The optimization of serum-free medium for the production of the scu-PA by the addition of algal extracts

The addition of 2.8 g/ml algal extracts enhanced both scu-PA production and cell growth in a serum-free medium, compared to a conventional serum-free medium for the cultivation of recombinant CHO cells. The growth rate and scu-PA production were relatively lower in the serum-free medium than 5% serum containing medium: however, specific scu-PA production rate was higher in the serum-free medium due to the long-term period of cultivation (3.66×10^–4 vs. 2.48×10^–4 IU/cell/day). Overall scu-PA production rate was also greater in an enforced serum-free medium as 25,000 IU/day over 50 d of perfusion cultivation. The conversion ratio of scu-PA to tcu-PA was greatly reduced in the serum-free medium during perfusion cultivation (10% compared to 20% conversion in a serum containing medium).     

Liposome mediated delivery of retinoids and aromatic polyamidines: Effects on growth of tumor cell lines

Ceramic pieces composed of 99.5% Al₂O₃, 3 to 6 mm long, were found to be a good matrix for growth of the human embryonic lung diploid fibroblast, IMR-90 cells. The tissue plasminogen activator (t-PA) was secreted in DME medium containing proteose peptone as a t-PA inducer. In addition, production of t-PA was enhanced by increasing extracellular CaCl₂, from 3.6 to 5.4 mM. In order to eliminate negative feed-back control caused by t-PA produced and thus raise productivity, perfusion cultivation was performed using a ceramic-packed bed column, with a recirculating vessel. The recirculating vessel was used to mix fresh medium with spent medium, and to control dissolved oxygen concentrations in the extracellular environment by stirring. In continuous production using the packed bed column with 2 kg of ceramics (Ø=H=150 mm), increasing dilution rate to 0.5 day^-1 could reduce product inhibition at 3–4×10⁵cells/ml. Cellular productivity of 560 IU/10⁶cells/day was obtained over 40 days and corresponded to the volumetric productivity of 183 IU/ml/day.Abbreviations CBR Ceramic Bed Reactor - Lv Linear Velocity     

Continuous flow cultures of a HeLa cell line as a basis for a steady supply of Rubella virus

A HeLa cell line was propagated in semicontinuous suspension culture, 85 liters final volume, and in continuous flow culture with a volume of 300 ml. or 5 liters in an autoclavable medium to which 8% calf serum had been added. A medium containing 0.1% Methocel and 2% calf serum was also tested. Maximum productivity was obtained at a dilution rate of 0.33 day^?1 with a cell density of about 1.0 × 10⁶ cells/ml. The same cell line was also infected with Rubella virus and the production of virus was followed at the 5-liter cultivation level.     

Determination of cell lysis and death kinetics in continuous hybridoma cultures from the measurement of lactate dehydrogenase release

The death of the hybridoma VO 208 in a continuous culture at pH 7 and 6.8 was investigated by measuring both the appearance of visible dead cells which do not exclude the trypan blue dye and the release of lactate dehydrogenase (LDH) in the culture medium. The intracellular LDH was found to be completely released either when live cells lysed or when they were transformed into visible dead cells. No significant lysis of blue dead cells could be observed at the two different pH. Using a LDH balance over the culture system, cell lysis was found negligible at pH 7, but accounted for 20% of the total cell death at pH 6.8. A methodology is proposed to evaluate the rate constants of hybridoma lysis and total death. For the investigated cell line in continuous culture, the calculated total cell death rate constant was found to increase from 0.002 h^–1 to 0.01 h^–1 when decreasing the pH from 7 to 6.8.Abbreviations D dilution rate (h^–1) - k_b specific trypan-blue dead cells appearance rate (h^–1) - k_L specific lysis rate of viable cells (h^–1) - k_d specific death rate (h-1) - LDH₀ lactate dehydrogenase activity in the feed culture medium (IU.l^–1) - LDH lactate dehydrogenase activity in the outlet culture medium (IU.l^–1) - LDH_i intracellular lactate dehydrogenase activity of viable cells (IU.10^–9 cells) - r_LDH total rate of LDH release (IU.h^–1.L^–1) - r_b transformation rate of viable cells into blue dead cells (10⁹ cells.h^–1.L^–1) - x_v viable cell concentration (10⁹ cells.l^–1) - x_b trypan-blue dead cell concentration (10⁹ cells.l^–1)     

Stabile production of a thrombin resistant pro-urokinase derivative (PRO-UKS1) by Namalwa KJM-1 cells adapted to serum-free medium

Pro-UKS1 was designed as a thrombin-resistant derivative of pro-urokinase (pro-UK) by introducing a glycosylation site using site-directed mutagenesis. An expression plasmid for pro-UKS1, pMo1UKS1SEd1-5, was constructed and introduced into Namalwa KJM-1 cells (Hosoiet al., 1988), and cells resistant to G418 and Methotrexate (MTX) were obtained. Amongst them, the highest pro-UKS1 producer (resistant to 500 nM of MTX), clone 41-8, was selected and further characterized. Clone 41-8 was cultured in serum-free ITPSGF medium (Hosoiet al., 1988). Under the conventional conditions, the concentration of pro-UKS1 reached 26 g ml^–1. Addition of glucose and tri-iodothyronine (T₃) improved productivity, and the maximal productivity of pro-UKS1 was 67 g ml^–1 day^–1. In this conditioned medium, content of pro-UKS1 was above 80% of total proteins.Abbreviations BSA bovine serum albumin - dhfr dihydrofolate reductase - HEPES 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid - kb kilobase pairs - kDa kilodaltons - MTX Methotrexate - PBS phosphate buffered saline - pro-UK pro-urokinase - SDS-PAGE sodium dodecyl sulfate-polyacrylamide gel electrophoresis - T₃ tri-iodothyronine - Tween-PBS phosphate buffered saline containing 0.05% Tween 80     

Continuous culture of Candida boidinii variant 60 growing on methanol

Summary A new variant, Candida boidinii variant 60, which is less sensitive to methanol and formaldehyde shocks was grown in continuous cultures with methanol as sole carbon source. The substrate concentration in the feeding medium was either 1% methanol or 3% methanol. Biomass production, methanol consumption, the formation of formaldehyde and gas exchange were measured at different dilution rates. With low methanol feeding (10 g/l) maximal productivity of 0.44 g biomass/l·h is obtained at a dilution rate of 0.14 h^–1. Maximal specific growth rate is 0.18 h^–1. A yield of 0.32 g biomass/g methanol was obtained and the respiration quotient was determined as 0.55. Independently of initial substrate concentration, biomass decreases if methanol and formaldehyde are accumulating in the culture broth.In the culture with high methanol feeding (30 g/l) cell concentratioon increases up to 9 g/l at D=0.04 h^–1. At higher dilution rates methanol and form-aldehyde appear in the medium. Formaldehyde is then preferably oxidized without energy advantages for the cells. It seems that this enables the cells to overcome toxic effects caused by methanol and formaldehyde.     

Pectin lyase production by Penicillium griseoroseum grown in sugar cane juice in repeated batch cultures

Penicillium griseoroseum cultured in the presence of sucrose and yeast extract produces pectin lyase (EC 4.2.2.10) (PL) in the absence of its natural inducer pectin. This fungus was cultured in a fermenter at an aeration rate of 0.5 l/min for the first 25 h and 1.0 l/min for the remainder of the culture period, and at a stirring rate of 200 rev/min for the entire culture period. Fungal spores were inoculated directly into the fermenter at a final concentration of 5 × 10⁴ spores/ml. The fungus was cultured in minimal medium supplemented with powdered dehydrated sugar cane juice, producing PL without added yeast extract. Maximum PL activity (0.067 IU/ml) was obtained after 65 h in batch culture. Pellet morphology of the mycelia made it possible to carry out three cycles of repeated batch culture. The same medium was used for renewal as for the single batch culture. The initial cycle was 53 h, after which approximately 0.103 IU/ml of PL was obtained. After this period, the medium was renewed and fermentation continued for two more cycles, which lasted approximately 20 h. Activity of PL obtained in the second cycle was approximately 0.118 IU/ml and in the third, approximately 0.109 IU/ml.     

Autoinduction of bacterial bioluminescence in a carbon limited chemostat

Several strains of four species of luminous marine bacteria were maintained in a chemostat at a constant dilution rate and a variety of steady state densities by carbon (glycerol) limitation in order to study the relationship between culture density and bioluminescence activity. In general, luminescence per cell was constant at high culture density, and decreased dramatically at low culture density. For Vibrio fischeri, luminescence decreased to nondectable levels when the culture was maintained at low density; such dark cells were stimulated to synthesize luciferase and became luminous within minutes when purified autoinducer was added to the chemostat. Two strains, Photobacterium phosphoreum NZ11D and Photobacterium leiognathi S1, did not show the decrease in light intensity at low culture density that was characteristic of all other strains tested; they appeared to be constitutive for bioluminescence.Abbreviations BCM basal salts glycerol medium - BM basal salts medium - BSA bovine serum albumin - D dilution rate - DTT dilitiothreitol - LU light unit=2×10¹⁰ quanta s^-1 - OD optical density - SWC sea water complete medium - specific growth rate     

Biofilm build-up of Pseudomonas putida in a chemostat at different dilution rates

Summary A test system was set up where the build-up of a biofilm on a defined surface could be studied in a carbon source limited chemostat.The attachment of P. putida ATCC 11172 to glass when growing on L-asparagine was studied at different dilution rates (specific growth rates) from 0.1 to 1.5 h^–1 The number of attached colony forming units (cfu) increased with dilution rate from 1×10⁶ cfu/cm² at 0.1 h^–1 to 4×10⁷ cfu/cm² at 1.0 h^–1 and then the attachment decreased to about 6×10⁶ cfu/cm² at higher dilution rates (1.1–1.5 h^–1). The number of attached cfu was measured after 24 h exposure. The value of the maximum specific growth rate in batch culture was 0.6 h^–1.The total amount of attached cell-mass followed roughly the same pattern as the viable count.The viable count of the cells suspended in the growth medium showed its lowest value at the same dilution rate as resulted in maximum adhesion.It was shown that the effect of growth rate on the biofilm build-up of P. putida is significant, and ought to be borne in mind when continuous culture systems are set up and results evaluated.     

Continuous production of pediocin by immobilized Pediococcus acidilactici PO2 in a packed-bed bioreactor

 A continuous bioreactor packed with a fibrous matrix was set up. Cells of Pediococcus acidilactici PO2 were inoculated and MRS broth was fed gradually until cell growth and immobilization were achieved. Kinetics of fermentation and production of bacteriocin were investigated at dilution rates ranging from 0.63 day^-1 to 1.58 day^-1 and at pH values that varied between 4.0 and 5.5. A maximum bacteriocin activity of 6400 AU/ml was detected when the medium was fermented at dilution rates of at least 1.19 day^-1 and the pH controlled at 4.5. The maximum bacteriocin productivity was 1.0×10⁷ AUl^-1 day^-1 at a dilution rate of 1.58 day^-1 and pH 4.5. At this high dilution rate, 1.21 g cells/l medium was produced, 95.9% of the glucose in MRS broth was utilized, and 15.1 g lactic acid/l accumulated in the bioreactor effluent. The bioreactor was operated continuously for 3 months without encountering any clogging, degeneration, or contamination problems, indicating good long-term stability of the bioreactor for bacteriocin production. About 94% of the cells in the bioreactor were immobilized, and the remainder were suspended in the medium. According to scanning electron microscopic observations, cell immobilization in the fibrous matrix was attained by natural attachment to fiber surfaces and entrapment in the void volume within the fibrous matrix. In conclusion, conditions for the optimum continuous production of pediocin were defined; this may facilitate the development of large-scale industrial processes for production of this bacteriocin. Received: 25 September 1995/Received revision: 30 November 1995/Accepted: January 1996     

Cell protein degradation in cultured rat embryo fibroblasts suppression by vinblastine of the enhanced proteolysis by serum-deficient media

Rat embryo fibroblasts grown in Eagle's minimal essential medium with 10% serum were labeled with L-[¹⁴C]leucine. After a 24 h cold chase, rates of proteolysis were evaluated by measuring the appearance of trichloroacetic acid-soluble ¹⁴C in the media. Cells remaining in minimal essential medium with 10% serum (basal) showed a proteolysis rate of 1% per h, whereas cells placed in minimal essential medium alone (serum-deficient) showed a stimulation of proteolysis to 3–4% per h. This enhanced proteolysis was transitory, occuring only for the first 4–8 h after cells were placed in the serum-deficient media. Vinblastine 10⁻⁵ M inhibited the enhanced proteolysis 40% but had no effect on basal proteolysis. Control experiments showed no detectable hydrolysis of extracellular proteins, nor did vinblastine affect the rate of protein synthesis. These data suggest that basal and enhanced proteolysis have at least partially distinct mechanisms in the cell and that only enhanced proteolysis involves microtubules.     

Insulin binding in cultured Chinese hamster kidney epithelial cells: The effect of serum in the medium

Summary [¹²⁵I]Insulin (porcine) binding to an epithelial cell line established from a Chinese hamster kidney, CHK-AC_E−100, showed an optimum at pH 8.0 and reached a maximum after 2.5 h incubation at 25°C. Dissociation of bound [¹²⁵I]insulin was facilitated by the addition of unlabeled insulin in the dilution buffer. Porcine insulin effectively competed for [¹²⁵I]insulin binding to the cultured cells and was 30 and 90 times as potent as guinea pig insulin and porcine proinsulin in causing 50% inhibition of [¹²⁵I]insulin binding; glucagon was completely ineffective. Scatchard analysis of the binding data yielded a curvilinear plot and a capacity of 0.6 ng/10⁶ cells; the average affinity of the empty receptor, , was calculated to be 1.78×10⁸ M ⁻¹ and that of the filled receptor, , 0.57×10⁸ M ⁻¹. Substitution of fetal bovine serum (FBS) in the culture medium with bovine calf, bovine newborn, or bobby calf serum altered insulin binding characteristics in the cells and reduced cell growth. Insulin binding characteristics of cells grown in hormone-supplemented medium containing 0 to 0.1% FBS were similar to those of cells grown in minimum essential medium (MEM) containing 2 to 5% FBS. The data indicated that the established Chinese hamster kidney epithelial cell line CHK-AC_E−100 possessed specific insulin receptors and the characteristics of the receptors could be manipulated by changing the serum in culture medium.     

Optimization of pro-urokinase secretion from recombinant Saccharomyces cerevisiae

Secretion of a nonglycosylated form of human pro-urokinase, also known as single-chain urinary plasminogen activator (scu-PA), from Saccharomyces cerevisiae is described. A "supersecreting" yeast strain harboring multiple copies of integrated plasmids was grown batchwise and at constant respiratory quotient (RQ) in 20-L fermenters. Because the promoters used to drive expression of the pro-urokinase genes are not tightly regulated, secretion into the culture supernatant was growth associated. Although the final cell density achieved in the perturbed-batch fermentation (45 g dry wt/L) was less than that observed in the RQ-controlled culture (77 g dry wt/L), the scu-PA titer in the perturbed-batch fermentation (1863 IU/mL) was nearly twice that attained at constant RQ (1108 IU/mL). The effects on cell growth and scu-PA titer of other process variables (pH, temperature, phosphate concentration, and medium composition) are also discussed.     

The serum growth and survival requirements of SV40-transformed 3T3 cells

Summary Simian virus 40-transformed 3T3 cells are dependent on serum for survival and growth. This growth activity can be separated on a pH 2 Sephadex G100 column into two fractions: a high molecular weight activity and a low molecular weight substance that has recently been characterized as containing as its major agent, biotin. To replace the remainder of the serum requirement, hormones and other growth factors were tested. Both insulin at high, nonphysiological concentrations (200 to 500 ng/ml) and transferrin (5×10⁻⁸ M) stimulate the growth rate in low serum medium (0.3% v/v bovine calf serum DME) individually and, when added together, are nearly as growth enhancing as 10% serum. The need for the residual serum in this medium can be eliminated by the use of crystalline trypsin during trypsinization. Under these serum-free conditions, biotin and transferrin supplementation provide for moderately good growth (20 to 30 hr population doubling time, 1×10⁶ cells/3.2-cm dish final cell density). Insulin addition further stimulates the growth rate (16 to 20 hr) and the final density (1.5×10⁶ cells). Although the protein growth factors, EGF (0.5 to 1.0 ng/ml) and FGF (4 to 10 ng/ml), also appear to enhance growth individually and additively, their effects are slight and very variable. Nevertheless, the complete serum-free medium (DME supplemented with biotin, transferrin, insulin, EGF and FGF) yields growth comparable but still inferior to 10% serum supplementation (14-versus 12-hr population doubling time, 1 to 2×10⁶ versus 2 to 3×10⁶ cells final cell density). This work was supported by NIH Grant CA 20040.     

CHO工程细胞 (11G-S) 悬浮培养的无血清培养基的设计

以悬浮适应的表达重组尿激酶原 (Pro-urokinase,pro-UK) CHO工程细胞系11G-S为对象,采用Plackett-Burman实验设计及响应面分析法,设计支持CHO工程细胞 (11G-S) 悬浮生长的无血清培养基。以细胞密度为评价指标,在单因素实验的基础上采用Plackett-Burman实验设计对影响细胞生长的培养基添加成分进行考察,确定了3种对细胞生长明显促进作用的培养基添加成分：胰岛素、转铁蛋白及腐胺。继而利用响应面法分析了这3种添加成分的最佳水平范围,设计了一种适用于CHO工程细胞 (11G-S) 悬浮培养的无血清培养基SFM-CHO-S。11G-S细胞在SFM-CHO-S批次悬浮培养的细胞最大生长密度达到4.12×106 cells/mL,pro-UK的最大累积活性达到5 614 IU/mL,培养效果优于商品化的同类无血清培养基。     

Optimal conditions for the preservation of mouse lymph node cells in liquid nitrogen using cooling rate techniques

The factors that affect the survival of mouse lymphocytes throughout a procedure for storage at ?196 °C have been studied both for the improvement of recovery and the possible extension to the mouse system of cell selection by freezing. After thawing, the survival of cells cooled at different rates in dimethyl sulphoxide (DMSO, 5 or 10%, $\text{v}\text{v}$) was assessed from the [³H]thymidine incorporation in response to phytohaemagglutinin and concanavalin A. Before freezing the protection against freezing damage increased with time (up to 20 min) in DMSO (5%, $\text{v}\text{v}$) at 0 °C. Superimposed upon this effect was toxicity due to the DMSO. During freezing and thawing the cooling rate giving optimal survival was 8 to 15 °C/min for cells in DMSO (5%) and 1 to 3 °C/min for DMSO (10%). Omission of foetal calf serum was detrimental. Rapid thawing (>2.5 °C/min) was superior to slow thawing. After thawing dilution at 25 or 37 °C greatly improved cell survival compared with 0 °C; at 25 °C survival was optimal (75%) at a moderate dilution rate of 2.5 min for a 10-fold dilution in FCS (10%, $\text{v}\text{v}$) followed by gentle centrifugation (50g).Dilution damage during both thawing and post-thaw dilution may be due to osmotic swelling as DMSO and normally excluded solutes leave the cell. The susceptibility of the cell membrane to dilution damage may also be increased during freezing. The need to thaw rapidly and dilute at 25 °C after thawing is probably due to a decrease in dilution stress at higher temperatures. Optimisation of dilution procedures both maximised recovery and also widened the range of cooling rates over which the cells were recovered. These conditions increase the possibility of obtaining good recovery of a mixed cell population using a single cooling procedure. Alternatively, if cell types have different optimal cooling rates, stressful dilution may allow their selection from mixed cell populations.     

New method for testing solar sensitivity of commercial formulations of the granulovirus of codling moth (Cydia pomonella, Tortricidae: Lepidoptera)

A method for screening codling moth granulovirus (CpGV) formulation sensitivity to sunlight using specially prepared half apples and a solar simulator is described. The half apple preparation allows an even coverage of virus over the surface of the fruit that would not be possible using whole apples. Leaves and artificial medium were not usable for extended periods of exposure in the solar simulator due to excess drying. Fruit was sprayed with 10⁻³ and 10⁻⁵ dilutions of three commercial formulations of CpGV (Carpovirusine, Cyd-X, and Virosoft) and infested with codling moth neonates. Half of the sprayed fruit was exposed to 650 W/m² for 4 h in an Atlas Suntest CPS solar simulator resulting in an accumulated radiant energy of 9.36 × 10⁶ J/m² before they were infested with neonate codling moth larvae. Spraying non-irradiated fruit with the 10⁻³ dilution of Cyd-X and Virosoft resulted in nearly 100% mortality of neonate larvae. Irradiation reduced viral activity by 71-98% at the 10⁻³ dilution and by up to 32% at the 10⁻⁵ dilution relative to non-irradiated fruit. The procedures utilized enabled good preservation of the fruit throughout the incubation period and minimized invasion of the fruit by plant pathogens and saprophytic organisms. This laboratory method for screening candidate formulations and potential UV protectants could conserve time and resources by eliminating adjuvants with less potential in laboratory tests and field testing only the most promising candidates. It also enables year-round testing.     

The influence of serum components on the growth and mutation of Chinese hamster cells in medium containing aminopterin

When seeded in small numbers in medium containing 10^?6M aminopterin and fetal calf serum, V₇₉ Chinese hamster cells required dialyzable components from the serum for growth. However, the cells grew in medium containing 10^?6M aminopterin and dialyzed serum, provided that the medium was supplemented with 10^?5M hypoxanthine and sufficient 5·10^?6M) thymidine. A growth-inhibitory property of some batches of dialyzed serum was abolished on heating the serum for 30 min at 56°. Three lines of V₇₉ cells which lacked detectable hypoxanthine-guanine phosphoribosyl transferase (HGPRT) activity were seleccted in medium containing 8-azaguanine (8-AzG). In two of these, no spontaneous reversion to the HGPRT⁺ phenotype was detectable, and these cells did not cooperate metabolically with HGPRT⁺ cells to prevent the growth of the latter in HAT medium. One of the HGPRT^? lines showed a high rate of spontaneous reversion (118/10⁵ cells) in medium containing undialyzed serum. However, in medium containing dialyzed serum the spontaneous reversion rate fell to $\text{4}\text{10}{}^5\text{cells}$, suggesting that the revertants arising in medium containing undialyzed serum were biochemically heterogeneous.     

Observations consistent with autocrine stimulation of hybridoma cell growth and implications for large-scale antibody production

Existence of autocrine growth factors (aGFs) may influence the serum requirement for growth of hybridoma cells and thus significantly influence process economics. For the murine hybridoma cell line S3H5/2bA2, critical inoculum density (cID) and serum requirement for growth were inversely related for cultivation in both T flasks and spinner flasks. In spinner flasks, an inoculum density of 10⁶ cells/ml was necessary for the cells to grow in RPMI 1640 medium without serum supplement, and an inoculum density of 10³ cell/ml was necessary in RPMI 1640 medium with 10% serum. In T flasks, where the local cell density is higher than in spinner flasks, an inoculum density of 10⁶ cells/ml was necessary for the cells to grow in RPMI 1640 medium without serum supplement, and an inoculum density of 1 cell/ml was also necessary in RPMI 1640 medium with 10% serum. Further, immobilized cells at high local cell density could grow under conditions where cells in T flasks at corresponding overall cell density could not grow. The cells at high inoculum density were less sensitive to shear induced by mechanical agitation than the cells at low inoculum density. Taken together these observations support the existence of secreted aGF(s) by the hybridoma cell line used. Since the specific MAb production rate was independent of cultivation method and inoculum density, the existence of autocrine growth factors would suggest that the use of immobilized cells should improve the economics of MAb production.     

Multi-stage biofilm reactor for acetic acid production at high concentration

Summary Continuous production of acetic acid by liquid surface culture ofAcetobacter aceti M7 was investigated using a Multi-Stage Biofilm Reactor (MSBFR) composed of ten shallow flow horizontal reactors of laboratory scale. With varying dilution rate in the range from 0.049 to 0.2 h^–1, the maximum exit acetic acid concentration reached was as high as 98.0 g/l at the lowest dilution rate with step feed of ethanol-rich medium to stages 3, 5, and 7. The production rate (4.3 g/l/h) was rather high considering the inhibitory effect of high acetic acid concentration. This may be ascribed to non-homogeneous distribution of acetic acid concentration in the bioreactor and step feed of ethanol-rich medium.