Comparing BRIN-BD11 culture producing insulin using different type of microcarriers

This research was conducted to examine the growth profile, growth kinetics, and insulin-secretory responsiveness of BRIN-BD11 cells grown in optimized medium on different types of microcarriers (MCs). Comparisons were made on modified polystyrene (Hillex^® II) and crosslinked polystyrene Plastic Plus (PP) from Solohill Engineering. The cell line producing insulin was cultured in a 25 cm² T-flask as control while MCs based culture was implemented in a stirred tank bioreactor with 1 L working volume. For each culture type, the viable cell number, glucose, lactate, glutamate, and insulin concentrations were measured and compared. Maximum viable cell number was obtained at 1.47 × 10⁵ cell/mL for PP microcarrier (PPMCs) culture, 1.35 × 10⁵ cell/mL Hillex^® II (HIIMCs) culture and 0.95 × 10⁵ cell/mL for T-flask culture, respectively. The highest insulin concentration has been produced in PPMCs culture (5.31 mg/L) compared to HIIMCs culture (2.01 mg/L) and T-flask culture (1.99 mg/L). Therefore overall observation suggested that PPMCs was likely preferred to be used for BRIN-BD11 cell culture as compared with Hillex^® II MCs.     

Development of a chemically defined platform fed-batch culture media for monoclonal antibody-producing CHO cell lines with optimized choline content

A chemically defined platform basal medium and feed media were developed using a single Chinese hamster ovary (CHO) cell line that produces a monoclonal antibody (mAb). Cell line A, which showed a peak viable cell density of 5.9 × 10⁶ cells/mL and a final mAb titer of 0.5 g/L in batch culture, was selected for the platform media development. Stoichiometrically balanced feed media were developed using glucose as an indicator of cell metabolism to determine the feed rates of all other nutrients. A fed-batch culture of cell line A using the platform fed-batch medium yielded a 6.4 g/L mAb titer, which was 12-fold higher than that of the batch culture. To examine the applicability of the platform basal medium and feed media, three other cell lines (A16, B, and C) that produce mAbs were cultured using the platform fed-batch medium, and they yielded mAb titers of 8.4, 3.3, and 6.2 g/L, respectively. The peak viable cell densities of the three cell lines ranged from 1.3 × 10⁷ to 1.8 × 10⁷ cells/mL. These results show that the nutritionally balanced fed-batch medium and feeds worked well for other cell lines. During the medium development, we found that choline limitation caused a lower cell viability, a lower mAb titer, a higher mAb aggregate content, and a higher mannose-5 content. The optimal choline chloride to glucose ratio for the CHO cell fed-batch culture was determined. Our platform basal medium and feed media will shorten the medium-development time for mAb-producing cell lines.     

Enhancement of BDNF production by co-cultivation of human neuroblastoma and fibroblast cells

It has been proved that co-cultivation of human neuroblastoma cells and human fibrolast cells can enhance nerve cell growth and the production of BDNF in perfusion cultivation. In batch co-cultivation, maximum cell density was increased up to 1.76×10⁶ viable cells/mL from 9×10⁵ viable cells/mL of only neuroblastoma cell culture. The growth of neuroblastoma cells was greatly improved by culturing both nerve and fibroblast cells in a perfusion process, maintaining 1.5×10⁶ viable cells/mL, which was much higher than that from fed-batch cultivation. The nerve cell growth was greatly enhanced in both fed-batch and perfusion cultivations while the growth of fibroblast cells was not. It strongly implies that the factors secreted from, human fibroblast cells and/or the environments of co-culture system can enhance both cell growth and BDNF secretion. Specific BDNF production rate was not enhanced in co-cultures; however, the production period was increased as the cell growth was lengthened in the co-culture case. Competitive growth between nerve cells and fibroblast cells was not observed in all cases, showing no changes of fibroblast cell growth and only enhancement of the neuroblastoma cell growth and overall BDNF production. It was also found that the perfusion cultivation was the most appropriate process for cultivating two cell lines simultaneously in a bioreactor.     

Production of influenza H1N1 vaccine from MDCK cells using a novel disposable packed-bed bioreactor

A process for human influenza H1N1 virus vaccine production from Madin–Darby canine kidney (MDCK) cells using a novel packed-bed bioreactor is described in this report. The mini-bioreactor was used to study the relationship between cell density and glucose consumption rate and to optimize the infection parameters of the influenza H1N1 virus (A/New Caledonia/20/99). The MDCK cell culture and virus infection were then monitored in a disposable perfusion bioreactor (AmProtein Current Perfusion Bioreactor) with proportional–integral–derivative control of pH, dissolved O₂ (DO), agitation, and temperature. During 6 days of culture, the total cell number increased from 2.0?×?10⁹ to 3.2?×?10¹⁰ cells. The maximum virus titers of 768 hemagglutinin units/100 μL and 7.8?×?10⁷ 50 % tissue culture infectious doses/mL were obtained 3 days after infection. These results demonstrate that using a disposable perfusion bioreactor for large-scale cultivation of MDCK cells, which allows for the control of DO, pH, and other conditions, is a convenient and stable platform for industrial-scale production of influenza vaccines.     

Evaluation of a novel pneumatic bioreactor system for culture of recombinant Chinese hamster ovary cells

Single use culture systems are a tool in research and biotechnology manufacturing processes and are employed in mammalian cell-based manufacturing processes. Recently, we characterized a novel bioreactor system developed by PBS Biotech. The Pneumatic Bioreactor System? (PBS) employs the Air-wheel?, which is a mixing device similar in structure to a water wheel but is driven by the buoyant force of gas bubbles. In this study, we investigated the physical properties of the PBS system, with which we performed biological tests. In 2 L PBS, the mixing times ranged from 6 (30 rpm, 0.175 vvm) to 15 sec (10 rpm, 0.025 vvm). The k_La value reached upto 7.66/h at 0.5 vvm, even without a microsparger, though this condition is not applicable for cell cultures. Also, when a 10 L PBS equipped with a microsparger was evaluated, a k_La value of upto approximately 20/h was obtained particularly in mild cell culture conditions. We performed cultivation of Chinese hamster ovary (CHO) cells in 2 and 10 L PBS prototypes. Results from the PBS were compared with those from an Erlenmeyer flask and conventional stirred tank type bioreactor (STR). The maximum cell density of 10.6 × 106 cells/mL obtained fromthe 2 L PBSwas about 2 times higher than that from the Erlenmeyer flask (5.6 × 10⁶ cells/mL) andwas similar to the STR (9.7 × 10⁶ cells/mL) when the CHO-S cells were cultured. These results support the general suitability of the PBS system using pneumatic mixing for suspension cell cultivation as a novel single-use bioreactor system.     

High density culture of hybridoma cells in a dual hollow fiber bioreactor

Summary Hybridoma cells were cultured for two months in the dual hollow fiber bioreactor (DHFBR) which had been successfully used for high cell density cultures of various microbial cells. In batch suspension culture the concentration of monoclonal antibody (Mab) against human Chorionic Gonadotropin (hCG) and the cell density of Alps 25-3 hybridoma cells were obtained in 30 μg/mL and 2.35×10⁶ cells/mL, respectively. The continuous culture with DHFBR produced Mab of 100–130 μg/mL for 30 days and the estimated cell density in the extracapillary space of DHFBR was 1.87×10⁸ cells/mL based on the antibody production rate. The productivity of Mab was 205 mg/day per litre of the total reactor volume while that of the batch suspension culture was only 10 mg/L day.     

Use of moving aeration membrane bioreactor for the efficient production of tissue type plasminogen activator in serum free medium

A moving aeration-membrane (MAM) bioreactor was employed for the production of 2 μg/mL of tissue type Plasminogen Activator (tPA) in serum free medium from normal human fibroblast cells. This system could maintain high cell density for long periods of steady state conditions in perfusion cultivation. Under normal operating conditions, shear stress was as low as 0.65 dynes/cm² at the agitation speed of 80 rpm. Even though cell density gradually decreased with increasing agitation speed, tPA production increased linearly with increasing shear stress within a moderate range. This culture system allowed production of 2 μg tPA/mL while maintaining a high cell density of 1.0×10⁷ viable cells/mL.     

Cultivation ofLactobacillus crispatus KLB46 isolated from human vagina

Bacterial vaginosis can be treated by restoring the normal vaginal flora using lactobacilli.Lactobacillus crispatus KLB46 that was isolated from the human vagina has a strong antimicrobial activity and was grown in a batch and in a continuous fermentor. During batch cultivation, the maximum specific growth rate ofL. crispatus KLB 46 was 0.63 h⁻¹ and the highest viable cell count (1.9×10⁹ CFU/mL) was obtained at pH 5.5.L. crispatus KLB 46 did not grow well at either pH 3.5 or 7.5. During continuous cultivation, the highest viable cell count (1.53×10⁹ CFU/mL) was obtained at a dilution rate of 0.32 h⁻¹. However, the maximum productivity of viable cells was obtained at a dilution rate of 0.52 h⁻¹, and was 7.33×10¹¹ CFU L⁻¹ h⁻¹, that is approximately 5 times higher than that obtained from batch culture.     

Process development for an inducible rituximab-expressing Chinese hamster ovary cell line

Inducible mammalian expression systems are becoming increasingly available and are not only useful for the production of cytotoxic/cytostatic products, but also confer the unique ability to uncouple the growth and production phases. In this work, we have specifically investigated how the cell culture state at the time of induction influences the cumate-inducible expression of recombinant rituximab by a GS-CHO cell line. To this end, cells grown in batch and fed-batch cultures were induced at increasing cell densities (1 to 10 × 10 ⁶ cells/mL). In batch, the cell specific productivity and the product yield were found to reduce with increasing cell density at induction. A dynamic feeding strategy using a concentrated nutrient solution applied prior and postinduction allowed to significantly increase the integral of viable cells and led to a 3-fold increase in the volumetric productivity (1.2 g/L). The highest product yields were achieved for intermediate cell densities at induction, as cultures induced during the late exponential phase (10 × 10 ⁶ cells/mL) were associated with a shortened production phase. The final glycosylation patterns remained however similar, irrespective of the cell density at induction. The kinetics of growth and production in a 2 L bioreactor were largely comparable to shake flasks for a similar cell density at induction. The degree of galactosylation was found to decrease over time, but the final glycan distribution at harvest was consistent to that of the shake flasks cultures. Taken together, our results provide useful insights for the rational development of fed-batch cell culture processes involving inducible CHO cells. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2742, 2019     

Large-scale production of Erythroid Differentiation Factor (EDF) by gene-engineered Chinese hamster ovary (CHO) cells in suspension culture

From Chinese hamster ovary (CHO) cells which were producing Erythroid Differentiation Factor (EDF) in a culture medium, anchorage-independent cells, named as CHO-SPN, were produced by repeated cultivating in a suspension system. The growth time and maximum cell density of the CHO-SPN cells were 48 h and 7.8×10⁵ viable cells/ml. CHO-SPN cells accumulated 8,000 units/ml (corresponding to 4 mg/ml) of EDF in 4d. After 20 cycles of culture, CHO-SPN cells still possessed the same EDF productivity and the same growth kinetics. Furthermore, in an appropriate dissolved oxygen concentration and pH controlled culture system, the growth time and cell density became 24 h and 1×10⁶ viable cells/ml. The critical level of dissolved oxygen for cell growth was 0.015 atm. The maximum oxygen demand was 3.3×10⁻⁹ mole of O₂/ml/min.Fetal bovine serum (FBS) was indispensable for cell growth. However, a FBS-free medium (ASF201) was available for maintenance of the CHO-SPN cells, and EDF production occurred in the same medium.     

UV-induced mutagenesis at the hypoxanthine—guanine phosphoribosyl transferase locus in two L5178Y mouse lymphoma cell strains with different UV sensitivities

Two strains of L5178Y mouse lymphoma cells, L5178Y-R (LY-R) and L5178Y-S (LY-S), differ markedly in their sensitivity to 254 nm UV radiation (D₀ = 0.7 and 5.5 J/m²; n = 6.0 and 2.0 for LY-R and LY-S cells, respctively). In this study, the frequency o hypoxanthine-guanine-phosporibosyl-transferase-deficient mutants was determined, using 6-thioguanine (TG) as a selective agent, in populations of LY-R and LY-S cells exposed to various fluences of UV radiation. The spontaneous mutation frequency for LY-R cells was (3.7 ± 0.6) × 10^?5 TG^r mutants per viable cell, and the UV induction rate was (2.2 ± 0.8) × 10^?4 TG^r mutants per viable cell, per J/m². Both spontaneous and induced mutantion frequencies were much lower for LY-S cells. The sopntaneous mutation frequency for these cells were too low to make its measurement practicable ( < 0.0013 × 10^?5 TG^r mutants per viable cell). Mutation induction rate was (4.2 ± 2.2) × 10^?7 TG^r mutants per viable cell, per J/m². These differences in mutability do not appear to be due to gene duplication in LY-S cells, or to selective growth disadvantage of LY-S-derived TG-resistant mutants. Possible mechanisms underlying the differences in mutability of LY-R and LY-S cells are considered.     

Growth characterizations of a human monocytic leukemia cell line in a serum-free medium

A clone, AH-01S, derived from a human monocytic leukemia cell line, THP-1, grew rapidly in a serum-free medium containing insulin, transferrin, ethanolamine, and sodium selenite. In batch culture using the serum-free medium, the AH-01S cells proliferated at a specific growth rate (μ) of 0.30 to 0.50 (1/day) from a cell concentration of 1 × 10⁴ cells/ml to 1.6 × 10⁶ cells/ml, an increase of 160 times. A higher cell concentration of 0.45 × 10⁷ cells/ml (cell volume ratio was 0.5%) was obtained in spinner flask culture using the serum-free medium. A mean specific growth rate 0.50 (1/day) was also observed in a culture in a fully instrumented cell culture fermentor. However, μ decreased drastically after the cell concentration reached 1.5 × 10⁶ cells/ml. Analyses of medium composition during cultivation revealed that under lower cell concentration, l-glutamine was the main carbon source while glucose was converted to lactate almost stoichiometrically, and that the production of lactate from glucose decreased at higher cell concentrations. To obtain cultures of 1 × 10⁹ cells, 1,200 to 1,300 mg of a carbon source (glucose) and 400 to 500 of amino acids were consumed during high cell concentration cultivation of the AH-01S cells in the serum-free medium.     

Process intensification in fed-batch production bioreactors using non-perfusion seed cultures

ABSTRACT

Although process intensification by continuous operation has been successfully applied in the chemical industry, the biopharmaceutical industry primarily uses fed-batch, rather than continuous or perfusion methods, to produce stable monoclonal antibodies (mAbs) from Chinese hamster ovary (CHO) cells. Conventional fed-batch bioreactors may start with an inoculation viable cell density (VCD) of ~0.5 × 10⁶ cells/mL. Increasing the inoculation VCD in the fed-batch production bioreactor (referred to as N stage bioreactor) to 2–10 × 10⁶ cells/mL by introducing perfusion operation or process intensification at the seed step (N-1 step) prior to the production bioreactor has recently been used because it increases manufacturing output by shortening cell culture production duration. In this study, we report that increasing the inoculation VCD significantly improved the final titer in fed-batch production within the same 14-day duration for 3 mAbs produced by 3 CHO GS cell lines. We also report that other non-perfusion methods at the N-1 step using either fed batch or batch mode with enriched culture medium can similarly achieve high N-1 final VCD of 22–34 × 10⁶ cells/mL. These non-perfusion N-1 seeds supported inoculation of subsequent production fed-batch production bioreactors at increased inoculation VCD of 3–6 × 10⁶ cells/mL, where these achieved titer and product quality attributes comparable to those inoculated using the perfusion N-1 seeds demonstrated in both 5-L bioreactors, as well as scaled up to 500-L and 1000-L N-stage bioreactors. To operate the N-1 step using batch mode, enrichment of the basal medium was critical at both the N-1 and subsequent intensified fed-batch production steps. The non-perfusion N-1 methodologies reported here are much simpler alternatives in operation for process development, process characterization, and large-scale commercial manufacturing compared to perfusion N-1 seeds that require perfusion equipment, as well as preparation and storage vessels to accommodate large volumes of perfusion media. Although only 3 stable mAbs produced by CHO cell cultures are used in this study, the basic principles of the non-perfusion N-1 seed strategies for shortening seed train and production culture duration or improving titer should be applicable to other protein production by different mammalian cells and other hosts at any scale biologics facilities.     

Starvation survival of Gordonia polyisoprenivorans CCT 7137, isolated from contaminated groundwater in Brazil

Gordonia polyisoprenivorans CCT7137, exopolysaccharide-producing bacterium, was isolated from groundwater contaminated with leachate in a former municipal landfill site (São Paulo, Brazil). The strain was submitted to starvation in phosphate-buffered saline solution for 56 days so as to evaluate its behavior regarding cuturability and cell morphology. As a response to starvation, G. polyisoprenivorans CCT7137 presented reduction in viable cell count, cell size and cell shape alteration. The initial number of viable cells was 1.51 × 10⁷ c.f.u. ml. After 7 days of starvation culturability dropped to 13.70% (2.07 × 10⁶ c.f.u/ml) and, after 56 days, to 3.25% (4.93 × 10⁵ c.f.u/ml). It was also observed that after 7 days of starvation the cell size presented an average reduction in the values of length, length/width ratio, volume and area of 50, 58, 40 and 42%, respectively. The length/width ratio showed a change of shape from rod to coccobacillus. Changes in cell dimensions and distribution of cell into classes were not significant after day 7 of starvation. The results obtained show that it is not necessary for the strain to starve for more than a week to obtain G. polyisoprenivorans CCT7137 size- reduced cells. The results also indicate the potential for its starved forms to be used in future tests in porous medium to study the production of exopolysaccharide in situ.     

Improving lactate metabolism in an intensified CHO culture process: productivity and product quality considerations

In this study, we discussed the development and optimization of an intensified CHO culture process, highlighting medium and control strategies to improve lactate metabolism. A few strategies, including supplementing glucose with other sugars (fructose, maltose, and galactose), controlling glucose level at <0.2 mM, and supplementing medium with copper sulfate, were found to be effective in reducing lactate accumulation. Among them, copper sulfate supplementation was found to be critical for process optimization when glucose was in excess. When copper sulfate was supplemented in the new process, two-fold increase in cell density (66.5 ± 8.4 × 10⁶ cells/mL) and titer (11.9 ± 0.6 g/L) was achieved. Productivity and product quality attributes differences between batch, fed-batch, and concentrated fed-batch cultures were discussed. The importance of process and cell metabolism understanding when adapting the existing process to a new operational mode was demonstrated in the study.     

A feeder-cell independent subpopulation of the PICM-19 pig liver stem cell line capable of long-term growth and extensive expansion

A method for the feeder-independent culture of PICM-19 pig liver stem cell line was recently devised, but the cell line’s growth was finite and the cells essentially ceased dividing after approximately 20 passages over a 1 year culture period. Here we report the isolation, continuous culture, and initial characterization of a spontaneously arising feeder-independent PICM-19 subpopulation, PICM-19FF, that maintained replication rate and hepatocyte functions over an extended culture period. PICM-19FF cells grew to 90–98 % confluency after each passage at 2 week intervals, and the cells maintained a high cell density after 2 years and 48 passages in culture (average of 2.6 × 10⁶ cells/T25 flask or 1 × 10⁵ cells/cm²). Morphologically, the PICM-FF cells closely resembled the finite feeder-independent PICM-19 cultures previously reported, and, as before, no spontaneous formation of 3D multicellular ductules occurred in the cells’ monolayer. Their bipotent stem cell nature was therefore not evident. Over extensive passage, cytochrome P450 (EROD) activity was maintained, although urea production was reduced on a per mg protein basis at later passages. Two other attributes of fetal hepatocytes, γ-glutamyl transpeptidase activity and serum-protein secretion, were also shown to be maintained by the PICM-19FF cells. The PICM-19FF cells therefore appear to have indefinite growth potential as a feeder-independent cell line and this should enhance the experimental usefulness of the cell line, in general, and may also improve its application to toxicological/pharmacological assays and artificial liver devices.     

Mobilization and engraftment of peripheral blood stem cells in healthy related donors >55 years old

Background aimsThe increasing scarcity of young related donors has led to the use of older donors for related allogeneic hematopoietic stem cell transplantation (HSCT). This study analyzed the influence of age on the results of mobilization of peripheral blood stem cells (PBSCs) in healthy donors as well as on the engraftment and outcome of HSCT.MethodsA retrospective analysis from a single center was performed comparing the results of PBSC mobilization from related healthy donors according to their age.ResultsThe study included 133 consecutive related donors. The median age was 50 years (range, 4–77 years); 70 (53%) donors were males, and 44 (33%) were >55 years old. All donors were mobilized with granulocyte colony-stimulating factor for 5 days. The peak CD34⁺ cell count in peripheral blood was higher in younger than in older donors (median, 90.5 CD34⁺ cells/μL [range, 18–240 CD34⁺ cells/μL] versus 72 CD34⁺ cells/μL [range, 20–172.5 CD34⁺ cells/μL], P = 0.008). The volume processed was lower in younger than in older donors (16,131 mL [range, 4424–36,906 mL] versus 18,653 mL [range, 10,003–26,261 mL], P = 0.002) with similar CD34⁺ cells collected (579.3 × 10⁶ cells [range, 135.14 × 10⁶–1557.24 × 10⁶ cells] versus 513.69 × 10⁶ cells [range, 149.81 × 10⁶–1290 × 10⁶ cells], P = 0.844). There were no differences in time to recovery of neutrophils and platelets or in the incidences of acute and chronic graft-versus-host disease, overall survival, non-relapse mortality and relapse incidence.ConclusionsDonors >55 years old mobilized fewer CD34⁺ cells and required a greater volume to collect a similar number of CD34⁺ cells. The outcome of HSCT was not influenced by donor age. Donor age should not be a limitation for related allogeneic HSCT.     

Developement of serum-free media in CHO-DG44 cells using a central composite statistical design

A serum free medium was developed for the production of recombinant antibody against Botulinum A (BoNTA) using dihydrofolate reductase deficient Chinese Hamster Ovary Cells (CHO-DG44) in suspension culture. An initial control basal medium was prepared, which was similar in composition to HAM’s F12: IMDM (1:1) supplemented with insulin, transeferrin, selenium and a lipid mixture. The vitamin concentration of the basal medium was twice that of HAM’s F12: IMDM (1:1). CHO-DG44 cells expressing S25 antibody grew from 2 × 10⁵ cells to maximum cell density of 1.04 × 10⁶ cells/ml after 5 days in this control medium. A central composite design was used to identify optimal levels and interaction among five groups of medium components. These five groups were glutamine, Essential Amino Acids (EAA), Non Essential Amino Acids (NEAA), Insulin, Transferrin, Selenium (ITS), and lipids. Fifty experiments were carried out in four batches, with two controls in each batch. There was little effect of ITS and Lipid concentrations over the range studied, and glutamine concentration showed a strong interaction with EAA. The optimal concentrations of the variables studied were 2.5 mM Glutamine, 7.4 mM (2×) EAA, 1.4 mM (0.5×) NEAA, 1× ITS supplement, 0.7× Lipids supplement. The maximum viable cell density attained in the optimized medium was 1.4 × 10⁶ cells/ml, a 35% improvement over the control culture, while the final antibody titer attained was 22 ± 3.4 μg/mL, a 50% improvement.     

Improved synchronous light scattering method for measuring baker’s yeast biomass using thickened suspensions

Measuring yeast biomass is important in the processes of microbial fermentations. It has been demonstrated that synchronous light scattering (SLS) signals could be applied for the quantification of model bioparticles such as Saccharomyces cerevisiae. In this study, an improved synchronous light scattering method was developed for yeast biomass estimation. The settlement of yeast cells during SLS signals measuring process was studied, and hydrolysis anionic polyacrylamide was added into yeast suspensions to increase the stability of the cells in liquid environment. By simultaneously scanning both the excitation and emission monochromators of a common spectrofluorometer with same starting excitation and emission wavelength (namely, ?λ = 0), the SLS intensity was found to be proportional to the yeast concentration in the range from 0 to 4.9 × 10⁶ cell/mL (R ² = 0.9907), the detection limit is 8.1 × 10³ cell/mL. The developed method exhibited good stability and sensitivity in the recovery test and growth curve drawing process, demonstrating the potential of the method in practical application of biomass estimation.