12 beta-Hydroxylation of digitoxin by suspension-cultured Digitalis lanata cells: production of digoxin in 20-litre and 300-litre air-lift bioreactors.

A biotransformation process for the production of digoxin was developed using Digitalis lanata cell suspension cultures. Digitoxin was used as the substrate for biotransformation. Digoxin production was carried out in a variety of vessels, including 1-l exsiccators, 20-l glass reactors and a 300-l air-lift bioreactor. A culture volume of 200 l was established after 28 d and the cells were then cultured semi-continuously in a 300-l bioreactor employing the draw-fill cultivation method. Maximal digoxin production was achieved in an 8% glucose medium with a production optimum after 40-60 h of incubation in the presence of 0.65-0.8 mmol digitoxin per l. Levels of 0.52, 0.53 and 0.60 mmol digoxin per l suspension were achieved in 1-l, 20-l and 300-l vessels, respectively. About 80% of the digoxin produced was found in the bathing medium.     

Kinetic model for biotransformation of digitoxin in plant cell suspension culture ofDigitalis lanata

Batch suspension cultures ofDigitalis lanata plant cell were performed to investigate the biotransformation of digitoxin.Digitalis lanata K3OHD plant cells were used to biotransform digitoxin into deacetyllanatoside C. A kinetic model was proposed to describe cell growth, substrate consumption, depletion of digitoxin, formation and depletion of digoxin and purpureaglycoside A, and formation of deacetyllanatoside C. The digoxin and purpureaglycoside A are intermediates of deacetyllanatoside C formation from digitoxin. Interactions between extracellular and intracellular compounds were considered. The proposed model could accurately predict cell growth, substrate consumption and product synthesis. And it can provide a useful framework for quantitative analysis of biotransformation in a plant cell culture system.     

12β-Hydroxylation of digitoxin by Digitalis lanata cells. Production of deacetyllanatoside C in a 20-litre airlift bioreactor

Digitalis lanata cell lines obtained via cell aggregate cloning have been characterized with regard to their growth and ability to form deacetyllanatoside C from digitoxin. Cell line W.1.4 achieved 12-hydroxylation rates as high as 200 mg/L d. It was thus used in biotransformation experiments on a 20-litre scale. Six fermentor runs were performed, the best of which yielded 13.2 g deacetyllanatoside C.     

Production of C<Subscript>35</Subscript> isoprenoids depends on H<Subscript>2</Subscript> availability during cultivation of the hyperthermophile<Emphasis Type="Italic"> Methanococcus jannaschii</Emphasis>

A series of five progressively saturated C₃₅ isoprenoids has been identified in cell-free extracts of the deep-sea methanogen Methanococcus jannaschii. Production and relative abundance of the isoprenoids were dependent on culture conditions; significant production occurred in a 16-l fermentor (12-l working volume) and a 2.5-l fermentor (2-l working volume) but could not be duplicated in serum bottles. Several factors were investigated and shown not to account for the different production levels, including medium composition, pH, and temperature. However, the interphase mass transfer rate was shown to significantly affect the production of C₃₅ isoprenoids in a fermentor. The structures of the novel isoprenoids were confirmed by hydrogenation reactions and mass spectra of the isoprenoids. Indirect evidence based on genomics and mass spectrometry data implicates head-to-head condensation of farnesyl pyrophosphate (C₁₅) with geranylgeranyl pyrophosphate (C₂₀) as the mechanism for C₃₅ synthesis.Communicated by J. WiegelB.P. Manquin and J.A. Morgan contributed equally to this work.     

Optimisation of culture medium and conditions for alpha-l-Arabinofuranosidase production by the extreme thermophilic eubacterium Rhodothermus marinus

The culture medium for Rhodothermus marinus was optimised on a shake-flask scale by using statistical factorial designs for enhanced production of a highly thermostable alpha-L-arabinofuranosidase (AFase). The medium containing 3.6 g/l birch wood xylan and 8.2 g/l yeast extract yielded a maximum of 110 nkat/ml AFase activity together with 125 nkat/ml xylanase and 65 nkat/ml beta-xylosidase activity. In addition, low levels of beta-mannanase (30 nkat/ml), alpha-galactosidase (0.2 nkat/ml), beta-galactosidase (0.3 nkat/ml), endoglucanase (5 nkat/ml) and beta-glucosidase (30 nkat/ml) were detected in the culture filtrate. Among the various carbon sources tested, birchwood xylan was most effective for the formation of AFase and xylanase activities, followed by oat spelt and beechwood xylans, and xylan-rich lignocelluoses (e.g., starch-free sugar beet pulp and wheat bran). Constitutive levels of enzyme activities were detected when the bacterium was grown on other polysaccharides and low-molecular-weight carbohydrates. A fermentation in a 5-l fermenter (3-l working volume) using the optimised medium yielded 60 nkat/ml AFase associated with 65 nkat/ml xylanase and 35 nkat/ml beta-xylosidase activities. The crude AFase displayed optimal activity between pH 5.5 and 7 and at 85 degrees C. It had half-lives of 8.3 h at 85 degrees C and 17 min at 90 degrees C. It showed high stability between pH 5 and 9 (24 h at 65 degrees C). The combined use of AFase-rich xylanase and mannanase from R. marinus in the prebleaching of softwood kraft pulp gave a brightness increase of 1.8% ISO. To our knowledge, this is the first report on the production of a high AFase activity by an extreme thermophilic bacterium and this enzyme is the most thermostable AFase reported so far.     

Scalable transient gene expression in Chinese hamster ovary cells in instrumented and non-instrumented cultivation systems

Cell expansion, gene transfer and protein production were all executed with a single serum-free, animal protein-free commercial medium designed for suspension-adapted Chinese hamster ovary cells (CHO DG44). This is a most important process to consider for clinical production of recombinant proteins. The transfection with polyethylenimine (PEI) was shown here to be scalable using both stirred-tank bioreactors of 3- and 150-l and novel agitated cultivation vessels (50 ml ventilated centrifuge tubes and 1-l square-shaped glass bottles) that lack any instrumentation. The transient transfections spanned a range of working volumes from 2 ml to 80 l. The maximum transient recombinant antibody yield was 22 mg/l, the highest ever reported for a multiliter transfection in CHO. The transiently expressed protein had the same extent of glycosylation as the same antibody produced from a stably transfected recombinant CHO cell line.     

Nutrition and bioprocess development for efficient biosynthesis of an antitumor compound from marine-derived fungus

An integrated nutrition and bioprocess strategy was developed for improving the biosynthesis of an antitumor compound, 1403C, by a marine-derived fungus, Halorosellinia sp. (no. 1403). First, statistical design strategies were synthetically applied to optimize the nutritional composition. The resulting 1403C production reached 2.07 g/l, which was 143.5 % higher than the original production. However, it only produced 0.44 g/l of 1403C in 5-l bioreactor fermentation. Thus, the operating parameters including culture pH, dissolved oxygen, agitation speed, impeller type and inoculum level were considered to improve the fermentation process, and an effective control strategy for 1403C production by Halorosellinia sp. submerged in a 5-l bioreactor was established. When inoculating 0.22 g/l dry biomass, controlling dissolved oxygen not lower than 30 % during the growth phase but ranging between 30 and 40 % during the stationary phase, using a double-layer six-flat-blade Rushton disc turbine agitated at 400 rpm, keeping short-term low pH and rapid-rising pH with glucose starvation, the highest 1403C production was finally obtained at 1.32 g/l, which was promoted by 200 % compared to before optimization. Fermentation scale-up was finally performed in a 500-l bioreactor, and 1403C production of 1.09 g/l was obtained.     

Overproduction of recombinant human VEGF (vascular endothelial growth factor) in Chinese hamster ovary cells

Vascular endothelial growth factors (VEGFs) are a family of proteins that mediate angiogenesis. VEGF165 is a VEGF-A isoform and has been extensively studied owing to its potential use in therapeutic angiogenesis. This study established Chinese hamster ovary (CHO) cells overexpressing recombinant human VEGF165 (rhVEGF165) protein. The production rate of the established CHO cells was over 80 mg/l of rhVEGF165 protein from a 7-day batch culture process using a 7.5-l bioreactor with a 5-l working volume and serum-free medium. The rhVEGF165 protein was purified to homogeneity from the culture supernatant using a two-step chromatographic procedure that resulted in a 48% recovery rate. The purified rhVEGF165 protein was a glycosylated homodimeric protein with a higher molecular weight (MW) than the protein expressed from insect cells, suggesting that the glycosylation of the rhVEGF165 protein in CHO cells differed from that in insect cells. The purified rhVEGF165 protein in this study was functionally active with a half-maximal effective concentration of 3.8 ng/ ml and specific activity of 2.5 x 105 U/mg.     

酵母菌半连续转化人参皂苷Rb1的条件优化

以单因素实验为基础,通过多因素方差分析实验对人参皂苷半连续转化的条件进行优化,选出最佳条件组合,得到最佳的补料方式,补料浓度为6%,补料体积为24mL,补料周期为12h,在此条件下人参皂苷Rb1生物转化达33.5%左右。在最佳补料条件下进行人参皂苷酵母菌转化,其稳定性好,转化率高,对工业生产有积极的推动作用。     

A comparison of models for predicting slurry production on a pig farm

Three methods of predicting slurry production were compared with the volumes actually produced on a 150 sow breeding and fattening pig unit. The methods were based on (a) feed, water and slurry relationships measured in crated and penned pigs; (b) values given in the literature and used by ADAS to predict slurry outputs from pigs; (c) a method based on the digestibility of feed and of water measured at the actual piggery. Method (a) was not found appropriate because of the high overall water:meal ratio found in the unit (13:1). Method (b) was able to predict dry matter production accurately but underestimated the volume produced unless the ADAS allowance of 0·5 litres pig⁻¹ day⁻¹ for washing water and leaking drinkers was increased to 10 litres. Method (c) was the best method for estimating volume but underestimated dry matter production. Combining the better aspects of methods (b) and (c) allows volume, dry matter production and dry matter concentration to be predicted satisfactorily. The daily movements of slurry from the reception pit were very variable. The use of water meters on pig units is recommended to identify wastage.     

An enzymatic route to produce pyruvate from lactate

A bacterial strain of Acinetobacter sp., which was capable of enzymatic production of pyruvate from lactate, was cultured in a 5-l reactor with a basal salt medium. After 14 h of fed-batch fermentation, 9.56 g l^–1 cell concentration in the broth was obtained with 20 g l^–1 (178 mM) sodium lactate and 4 g l^–1 NH₄Cl in the medium; and the biotransformation ability was 2.51 units ml^–1. The cells were harvested from one reactor and then used for pyruvate production from lactate in the same reactor. l-lactate at a concentration about 527 mM was almost stoichiometrically converted to pyruvate in 28 h. After a total 42 h of cell culture and biotransformation, the transformative yield was about 0.72 g g^–1 pyruvate from lactate and the rate of pyruvate production was calculated as 1.33 g l^–1 h^–1 during the process. The results suggested this simple enzymatic production of pyruvate from lactate should be a promising process and may bring a yield higher than that by microbial fermentation. By this process, the recovery of pyruvate from such a simple reaction liquid is relatively easy and inexpensive to perform.     

High rate anaerobic digestion of piggery manure with polyurethane sponges as support material

Summary The use of polyurethane foam sponges to colonize methanogenic associations for the digestion of piggery manure has been investigated. Fermentors containing polyurethane pads as colonization matrix reached a biogas production rate of ca. 2.0 litres per litre reactor per day (30–33°C), hydraulic retention time 7.5 daysl and a biogas yield of 16 litres per litre piggery manure (7–9% TS). Corresponding control fermentors containing no pads reached a gas production rate of 1.3 litres per litre reactor per day and only about 10 litres biogas per litre piggery manure.     

Optimisation of biogas production from manure through serial digestion: lab-scale and pilot-scale studies

In the present study, the possibility of optimizing biogas production from manure by serial digestion was investigated. In the lab-scale experiments, process performance and biogas production of serial digestion, two methanogenic continuously stirred tank reactors (CSTR) connected in series, was compared to a conventional one-step CSTR process. The one-step process was operated at 55 degrees C with 15d HRT and 5l working volume (control). For serial digestion, the total working volume of 5l was distributed as 70/30%, 50/50%, 30/70% or 13/87% between the two methanogenic reactors, respectively. Results showed that serial digestion improved biogas production from manure compared to one-step process. Among the tested reactor configurations, best results were obtained when serial reactors were operated with 70/30% and 50/50% volume distribution. Serial digestion at 70/30% and 50/50% volume distribution produced 13-17.8% more biogas and methane and, contained low VFA and residual methane potential loss in the effluent compared to the one-step CSTR process. At 30/70% volume distribution, an increase in biogas production was also noticed but the process was very unstable with low methane production. At 13/87% volume distribution, no difference in biogas production was noticed and methane production was much lower than the one-step CSTR process. Pilot-scale experiments also showed that serial digestion with 77/23% volume distribution could improve biogas yields by 1.9-6.1% compared to one-step process. The study thus suggests that the biogas production from manure can be optimized through serial digestion with an optimal volume distribution of 70/30% or 50/50% as the operational fluctuations are typically high during full scale application. However, process temperature between the two methanogenic reactors should be as close as possible in order to derive the benefits of serial coupling.     

Optimization of feed conditions in a 2.5-l fed-batch culture using rice oil to improve cephalosporin C production by <Emphasis Type="Italic">Cephalosporium acremonium</Emphasis> M25

Summary Rice oil significantly affected cephalosporin C production in a 2.5-l bioreactor culture of Cephalosporium acremonium M25. To improve cephalosporin C production, the feed conditions of rice oil were optimized. Reducing the feed rate of rice oil improved cephalosporin C production to 1.01 g/l when the consumption rate of rice oil decreased. Overall, under optimal feed conditions in the 2.5-l fed-batch culture, cephalosporin C production increased about four times compared to before optimization.     

Morphology and kinetics studies on cephalosporin C production by Cephalosporium acremonium M25 in a 30-l bioreactor using a mixture of inocula

AIMS: In this study, the relationship between morphology and cephalosporin C (CPC) production in a 30-l bioreactor culture of Cephalosporium acremonium M25 using a 3:7 seed mixture was investigated. In addition, the kinetic model was established and applied. METHODS AND RESULTS: CPC production was performed in a 30-l bioreactor using a 3:7 seed mixture. It was recognized that a 3:7 seed mixture was able to reduce lag phase and enhance CPC production. The maximum CPC production and cell mass were 1.96 and 81.5 g l-1 respectively. Through a morphology study by observation using image analysis, it was concluded that changes of morphological features predicted the progressive production of CPC and that a morphology study could be useful in monitoring the CPC fermentation by C. acremonium M25. In the kinetics study, a kinetic model of CPC fermentation was developed and applied. The proposed model could adequately describe the fermentation of C. acremonium M25 in a 30-l bioreactor. CONCLUSIONS: CPC productivity was improved by using a 3:7 seed mixture in a 30-1 bioreactor. The changes in morphological features showed a very similar tendency with CPC production. A kinetic model of CPC fermentation was successfully established. SIGNIFICANCE AND IMPACT OF THE STUDY: The results of the present study suggest that the use of a 3:7 seed mixture inocula has considerable possibilities for improving CPC productivity if applied to industrial scale fermentations. Through morphology and kinetics study, the kinetic model to describe the morphological differentiation and CPC production by C. acremonium M25 was established.     

Comparison of air-lift and stirred tank reactors for itaconic acid production by Aspergillus terreus

In a 2-l stirred tank reactor (STR), maximum production rate ofitaconic acid was 0.48g/l.h , for an agitation rate of 400 rpm andan aeration rate of 0.5 vvm. In an air-lift reactor (ALR) themaximum production rate was 0.64 g/l.h at an O supply rate of0.41 l O /l. min. Power input per unit volume which gave themaximum production rates for STR and ALR were 1180 and 542 W/m 3,respectively. If O -enriched air was used in place of air for ALR,the corre-sponding power input per unit volume was decreased to 34W/m 3 . ALR requires less power input per unit volume in comparisonwith that of STR whether therefore air or O -enriched air is used.ALR would be a suitable bioreactor for a large production of itaconicacid.     

Optimization of culture conditions for production of the anti-tubercular alkaloid hirsutellone A by Trichoderma gelatinosum BCC 7579

AIMS: This work aimed to optimize the culture conditions for production of a novel and potent anti-tubercular alkaloid, hirsutellone A, by the saprophytic soil fungus Trichoderma gelatinosum BCC 7579. METHODS AND RESULTS: The fungus was initially cultured in shake flasks at 25 degrees C in the potato dextrose broth (PDB) supplemented with various carbon and nitrogen sources and mineral salts to select suitable medium for mycelial growth and hirsutellone A production. Cultivation conditions were further optimized by adjusting initial pH and changing temperature levels to maximize the production of hirsutellone A. The optimal condition that increased the production of hirsutellone A from 19.04 mg l(-1), obtained from basal condition, to 610.55 mg l(-1) and reduced the cultivation time from 40 to 6 days was to cultivate in a shaker at 200 rev min(-1) at 25 degrees C in PDB plus 20 g l(-1) soluble starch, 10 g l(-1) peptone and 2.5% (v/v) salt solution with initial pH of 7. Production of hirsutellone A in larger-scale using a 5-l batch fermenter was also completed yielding 958 mg l(-1) of hirsutellone A within 6 days. CONCLUSIONS: The suitable culture conditions for hirsutellone A production by T. gelatinosum BCC 7579 was the cultivation in 5-l fermenter at 25 degrees C in PDB plus 20 g l(-1) soluble starch, 10 g l(-1) peptone and 2.5% (v/v) salt solution with an initial pH of 7. SIGNIFICANCE AND IMPACT OF THE STUDY: The production of hirsutellone A in a fermenter to obtain a high yield and reduce an incubation period will become very useful in anti-tubercular drug development process in the future.     

Wet oxidation pretreatment for the increase in anaerobic biodegradability of newspaper waste

Wet oxidation was investigated for its process performance on methane fermentation of newspaper waste. The mechanisms of solubilization of newspaper waste were investigated using the following criteria: destruction of total COD (TCOD), production of soluble COD (SCOD), production of volatile fatty acids, production of soluble carbohydrates, production of soluble lignin derivatives (SLD), production of furan (F) and destruction of lignin and cellulose. Wet oxidation was carried out at 170, 190, and 210 degrees C, with a retention time of 1 h. The highest removal efficiencies of TCOD and cellulose were achieved at 210 degrees C, approximately 40% and 69% were destroyed, respectively. On the other hand, highest lignin removal efficiency was achieved at 190 degrees C in which approximately 65% was removed. Batch methane fermentation tests were performed in 2-l glass bottles filled with the wet oxidized newspaper samples. Methane fermentation of newspaper pretreated at 190 degrees C gave the highest CH(4) conversion efficiency (59% of the initial TCOD was recovered as CH(4) gas). Anaerobic cellulose removals varied from 74% to 88%.     

Influence of temperature on Biogas Production from Pistia stratiotes

Pistia stratiotes, an aquatic weed, was investigated as a substrate for biogas production. Experiments were carried out as batch runs in laboratory-scale digesters with the addition of inoculum (digested cattle manure). Gas yields were in the range of 533–707 litres kg⁻¹ VS (STP), respectively, 21–28 litres kg⁻¹ fresh weight of P. stratiotes, with 30 days digestion time at temperatures of 29·5, 33·0 and 37·5°C. The average methane content was 58–68%. Due to its high biodegradability (approximately 83–99% of VS) Pistia stratiotes is very suitable as a substrate for biogas production.