High-density culture of recombinant Chinese hamster ovary cells producing prothrombin in protein-free medium

A recombinant CHO cell line, CHO2DS, was immobilized on porous microcarrier Cytopore 1 and cultivated in 1 l modified Super-spinner and 2 l stirred tank bioreactor with the perfusion of a low-cost chemically defined protein-free medium DF6S. CHO2DS cells could enter into the inner space and grew both in the inner space and on the surface of Cytopore 1 in DF6S and produced prothrombin at 22 mg l^–1 after 10 days. From a seeding density of 5.7 × 10⁵ cells ml^–1, the highest viable cell density of CHO2DS was 1.12 × 10⁷ cells ml^–1.     

Development of a serum-free culture medium for the large scale production of recombinant protein from a Chinese hamster ovary cell line

A serum-free medium, WCM5, has been developed for the large scale propagation of CHO (Chinese hamster ovary) cells which express recombinant protein using dihydrofolate reductase as a selectable marker. WCM5 was prepared by supplementing Iscoves medium without lecithin, albumin or transferrin with a number of components which were shown to benefit growth. WCM5 medium contained 5 mg l^–1 human recombinant insulin (Nucellin) but was otherwise protein-free. CHO 3D11^* cells which had been engineered to express a humanised antibody, CAMPATH^*-1H, were routinely grown using serum-containing medium. From a seeding density of 10⁵ cells ml^–1, cells grown in static culture with serum reached a maximal cell density of 6.5×10⁵ cells ml^–1 after 6 days in culture and produced a maximal antibody concentration of 69 mg l^–1 after 11 days in culture. CHO 3D11^* cells grown with serum were washed in serum-free medium then cultured in WCM5 medium. Following a period of adaptation the cell growth and product yield was superior to that achieved with serum-containing medium. CHO cells producing CAMPATH-1H grown in an 8000 l stirred bioreactor seeded with 2×10⁵ cells ml^–1 reached a maximal viable cell density of 2.16×10⁶ cells ml^–1 after 108 h in culture and a maximal antibody concentration of 131.1 mg l^–1 after 122 h in culture.Abbreviations CHO Chinese hamster ovary - dhfr dihydrofolate reductase - dhfr dihydrofolate reductase deficient - MTX methotrexate - H hypoxanthine - T thymidine - T/V trypsin versene - F12 Hams F12 medium - NEAA non essential amino acids     

Propagation ofSpodoptera frugiperda cells (Sf9) and production of recombinant proteins with the baculovirus expression system using improved spinner flasks with membrane aeration

Summary It has been shown that the growth of Spodoptera frugiperda cells is significantly reduced or ceased under oxygen limiting culture conditions. This paper describes the use of a new membrane-aerated spinner flask which was compared to conventional surface-aerated spinner flasks with regard to growth of the insect cell line Sf9 and recombinant protein production after infection with baculovirus. Using a commercially available serum-free culture medium Sf9 cells reached highest cell densities (3×10⁶ ml^–1) in the membrane-aerated spinner flask. Production of recombinant protein was also influenced by the oxygen supply. In the membrane-aerated spinner flask and in a surface-aerated spinner flask with reduced filling volume more than 20000 U ml^–1 of a recombinant interleukin-2 variant were accumulated whereas only 100 U ml^–1 were produced in a surface-aerated spinner flask with insufficient oxygen supply. Sufficient oxygenation appears to be essential for proliferation of Sf9 cells as well as recombinant protein production after infection with baculovirus. Membrane oxygenation allows sufficient oxygen supply at high cell density and an at least 2.5 fold higher filling volume per spinner unit.     

Serum-free production of a chimeric E-selectin-IgG protein from 1 to 100 l scale: Repeated batch cultivation versus continuous spin filter perfusion

On inflamed endothelium the cell surface protein E-selectin isexpressed which supports the initial process of attachment –capturing and rolling of leukocytes. A recombinant CHO cell linesecreting a soluble E-selectin-IgG chimera was cultivated competitively under serum free conditions in three different bioreactor systems: a 1 l Super-Spinner, a 2 l stirred tank bioreactor equipped with a spinfilter, and a 100 l stirred tankbioreactor. In the smallest system 25.4 mg E-selectin-IgG wereproduced in 62 days using a repeated batch process whileachieving a maximal viable cell density of 3.7 × 10⁶ cells ml^-1. Using continuous perfusion mode a total amount of35.2 mg were produced with a maximal viable cell density of1.65 × 10⁷ cells ml^-1 in the 2 l bioreactor within 29 days. Large scale cultivation in a 100 l stirred tankbioreactor yielded 105.6 mg in three batches with a maximal viable cell density of 9.7 × 10⁵ cells ml^-1 within 15 days. After removal of the cells by continuous centrifugation and a depth filter clearance step, the supernatants were concentrated via ultra filtration. Purificationwas performed by affinity chromatography with rProtein A. Integrity of the E-selectin-IgG protein was checked with SDS PAGE. Its activity was verified in a cellular adhesion assay performed with HL-60 cells and a recombinant CHO cell line expressing membrane-anchored E-selectin constitutively, and E-selectin expressing HUVECs, respectively. Soluble E-selectin-IgG was used to block adhesion to these cell layerscompetitively. A concentation of 18.8 and 37.5 g ml^-1was sufficient to reduce the amount of adhering HL-60 cells to 50% on CHO and HUVEC layers, respectively.     

A low-cost chemically defined protein free medium for a recombinant CHO cell line producing prothrombin

A chemically defined protein free medium, DF6S, was developed for the cultivation of a recombinant Chinese hamster ovary cell line (CHO2DS) producing human prothrombin in suspension batch culture. DF6S was formulated by optimizing DME/F12 with amino acids and supplementing the optimized DME/F12 with aurintricarboxylic acid, ethanolamine, ferric sulfate, Pluronic F68, putrescine and sodium pyruvate. From a seeding density of 2.3 × 10⁵ cells ml^–1, CHO2DS cells grown in suspension in DF6S medium reached a maximal cell density of 1.92 × 10⁶ cells ml^–1 with an accumulated prothrombin concentration of 16.7 mg l^–1 after 6 days in culture.     

Establishment of callus and cell suspension cultures from Gypsophila paniculata leaf segments and study of the attachment of host cells by Erwinia herbicola pv. gypsophilae

Callus and cell suspension cultures were initiated from leaf segments of G. paniculata. Fresh and dry weights measurements of callus showed that callus growth was optimal on MS medium supplemented with 1.0 mg l^–1 2,4-dichlorophenoxyacetic acid (2,4-D) and 0.2 mg l^–1 benzyladenin (BA). Calli cultured on this medium, showed a two-fold increase in fresh weight by the fourth week of incubation. The initiated hard green callus was repeatedly subcultured on MS medium containing increasing concentrations of 2,4-D in order to increase its friability. The friable callus was then used for establishment of a cell suspension culture. Maximum growth of the suspension culture was on medium supplemented with 1.0 mg l^–1 2,4-D and 0.2 mg l^–1 BA.The suspension culture was used for studying plant host attachment in both electron and light microscopy. Upon infection with E. herbicola, plant cells showed aggregate formation within 24 h of infection. In the presence of the pathogenic Ehg,the number of aggregates formed was 342 aggregates ml^–1, in the presence of the non-pathogenic Ehg154 aggregates ml^–1 and in the control 115 aggregates ml^–1. These results show that the pathogenic strain causes formation of cell aggregates 5.8 times greater than the non-pathogenic one. Based on these results, it can be hypothesized that bacterial cells of the pathogenic strains bind to the plant cells and may form a bridge for attachment of plant cells to one another. Observations by electron microscope show that bacterial cells do attach to plant cells and that this attachment might be via formation of a bridge between the bacteria and the plant cell.     

Effect of microbial concentration on biodegradation rates of phenols

Summary Biodegradation rates of 12 phenols were measured with respect to acclimated microbial biomass ranging from 2.3×10⁴ to 2.3×10⁸ cells/l. Rates ranged between 0.02 mg l^–1 day^–1 for 1.6 mg/lp-bromophenol exposed to 2.3×10⁴ cells/l and 1.41 mg l^–1 day^–1 for 3.2 mg/lp-methylphenol exposed to 2.3×10⁸ cells/l. Generally, rates for all phenols were first-order in substrate concentration and zero-order in biomass concentration. Bromophenol biodegradation was preceded by lag periods of varying lengths and to a small extent the rate was dependent on microbial biomass. Results from this study suggest chemical biodegradation generally exhibits pseudo-first-and occasionally, second-order kinetics.     

Suspension culture of gametophytes of transgenic kelp in a photobioreactor

Transgenic Laminaria japonica gametophytes producing a recombinant tissue-type plasminogen activator (rtPA) protein, which is an effective third-generation thrombolytic agent for acute myocardial infarction (AMI), were cultured in an illuminated bubble column bioreactor. A maximum final dry cell weight of 1120 mg l⁻¹ was obtained in batch culture with an initial dry cell weight of 126 mg l⁻¹ and with aeration rate of 1.2 l air min⁻¹ l⁻¹ culture, nitrate at 1.5 mM and phosphate at 0.17 mM. The yield of rtPA was 56 μg g⁻¹ dry cell wt. This is the first report regarding cultivation of a transgenic macroalga in a bioreactor.Revisions requested 27 January 2005 and 14 April 2005; Revisions received 6 April 2005 and 17 May 2005     

Optimisation of the cell release from immobilised cells of Bacillus simplex cultivated in culture media enriched with Cd2+: influence of Cd2+, inoculum size, culture medium and alginate beads characteristics

Calcium alginate beads were used to entrap a Bacillus sp. that has the ability to biosorb cadmium. During the batch incubation of alginate beads in a `rich' or a `poor' liquid medium, cell release out of the beads was noticed with a lag phase which was inversely proportional to the inoculum size (2×10⁷ or 2×10⁸ cells ml^–1 alginate), to the medium content, and proportional to the alginate concentration (10 or 15 g l^–1) and to the cadmium concentration (1, 5 or 10 mg l^–1). In addition, the cell release occurred more quickly when the medium was renewed. When the concentration was below 5 mg l^–1, the alginate matrix seemed to protect the bacteria against Cd²⁺ toxicity.     

Enhanced antibody production associated with altered amino acid metabolism in a hybridoma high-density perfusion culture established by gravity separation

A high density hybridoma perfusion culture was established by separating and recycling cells from the product stream to the reactor using a simple external sedimentation-based separator — an inclined modified Erlenmeyer flask. After 3 weeks, when the optimal perfusion rate of 1.0 day^–1 had been reached, viable cell density stabilized at around 10×10⁶ cells ml^–1, a level five times that obtained by simple batch culture. The efficiency of the separator was enhanced by cell flocculation. Specific antibody productivity, which was initially 0.4 g 1×10⁶ cells^–1 h^–1, decreased to half that value while cell density was increasing, but recovered to the initial level when the culture finally stabilized at a high cell density. During the final phase, when viable cell density and specific antibody production were high, there was a marked shift in metabolism. Consumption of the two most important substrates for energy generation, glucose and glutamine, caused their broth concentrations to decrease to 1.5 mM and 1 mM, respectively, from input medium concentrations of 25 mM and 10 mM, respectively. At the same time there was an increase in the specific production of glycine and aspartate, their broth concentrations reaching 1.5 mM and 0.02 mM, respectively. We suggest that this shift in metabolism results in enhanced production of ATP from glutamine. The specific glucose consumption and lactate production also indicate that there is a shift to more energy efficient metabolism. The mechanism whereby this leads to enhanced specific antibody production remains to be elucidated. Nevertheless, the combination of high cell density and enhanced productivity obtained with the present perfusion culture resulted in a high monoclonal antibody production –100 mg l^–1 d^–1.     

The cell composition of Nannochloropsis sp. changes under different irradiances in semicontinuous culture

Nannochloropsis sp. was grown semicontinuously with a rate of daily renewal of the culture media of 40% of the volume of the culture under different irradiances (40, 60, 80, 220 and 480 mol quanta m^–2 s^–1). Under the conditions tested, light saturation was achieved at 220 mol quanta m^–2 s^–1 with no significant increase in steady-state cell density or of dry weight productivity with higher irradiance, reaching values of 115 × 10⁶ cells ml^–1 and 375 mg l^–1 day^–1 respectively. C/N ratios clearly indicated the point of light saturation, decreasing with increasing irradiance for light-limited conditions and increasing for light-saturated conditions. Under light-limited conditions, an increase in the irradiance produced an increase in the protein percentage of the organic fraction to the detriment of lipids and carbohydrates, while small changes were recorded under light-saturated conditions. The degree of unsaturation of fatty acids was lower with increasing irradiance, with a three-fold decrease of the percentage of total n–3 fatty acids, from 29 to 8% of total fatty acids, caused mainly by a decrease of eicosapentaenoic acid (EPA) (20:5n–3). The microalga reached its maximal value of dry weight productivity (375 mg l^–1 day^–1), EPA productivity (3.2 mg l^–1 day^–1) and maximal protein content (36% of the organic content) at the point at which light saturation was achieved. Results demonstrate the efficiency of the use of the irradiance for the modification of the biochemical composition of Nannochloropsis sp.     

A reproducible procedure for plant regeneration from seedling hypocotyl protoplasts of Vigna sublobata L.

Viable protoplasts of Vigna sublobata L. were isolated enzymatically from hypocotyls of axenic seedlings. Protoplast yields were dependent upon seedling age, with maximum yields (2.25 ± 0.35 × 10⁶ g fwt^–1) from seedlings aged 6 d. Protoplasts regenerated cell walls and underwent sustained divisions when cultured in either agarose-solidified or liquid K8P medium. The plating density affected the division frequency and plating efficiency; the division frequency (68 ±0 6.0%) was maximum at 4.0 × 10⁴ ml^–1 while plating efficiency was maximum (1.3 ± 0.1%) at 5.0 × 10⁴ ml^–1. Dividing protoplasts developed into microcalli, which produced glossy green compact nodular calli on transfer to 8.0 gl^–1 w/v agar-solidified medium containing MS salts, B5 organic components, 30 g l^–1 sucrose, NAA (0.2–0.5 mg l^–1), zeatin riboside (0.5–2.0 mg l^–1) and GA₃ (0.5–1.0 mg l^–1). These calli, after sub-culture on the same medium, produced shoot buds which underwent elongation following transfer of tissues to 6.0 g l^–1 agar-solidified B5 medium containing 30g l^–1 sucrose, IBA (0.01 mg l^–1) and BAP (1.0 mg l^–1). Elongated shoots developed roots after transfer to 8.0g l^–1 agar-solidified, hormone-free MS medium with 30 g l^–1 sucrose.Abbreviations IAA indole-3-acetic acid - IBA indole-3-butyric acid - BAP 6-benzyladenine or benzylaminopurine - B5 medium after Gamborg et al (1968) - 2,4-D 2,4-dichlorophenoxyacetic acid - GA³ gibberellic acid - 2,i-P 6-(--dimethylallylamino) purine - MS medium after Murashige and Skoog (1962) - NAA 1-naphthaleneacetic acid     

Cells of <Emphasis Type="BoldItalic">Candida utilis</Emphasis> for <Emphasis Type="BoldItalic">in vitro</Emphasis> (<Emphasis Type="BoldItalic">R</Emphasis>)-phenylacetylcarbinol production in an aqueous/octanol two-phase reactor

(R)-Phenylacetylcarbinol (PAC), a pharmaceutical precursor, was produced from benzaldehyde and pyruvate by pyruvate decarboxylase (PDC) of Candida utilis in an aqueous/organic two-phase emulsion reactor. When the partially purified enzyme in this previously established in vitro process was replaced with C. utilis cells and the temperature was increased from 4 to 21 °C, a screen of several 1-alcohols (C4–C9) confirmed the suitability of 1-octanol as the organic phase. Benzyl alcohol, the major by-product in the commercial in vivo conversion of benzaldehyde and sugar to PAC by Saccharomyces cerevisiae, was not formed. With a phase volume ratio of 1:1 and 5.6 g C. utilis l⁻¹ (PDC activity 2.5 U ml⁻¹), PAC levels of 103 g l⁻¹ in the octanol phase and 12.8 g l⁻¹ in the aqueous phase were produced in 15 h at 21 °C. In comparison to our previously published process with partially purified PDC in an aqueous/octanol emulsion at 4 °C, PAC was produced at a 4-times increased specific rate (1.54 versus 0.39 mg U⁻¹ h⁻¹) with simplified catalyst production and reduced cooling cost. Compared to traditional in vivo whole cell PAC production, the yield on benzaldehyde was 26% higher, the product concentration increased 3.9-fold (or 6.9-fold based on the organic phase), the productivity improved 3.1-fold (3.9 g l⁻¹ h⁻¹) and the catalyst was 6.9-fold more efficient (PAC/dry cell mass 10.3 g g⁻¹).*Dedicated with gratitude to Prof. Dr. Franz Lingens – “Theo”.     

Enhancement of Sf9 Cells and Baculovirus Production Employing Grace’s Medium Supplemented with Milk Whey Ultrafiltrate

Animal cells can be cultured both in basal media supplemented with fetal bovine serum (FBS) and in serum-free media. In this work, the supplementation of Grace’s medium with a set of nutrients to reduce FBS requirements in Spodoptera frugiperda (Sf9) cell culture was evaluated, aiming the production of Anticarsia gemmatalis nucleopolyhedrovirus (AgMNPV) at a cost lower than those for the production using Sf900 II medium. In Grace’s medium supplemented with glucose, Pluronic F68 (PF68) and yeast extract (YE), the effects of FBS and milk whey ultrafiltrate (MWU) on cell concentration and viability during midexponential and stationary growth phase were evaluated. In spite of the fact that FBS presented higher statistical effects than MWU on all dependent variables in the first cell passage studies, after cell adaptation, AgMNPV polyhedra production was comparable to that in Sf900 II. Batch cultivation in Grace’s medium with 2.7 g l⁻¹ glucose, 8 g l⁻¹ YE and 0.1% (w/v) PF68 supplemented with 1% (w/v) MWU and 3% (v/v) FBS increased viable cell concentration to about 5-fold (4.7×10⁶ cells ml⁻¹) when compared to Grace’s containing 10% (v/v) FBS (9.5×10⁵ cells ml⁻¹). AgMNPV polyhedra (PIBs) production was around 3-fold higher in the MWU supplemented medium (1.6×10⁷ PIBs ml⁻¹) than in Grace’s medium with 10% FBS (0.6×10⁷ PIBs ml⁻¹). This study therefore shows a promising achievement to significantly reduce FBS concentration in Sf9 insect cell media, keeping high productivity in terms of cell concentration and final virus production at a cost almost 50% lower than that observed for Sf900 II medium. C.A. Pereira is recipient of a CNPq fellowship.     

Calli and suspension cultures for biomass production ofEuphorbia characias L. subsp.characias

Summary Friable calli and cell suspension cultures were obtained from leaf segments ofEuphorbia characias L. subsp.characias, in Murashige and Skoog (MS) basal medium supplemented with 1g.l^–1 casein hydrolyzate (CH), 5mg.l^–1 ascorbic acid, 1.0mg.l^–1 2,4-dichlorophenoxyacetic acid (2,4-D) and 0.75mg.l^–1 benzyl adenine (BA). The highest callus specific growth rate (=0.085.day^–1), calculated for 1 year old calli cultures, was obtained with 0.25 mg.l^–1 2,4-D and 0.50mg.l^–1 BA. Suspension cultures started with an inoculum of 8.0×10⁴ cells.ml^–1 in supplemented liquid MS medium, gave a specific growth rate =0.256.day^–1.     

Characterization of a wine-like beverage obtained from sugarcane juice

Two yeasts (Saccharomyces cerevisiae and Saccharomyces cerevisiae var ellipsoideus)were tested for their ability to ferment sugarcane (Saccharum officinarum) juice. In order to do this, time course studies of volatile, fixed, and total acidity, pH, alcohol, total sugars and °Bx were performed and the presence of methanol was tested. The fermentation studies were carried out at 25, 28 and 30 °C and the juice was inoculated with 1 and 5% (v/v) suspensions of both yeasts containing 1 × 10⁸ cells ml⁻¹. Time course studies indicated a similar fermentative pattern at the three temperatures evaluated, hence 25 °C was chosen as the cheapest alternative. The size of the inoculum made no difference in the fermentation. Analyses of the sugarcane juice wine showed the following results: pH, 3.2; alcohol, 10 °GL; total solids, 16.5 g l⁻¹; ash, 1.4 g l⁻¹; total acidity, 5.4 g l⁻¹; volatile acidity, 0.12 g l⁻¹; fixed acidity, 5.3 g l⁻¹ and no methanol was detected. Two additional products were obtained after adding passion fruit juice and roselle (Hibiscus sabdarifa Linn) concentrates. The fruit-flavoured wines were significantly preferred (P ≤ 0.05) over the plain product. These results indicated that the elaboration of wine-like beverages is a good alternative use for sugarcane.     

Improvement of phenylethanoid glycosides production by a fungal elicitor in cell suspension culture of Cistanche deserticola

When, on the 15th day of growth, an elicitor from Fusarium solani was added at 40 mg l^–1 to Cistanche deserticola cell suspension cultures, the contents of echinacoside, acteoside and total phenylethanoid glycosides (PeGs) in cultured cells all increased over the next 27 d by over 100% to 15 mg g^–1 dry wt, 9 mg g^–1 dry wt and 57 mg g^–1 dry wt, respectively. The final biomass (1.3 mg dry wt ml^–1) was not affected.     

Functional expression of full length Limulus Factor C in stably transformed Sf9 cells

Limulus Factor C is a potent antagonist of endotoxin from Gram-negative bacteria. A fusion construct containing full length Factor C has been cloned intoSpodoptera frugiperda Sf9 cell. Stable Sf9 cell transfectants were obtained using Zeocin selection for 2 weeks. The recombinant Factor C (rFC) was secreted into the culture medium at 9 mg l^–1. Both the crude and partially purified rFC were able to detect lipid A at 10 pg ml^–1 in an ELISA-based lipid A binding assay.     

Taxol-induced apoptotic cell death in suspension cultures of Taxus cuspidata

Taxol caused apoptotic cell death of Taxus cuspidata in suspension cultures. Typical morphological and biochemical changes of apoptosis were observed by microscopy and total DNA agarose gel electrophoresis. Taxus cuspidata responded to the added Taxol by increasing the biosynthesis of Taxol. The percentage of apoptotic cells in total cells increased with the concentration of added Taxol. With Taxol added at 10 mg l^–1, the maximum concentration of Taxol produced was 23 mg l^–1, 3 times higher than that of the control culture.     

Enhancement of polyunsaturated fatty acid production by cerulenin treatment in polyunsaturated fatty acid-producing bacteria

When docosahexaenoic acid (DHA)-producing Moritella marina strain MP-1 was cultured in the medium containing 0.5 μ g cerulenin ml⁻¹, an inhibitor for fatty acid biosynthesis, the cells grew normally, but the␣content of DHA in the total fatty acids increased from 5.9–19.4%. The DHA yield of M. marina strain MP-1 cells also increased from 4 to 13.7 mg l⁻¹ by cerulenin treatment. The same effect of cerulenin was observed in eicosapentaenoic acid (EPA)-producing Shewanella marinintestina strain IK-1 grown in the medium containing 7.5 μg cerulenin ml⁻¹, and the cerulenin treatment increased the EPA yield from 1.6 to 8 mg l⁻¹. The use of cerulenin is, therefore, advantageous to increase the content of intracellular polyunsaturated fatty acids (PUFA) in particular PUFA-containing phospholipids in bacterial cells.An erratum to this article can be found at .