IAA 1mg L ;MS培养基中附加 6 -BA或组织提取液均促进愈伤组织的增殖。     

Control of ammonium concentration in Escherichia coli fermentations

A control system has been devised for the maintenance of stable ammonium concentrations throughout a fedbatch fermentation. The control system is based on an ammonia gas-sensing electrode that monitors a pH-adjusted effluent stream from the fermentor. To overcome the time lag between the fermentor and the electrode, feedback control included metered flows of ammonium to both the fermentor and the electrode vessel. The system was used to study the growth of Escherichia coli B (ATCC 11303) at controlled ammonium concentrations of 5 to 200mM. Apparent specific growth rates, biomass and protein production, and glucose yields were essentially constant from 5 to 170mM. Above 170mM ammonium growth was inhibited. As ammonium concentration decreased from 170 to 5mM, ammonium yields increased from 1 to 24 g cell dry wt/g ammonium utilized. The results demonstrate that control of ammonium concentrations at levels so low that ammonium would be exhausted in batch fermentations can significantly increase overall ammonium yields.     

Effects of dissolved oxygen concentration on biodegradation of 2,4-dichlorophenoxyacetic acid

Batch experiments were conducted to examine the effects of dissolved oxygen concentration on the degradation of 2,4-dichlorophenoxyacetic acid (2,4-D) by an enrichment culture of 2,4-D-utilizing bacteria. A modified Monod equation was found to describe the relationship between the specific growth rate and the concentrations of both the organic substrate and dissolved oxygen. Values for the maximum specific growth rate, yield, and Monod coefficient for growth on 2,4-D were 0.09 h-1, 0.14 g/g, and 0.6 mg/liter, respectively. The half-saturation constant for dissolved oxygen was estimated to be 1.2 mg/liter. These results suggest that dissolved oxygen concentrations below 1 mg/liter may be rate limiting for the biodegradation of chlorinated aromatic compounds such as 2,4-D, which have a requirement for molecular oxygen as a cosubstrate for metabolism.     

Effects of dissolved oxygen concentration on biodegradation of 2,4-dichlorophenoxyacetic acid.

Batch experiments were conducted to examine the effects of dissolved oxygen concentration on the degradation of 2,4-dichlorophenoxyacetic acid (2,4-D) by an enrichment culture of 2,4-D-utilizing bacteria. A modified Monod equation was found to describe the relationship between the specific growth rate and the concentrations of both the organic substrate and dissolved oxygen. Values for the maximum specific growth rate, yield, and Monod coefficient for growth on 2,4-D were 0.09 h-1, 0.14 g/g, and 0.6 mg/liter, respectively. The half-saturation constant for dissolved oxygen was estimated to be 1.2 mg/liter. These results suggest that dissolved oxygen concentrations below 1 mg/liter may be rate limiting for the biodegradation of chlorinated aromatic compounds such as 2,4-D, which have a requirement for molecular oxygen as a cosubstrate for metabolism.     

树状多节孢发酵生产紫杉醇工艺条件的初步研究*

研究了树状多节孢HQD33内生真菌融合子TPF-1摇瓶发酵工艺条件,进行了2.8L和10L通用式机械搅拌罐的发酵试验。结果表明,HQD33适宜发酵工艺条件是:发酵时间16～18d,培养基中蔗糖、苯丙氨酸、醋酸钠、酪氨酸、2,4-二氯苯氧乙酸和亚油酸的加量分别为10g/L、1mg/L、1.5g/L、15mg/L、5mg/L和15mg/L,摇瓶装量为150ml/500ml,在此条件下摇瓶发酵液中紫杉醇平均含量为448.52 g/L; 2.8L和10L罐发酵液中紫杉醇含量达406.95和395.12g/L(平均值)。     

Characterisation of the <Emphasis Type="Italic">Escherichia coli</Emphasis> membrane structure and function during fedbatch cultivation

BACKGROUND: Important parameters during recombinant protein production in Escherichia coli, such as productivity and protein activity, are affected by the growth rate. This includes the translocation of protein over the membrane to gain better folding capacity or reduced proteolysis. To vary the growth rate two techniques are available: fedbatch and continuous cultivation, both controlled by the ingoing feed rate. RESULTS: During fedbatch cultivation, E. coli contains phosphatidylethanolamine, phosphatidylglycerol, cardiolipin and saturated fatty acids in amounts which are stable with growth rate. However, the levels of cardiolipin are very high compared to continuous cultivation. The reason for fedbatch triggering of this metabolism is not known but hypothesised to result from an additional need for carbon and energy. The reason could be the dynamic and sometimes rapid changes in growth rate to which the fedbatch cell has at all times to adjust. The membrane flexibility, essential for translocation of various components, is however to some degree sustained by production of increased amounts of unsaturated fatty acids in phosphatidylglycerol. The result is a functionally stiff membrane which generally promotes low cell lysis and is constant with respect to protein leakage to the medium. At comparatively high growth rates, when the further stabilising effect of cyclic fatty acids is gone, the high level of unsaturated fatty acids results in a pronounced effect upon sonication. This is very much in contrast to the membrane function in continuous cultivation which shows very specific characteristics as a function of growth rate. CONCLUSIONS: The stiff and unchanging fedbatch membrane should promote a stable behaviour during downstream processing and is less dependent on the time of harvest. However, optimisation of protein leakage can only be achieved in the continuously cultivated cell where leakage is twice as high compared to the constant leakage level in fedbatch. If leakage is undesired, continuous cultivation is also preferred since it can be designed to lead to the lowest values detected. Induction at low growth rate (<0.2 h-1) should be avoided with respect to productivity, in any system, since the specific and total protein production shows their lowest values at this point.     

Growth and fermentation patterns of Saccharomyces cerevisiae under different ammonium concentrations and its implications in winemaking industry

AIMS: To study the effects of assimilable nitrogen concentration on growth profile and on fermentation kinetics of Saccharomyces cerevisiae. METHODS AND RESULTS: Saccharomyces cerevisiae was grown in batch in a defined medium with glucose (200 g l(-1)) as the only carbon and energy source, and nitrogen supplied as ammonium sulphate or phosphate forms under different concentrations. The initial nitrogen concentration in the media had no effect on specific growth rates of the yeast strain PYCC 4072. However, fermentation rate and the time required for completion of the alcoholic fermentation were strongly dependent on nitrogen availability. At the stationary phase, the addition of ammonium was effective in increasing cell population, fermentation rate and ethanol. CONCLUSIONS: The yeast strain required a minimum of 267 mg N l(-1) to attain complete dryness of media, within the time considered for the experiments. Lower levels were enough to support growth, although leading to sluggish or stuck fermentation. SIGNIFICANCE AND IMPACT OF THE STUDY: The findings reported here contribute to elucidate the role of nitrogen on growth and fermentation performance of wine yeast. This information might be useful to the wine industry where excessive addition of nitrogen to prevent sluggish or stuck fermentation might have a negative impact on wine stability and quality.