High density culture of mouse-human hybridoma cells using a perfusion culture apparatus with multi-settling zones to separate cells from the culture medium

Mouse-human hybridoma X87X cells were cultivated using a novel perfusion culture apparatus provided with three-settling zones to separate the cells from the culture medium by gravitational settling. The maximum viable cell density in a serum-free culture medium attained 3.0×10⁷ cells/ml, when the specific perfusion rate was set to 2.3 vol day^-1, and monoclonal antibody was continuously produced. These results were almost the same as those in the perfusion culture vessel with one settling zone and revealed that the process with a plurality of settling zones is a promising one for scale-up of a gravitation type of perfusion culture vessel.     

Selective recycle of viable animal cells by coupling of airlift reactor and cell settler

A new system for the perfusion culture of animal cells in suspension is described. It consists of an airlift loop reactor and a settling tank for cell retention. Insufficient nutrient and oxygen supply of the cells in the settling tank was prevented by cooling the cell suspension before entering the settler. As a result, the catabolic activity of the cells in the settler was reversibly reduced. Furthermore, the density gradient induced by cooling caused a liquid motion through the settler. Thus, it was not necessary to pump medium containing shear, sensitive cells. With this simple system, it was possible to prduce 2 to 5 g of antibodies in a 5.4-L reactor in continuous runs of 400 to 600 h. The productivity was increased by a factor of 17 and the cell density was 4 times higher in comparison with the corresponding batch system. The cell retention system was found to have the property of separating viable and nonviable cells. With the increasing perfusion rate, dead cells and debris were preferably washed out. For perfusion rates up to 1.3 d(-1), the retention efficiency of the settler was nearly 100% for viable cells; hence, this system may show advantages at the industrial scale.     

Serum-free cultivation of anchorage-dependent cells on microcarrier: Effective production of human macrophage colony-stimulating factor

For the purpose of establishing a large scale production process of biologically active substances by cultivation of anchorage-dependent mammalian cells, basic studies were carried out on the following items; establishment of a new cell line and derivation of high productivity; construction of optimal serum-free medium; optimization of cultivation method using microcarrier in serum-free medium; and establishment of purification process. The cell line, TRC-29SF, used in this study was newly established from human renal carcinoma with a function of producing macrophage colony-stimulating factor constitutively. Improvement of M-CSF productivity upon TRC-29SF cell line was performed by M-CSF gene amplification with dhfr-MTX system and by truncation of membrane-binding amino acid sequence by recombinant DNA technique. Two kinds of serum-free media, IPEG-85 and IREG-89, were formulated for the growth of TRC-29SF cell and its transformant, respectively. A new cell-adhesion method which permits homogeneous attachment to microcarrier in short term was developed by equalising the sedimentation velocity between cells and microcarrier by addition of 7% Ficoll into the medium. High cell density perfusion culture of TRC-29SF cells was achieved by microcarrier method using IPEG-85 medium, and final cell density reached over 10⁷ cells/ml. Based on the results obtained, long-term perfusion cultures were performed using Mn10-5 and Mn10-5/R600 cell lines, which were created by M-CSF gene transfection and amplification. We found that the productivity of M-CSF per cell began to decrease from the end of logarithmic growth phase. Long-term cultivation with high productivity was accomplished by perfusing medium containing 2 mM sodium butyrate. Purification process for M1-CSF from the culture supernatant of transformed cell line was also established.     

Modulating and optimizing Pluronic F-68 concentrations and feeding for intensified perfusion Chinese hamster ovary cell cultures

Perfusion culture is often performed with micro-sparger to fulfill the high oxygen demand from the densified cells. Protective additive Pluronic F-68 (PF-68) is widely used to mitigate the adverse effect in cell viability from micro-sparging. In this study, different PF-68 retention ratio in alternating tangential filtration (ATF) columns was found to be crucial for cell performance of different perfusion culture modes. The PF-68 in the perfusion medium was found retained inside the bioreactor when exchanged through ATF hollow fibers with a small pore size (50 kD). The accumulated PF-68 could provide sufficient protection for cells under micro-sparging. On the other hand, with large-pore-size (0.2 μm) hollow fibers, PF-68 could pass through the ATF filtration membranes with little retention, and consequently led to compromised cell growth. To overcome the defect, a PF-68 feeding strategy was designed and successfully verified on promoting cell growth with different Chinese hamster ovary (CHO) cell lines. With PF-68 feeding, enhancements were observed in both viable cell densities (20%–30%) and productivity (~30%). A threshold PF-68 concentration of 5 g/L for high-density cell culture (up to 100 × 10⁶ cells/mL) was also proposed and verified. The additional PF-68 feeding was not observed to affect product qualities. By designing the PF-68 concentration of perfusion medium to or higher than the threshold level, a similar cell growth enhancement was also achieved. This study systematically investigated the protecting role of PF-68 in intensified CHO cell cultures, shedding a light on the optimization of perfusion cultures through the control of protective additives.     

Experimental Measurement of Settling Velocity of Spherical Particles in Unconfined and Confined Surfactant-based Shear Thinning Viscoelastic Fluids

An experimental study is performed to measure the terminal settling velocities of spherical particles in surfactant based shear thinning viscoelastic (VES) fluids. The measurements are made for particles settling in unbounded fluids and fluids between parallel walls. VES fluids over a wide range of rheological properties are prepared and rheologically characterized. The rheological characterization involves steady shear-viscosity and dynamic oscillatory-shear measurements to quantify the viscous and elastic properties respectively. The settling velocities under unbounded conditions are measured in beakers having diameters at least 25x the diameter of particles. For measuring settling velocities between parallel walls, two experimental cells with different wall spacing are constructed. Spherical particles of varying sizes are gently dropped in the fluids and allowed to settle. The process is recorded with a high resolution video camera and the trajectory of the particle is recorded using image analysis software. Terminal settling velocities are calculated from the data.The impact of elasticity on settling velocity in unbounded fluids is quantified by comparing the experimental settling velocity to the settling velocity calculated by the inelastic drag predictions of Renaud et al.¹ Results show that elasticity of fluids can increase or decrease the settling velocity. The magnitude of reduction/increase is a function of the rheological properties of the fluids and properties of particles. Confining walls are observed to cause a retardation effect on settling and the retardation is measured in terms of wall factors.     

Development and implementation of a perfusion-based high cell density cell banking process

A perfusion-based high cell density (HD) cell banking process has been developed that offers substantial advantages in time savings and simplification of upstream unit operations. HD cell banking provides the means to reduce the time required for culture inoculum expansion and scale-up by eliminating the need for multiple small to intermediate scale shake flask-based operations saving up to 9 days of operation during large-scale inoculum expansion. HD perfusion cultures were developed and optimized in a disposable Wave bioreactor system. Through optimization of perfusion rate, rocking speed and aeration rate, the perfusion system supported peak cell densities of >20 × 10(6) cells/mL while maintaining high cell viability (≥ 90%). The cells were frozen at HD (90-100 × 10(6) viable cells/mL) in 5-mL CryoTube vials. HD cell banks were demonstrated to enable direct inoculation of culture into a Wave bioreactor in the inoculum expansion train thus eliminating the need for intermediate shake flask expansion unit operations. The simplicity of the disposable perfusion system and high quality of the cell banks resulted in the successful implementation in a 2000 L scale manufacturing facility.     

Enhancement of productivity of recombinant α-amidating enzyme by low temperature culture

We have produced a recombinant C-terminal α-amidating enzyme (799BglIIα-AE) derived from Xenopus laevis by culturing a CHO cell line named 3μ-1S. Recently, we demonstrated that culturing 3μ-1S cells at a temperature below 37 °C led to the following phenomena: inhibited cell growth with high viability, enhanced cellular productivity (maximally at 32 °C), and suppressed medium consumption and release of impurities from the cells. Therefore, it is suggested that the 799BglIIα-AE production will be increased by culturing a sufficient number of the cells at a low temperature (especially at 32 °C). To assess this effect on batch and perfusion cultures, the culture temperature was shifted from 37 to 32 °C in the mid-exponential phase in the case of batch culture and from 37 to 34 °C when the cell density became high enough in the case of perfusion culture. Application of the low temperature culture to batch and perfusion cultures was effective in comparison with the culture at 37 °C: the productivity per medium and the productivity per time were increased severalfold with enhanced cellular productivity at a low culture temperature. The low temperature culture also increased the relative content of 799BglIIα-AE in the supernatant and reduced the glucose consumption. The method presented here would contribute to production of bioactive proteins using other recombinant cell lines. This revised version was published online in August 2006 with corrections to the Cover Date.     

Production of human-mouse chimeric antibody by high cell density perfusion culture

Two mouse myeloma cell lines which were transfected with chimeric mouse variable-human constant immunoglobulin heavy and light chain genes have been cultured at high cell density in a settling perfusion culture vessel to produce chimeric antibody specific for human common acute lymphocytic leukemia antigen (cALLA).J558L transfectant proliferated well in a serum-free medium (ITES-eRDF) to a viable cell density of 3.7×10⁷ cells/ml and produced chimeric antibody to a maximum value of 60 g/ml in 120 ml scale vessel. X63Ag8.653 transfectant reached a density of 1.9×10⁷ cells/ml in 1.2 I scale vessel in serum supplemented medium (10% FCS-eRDF) and produced chimeric antibody which consisted of chimeric gamma and chimeric kappa chains to a maximum value of 5.8 g/ml.     

“Differentiation Induction” culture of human leukemic myeloid cells stimulates high production of macrophage differentiation inducing factor

We recently developed a new culture system based on dialysis perfusion (designated JCC-device) for the generation and expansion of human lymphokine-activated killer (LAK) cells (Murata et al., 1990). More recently we have scaled up the volume of the culture vessel of the JCC-device from 100 ml to 400 ml for clinical use. In the present study, using this new 400 ml JCC-device, we cultured human lymph node lymphocytes (LNL) obtained from 8 surgical patients with primary lung cancer, and investigated the cellular characteristics in comparison with a conventional batchwise culture system using tissue culture dishes. With the JCC-device, the cell density reached a maximum 2.7×10⁷ cells/ml with greater than 90% viability by the appropriate exchange of perfusion medium and by making additions at the appropriate intervals for recombinant interleukin-2 (rIL-2). The expansion fold of LNL with the JCC-device, ranging 6.6- to 19.2-fold (mean 13.8-fold), was not significantly different from that in dish cultures. There was no marked difference in cell surface phenotypes between the two culture systems in 7 out of 8 cases. As for LAK activity of LNL, the JCC culture was either superior or equal in 4 out of 8 cases, but inferior in the other 4 cases to the conventional dish cultures. In the latter cases, the usage of serum for the JCC culture was limited, which might have resulted in the low LAK activity. The JCC-device was able to reduce the consumption of basal medium, rIL-2 and serum by 20%, 84% and 96%, respectively compared to the conventional tissue culture systems. The JCC-device improved the routine performance of adoptive immunotherapy with LAK cells and rIL-2.Abbreviations LAK lymphokine-activated killer - rIL-2 recombinant interleukin-2 - LNL lymph node lymphocytes - BM basal medium - CM complete medium - HBSS Hanks balanced salt solution - JRU Japan reference unit     

Retroviral vector production using suspension-adapted 293GPG cells in a 3L acoustic filter-based perfusion bioreactor

Recombinant retroviruses are now an established tool for gene delivery. Presently they are mainly produced using adherent cells. However, due to the restrictive nature of adherent cell culture, this mode of production is hampered by low cell-specific productivity and small production units. The large-scale production of retroviral vectors could benefit from the adaptation of retrovirus packaging cell lines to suspension culture. Here, we describe the ability of a 293 packaging cell line to produce retroviral vectors in suspension culture at high titer. Adherent 293GPG cells, producing a Moloney Murine Leukemia Virus (MoMLV) retrovirus vector pseudotyped with the vesicular stomatitis virus G (VSVG) envelope protein and expressing a TK-GFP fusion protein, were adapted to suspension culture in calcium-free DMEM. At a cell density similar to adherent cell culture, the suspension culture produced retroviral vector consistently in the range of 1 x 10(7) infectious viral particles/mL (IVP/mL), with a specific productivity threefold higher than adherent culture. Furthermore, at the same medium replacement frequency, the suspension producer cells could be cultured at higher density than their adherent counterparts, which resulted in virus titer of 3-4 x 10(7) IVP/mL at 11.0 x 10(6) cells/mL. This corresponds to a 10-fold increase in viral concentration compared to adherent cells. The capacity to up scale the retroviral vector production was also demonstrated by performing a 2 VVD perfusion culture for 9 days in a 3L Chemap bioreactor. The combination of suspension and perfusion led to a 20-fold increase in maximum virus productivity compared to the adherent culture.     

In vitro behaviour of human osteoblasts on dentin and bone

This investigation studied how the behaviour of isolated osteoblasts on standard tissue culture polystyrene compared with cells cultured on cut surfaces of dentin, a natural calcified material. Cellular attachment, viability and growth were monitored in parallel cultures of human osteosarcoma cell lines (MG63, HOS TE85, SaOS-2) and primary human osteoblast-like cells (HOBs). Culture plastic was either left untreated or roughened with abrasive paper of various grit sizes (4000-1200 grit) in order to obtain a level of roughness comparable to that of the dentin slices. Cell counting and intracellular BCECF staining showed that after an initial incubation of 2 h, the primary cells attached and spread out more quickly on the different substrates than the three cell lines. The primary cells also showed a stronger mitochondrial staining and viability on dentin. During subsequent culture morphological differences appeared with the cells on dentin displaying more cellular extensions. All three cell lines proliferated more slowly on dentin than on plastic. In contrast, the primary HOBs were not significantly affected in their growth by the different substrates. Total and specific alkaline phosphatase (AP) activity of the cell lines was not significantly affected by the different substrates after short-term adhesion, but it was increased for the primary cells on the dentin. However, after 2-3 days of culture, AP was decreased on the dentin slices for both the cell lines and primary HOBs. Plasma treatment of the roughened plastic did not alter cellular viability or AP activity, suggesting that grinding of the surface did not affect the property of the culture plastic to support cell attachment and growth. In conclusion, the results show that not only do osteoblastic cells behave differently on a natural calcified substrate surface than on standard culture plastic, but also that differences were evident between the various cell types, in particular the primary HOB versus the continuous cell lines.     

Establishment of phagocytic cell lines from larval hemocytes of the beet armyworm, Spodoptera exigua

Hemolymph was taken from beet armyworm (Spodoptera exigua) larvae and a new hemocyte cell line (SeHe920-1a) was established by supplementing the culture medium with a reduced form of glutathione to avoid the activation of prophenoloxidase cascade. To evaluate the phagocytic ability of the SeHe920-1a cells, polystyrene microspheres of two sizes (6.14 +/- 0.45 microm and 2.84 +/- 0.14 microm in diameter) and inactivated spores of an entomopathogenic microsporidium, Vairimorpha sp. NIS M12 (5.10 +/- 0.21 microm x 2.00 +/- 0.11 microm), were introduced into the cell culture. The SeHe920-1a cells had higher phagocytic ability than other lepidopteran cell lines that were not derived from the hemocytes. When microsporidian spores were inoculated, 27% of SeHe920-1a cells were observed to take up spores (average 1.7 spores per cell). By cloning SeHe920-1a cells, 12 cell lines were established and designated SeHe920Y1 to SeHe920Y12. In comparison with the parental cell line, phagocytic activity was enhanced in SeHe920Y6, SeHe920Y10, and SeHe920Y11 cell lines and especially in the SeHe920Y7 cell line, where approximately 50% of cells were phagocytic and the average number of microsporidian spores engulfed per cell was twice that of the SeHe920-1a cell line.     

Perfusion culture apparatus for suspended mammalian cells

A variety of processes have been proposed for mammalian cell culture in the commercial production of useful substances (e.g., monoclonal antibodies, therapeutic and diagnostics proteins). Among them, the perfusion culture of suspended non-immobilized cells is the most advantageous. Perfusion culture can be classified by the separation process of suspended cells from the culture mixture into three types, namely filtration, gravitational settling and centrifugation. From a commercial point of view, the present situation and technical problems of suspended-cell perfusion culture will be reviewed based on the three types, The recent development of perfusion culture has been carried out mainly on the filtration separation process, but the centrifugation process seems to have a promising future because of operation stability and scale-up feasibility. The reasons will be explained in details.     

NS0 cell damage by high gas velocity sparging in protein-free and cholesterol-free cultures

Recent developments in high cell density and high productivity fed-batch animal cell cultures have placed a high demand on oxygenation and carbon dioxide removal in bioreactors. The high oxygen demand is often met by increasing agitation and sparging rates of air/O2 in the bioreactors. However, as we demonstrate in this study, an increase of gas sparging can result in cell damage at the sparger site due to high gas entrance velocities. Previous studies have showed that gas bubble breakup at the culture surface was primarily responsible for cell damage in sparged bioreactors. Such cell damage can be reduced by use of surfactants such as Pluronic F-68 in the culture. In our results, where NS0 cells were grown in a protein-free and cholesterol-free medium containing 0.5 g/L Pluronic F-68, high gas entrance velocity at the sparger site was observed as the second mechanism for cell damage. Experiments were performed in scaled-down spinners to model the effect of hydrodynamic force resulting from high gas velocities on antibody-producing NS0 cells. Cell growth and cell death were described by first-order kinetics. Cell death rate constant increased significantly from 0.04 to 0.18 day(-1) with increasing gas entrance velocity from 2.3 to 82.9 m/s at the sparger site. The critical gas entrance velocity for the NS0 cell line studied was found to be approximately 30 m/s; velocities greater than 30 m/s caused cell damage which resulted in reduced viability and consequently reduced antibody production. Observations from a second cholesterol-independent NS0 cell line confirmed the occurrence of cell damage due to high gas velocities. Increasing the concentration of Pluronic F-68 from 0.5 to 2 g/L had no additional protective effect on cell damage associated with high gas velocity at the sparger. The results of gas velocity analysis for cell damage have been applied in two case studies of large-scale antibody manufacturing. The first is a troubleshooting study for antibody production carried out in a 600 L bioreactor, and the second is the development of a gas sparger design for a large bioreactor scale (e.g., 10,000 L) for antibody manufacturing.     

Perfusion system for studying peptide secretion from endocrine cells with high time resolution

To study the secretion from endocrine cells in culture, we have developed a cell column perfusion system with a time resolution of 4 s. The core of the system is a perfusion chamber with a cell-supporting matrix of monosized polystyrene beads. The particles are solid and can withstand a high pressure gradient without deformation. The minimum amount of cell material required to obtain detectable levels of secretory products is a function of the assay sensitivity, perfusion flow, fraction volume and time resolution. The volume of the perfusion chamber is therefore adjustable to satisfy varying demands of minimum cell number. The general flow characteristics of the system were characterized using radiolabeled substances of various molecular sizes. Using the system in secretory studies of rat pituitary tumor (GH4C1) cells, we have identified differences in secretion profiles that may be related to the kinetics of the different transmembrane and intracellular mechanisms involved.     

Perfusion bioreactors for the production of recombinant proteins in insect cells

Conclusion High density perfusion culture of insect cells for the production of recombinant proteins has proved to be an attractive alternative to batch and fed-batch processes. A comparison of the different production processes is summarized in Table 3. Internal membrane perfusion has a limited scale-up potential but appears to the method of choice in smaller lab-scale production systems. External membrane perfusion results in increased shear stress generated by pumping of cells and passing through microfiltration modules at high velocity. However, using optimized perfusion strategies this shear stress can be minimized such that it is tolerated by the cells. In these cases, perfusion culture has proven to be superior to batch production with respect to product yields and cell specific productivity. Although insect cells could be successfully cultivated by immobilization and perfusion in stationary bed bioreactors, this method has not yet been used in continuous processes. In fluidized bed bioreactors with continuous medium exchange cells showed reduced growth and protein production rates.For the cultivation of insect cells in batch and fedbatch processes numerous efforts have been made to optimize the culture medium in order to allow growth and production at higher cell densities. These improved media could be used in combination with a perfusion process, thus allowing substantially increased cell densities without raising the medium exchange rate. However, sufficient oxygen supply has to be guaranteed during fermentation in order to ensure optimal productivity.     

AN ANALYSIS OF VARIABILITY IN SEED SETTLING VELOCITIES OF SEVERAL WIND-DISPERSED ASTERACEAE

Dispersal is an important life history component. Seed settling velocity may be a useful surrogate for the measurement of dispersal ability in wind-dispersed plants, particularly those whose seeds have plumose dispersal structures. I measured settling velocities on seeds of eight species of Asteraceae, including annuals, biennials, and perennials, and including both native and introduced species. The species are Aster exilis, Picris echioides, Chrysopsis villosa, Heterotheca grandiflora, Conyza bonariensis, Sonchus oleraceous, Senecio vulgaris, and Taraxacum officinale. From these data I estimated components of total variation in seed settling velocities due to differences among species, among plants within species, and among inflorescences and seeds within plants. Significant amounts of variability were found at all levels. Contrasts among mean settling velocities showed that the five introduced species have lower settling velocities than the three native species; this result continues to be true when annuals are considered separately from biennials and perennials. Also, over all eight species, annuals have lower settling velocities than biennials and perennials. Variability among species apparently reflects different dispersal “strategies” employed by the species; these different strategies may be correlated with other life-history traits and with ecological characteristics. Variability within species also may have ecological consequences in that such variability may represent an example of risk-spreading.     

Influence of alterations in culture condition and changes in perfusion parameters on the retention performance of a 20 μm spinfilter during a perfusion cultivation of a recombinant CHO cell line in pilot scale

Since 1969 much attention has been devoted to the useof spinfilter systems for retention of mammalian cellsin continuous perfusion cultivations. Previousinvestigations dealt with hydrodynamic conditions,fouling processes and upscaling. But hydrodynamicconditions and fouling processes seem to have asecondary importance in spinfilter performance duringauthentic perfusion cultivations. Obviously,alterations in culture condition are more relevantespecially during long-term processes. Therefore, ourpratical approach focussed on the performance qualityof a commercially available 20 m spinfilterduring a perfusion cultivation of a recombinant CHOcell line in pilot scale regarding the followingissues: 1) retention of viable cells in thebioreactor; 2) removal of dead cells and cell debrisfrom the bioreactor; 3) alterations in culturecondition; and 4) changes in perfusion mode.Furthermore, we tested the performance of 20 mspinfilters in 2 and 100 l pilot scale using solidmodel particles instead of cells. Our investigationsshowed that retention of viable cells in pilot scalewas independent of spinfilter rotation velocity andperfusion rate; the retention increased from 75 to 95%corresponding to operation time, enlarging celldiameter and enhanced formation of aggregates in theculture during the perfusion cultivation. By means ofthe Cell Counter and Analyzer System (CASY) anoperation cut off of 13 m was determined forthis spinfilter. Using solid model particles in 2 lscale, optimal retention was achieved at a tip speedof 0.43 m s^-1 (141 rpm) – furtherenhancement of spinfilter rotation velocity up to0.56 m s^-1 (185 rpm) decreased the retentionrapidly. In pilot scale best retention performance wasobtained with tip speeds of 0.37 m s^-1(35 rpm) and 1.26 m s^-1 (120 rpm). Hence,significant retention in pilot scale could already beachieved with low agitation. Therefore, the additionof shear force protectives could be avoided so thatthe purification of the target protein from thesupernatant would be facilitated.     

Anti-apoptotic genes Aven and E1B-19K enhance performance of BHK cells engineered to express recombinant factor VIII in batch and low perfusion cell culture

The engineering of production cell lines to express anti-apoptotic genes has been pursued in recent years due to potential process benefits, including enhanced cell survival, increased protein expression, and improved product quality. In this study, a baby hamster kidney cell line secreting recombinant factor VIII (BHK-FVIII) was engineered to express the anti-apoptotic genes Aven and E1B-19K. In high cell density shake flask culture evaluation, 11 clonal cell lines expressing either E1B-19K or a combination of Aven and E1B-19K showed improved survival compared to both parental and blank vector cell line controls. These cell lines exhibited lower caspase-3 activation and reduced Annexin-V binding compared to the controls. Parental and blank vector cell lines were less than 50% viable after 48 h of exposure to thapsigargin while cell lines expressing E1B-19K with or without Aven maintained viabilities approaching 90%. Subsequently, the best Aven-E1B-19K candidate cell line was compared to the parental cell line in 12-L perfusion bioreactor studies. Choosing the appropriate perfusion rates in bioreactors is a bioprocess optimization issue, so the bioreactors were operated at sequentially lower specific perfusion rates, while maintaining a cell density of 2 x 10(7) viable cells/mL. The viability of the parental cell line declined from nearly 100% at a perfusion rate of 0.5 nL/cell/day to below 80% viability, with caspase-3 activity exceeding 15%, at its lower perfusion limit of 0.15 nL/cell/day. In contrast, the Aven-E1B-19K cell line maintained an average viability of 94% and a maximum caspase-3 activity of 2.5% even when subjected to a lower perfusion minimum of 0.1 nL/cell/day. Factor VIII productivity, specific growth rate, and cell size decreased for both cell lines at lower perfusion rates, but the drop in all cases was larger for the parental cell line. Specific consumption of glucose and glutamine and production of lactate were consistently lower for the Aven-E1B-19K culture. Furthermore, the yield of ammonia from glutamine increased for the Aven-E1B-19K cell line relative to the parent to suggest altered metabolic pathways following anti-apoptosis engineering. These results demonstrate that expression of anti-apoptotic genes Aven and E1B-19K can increase the stability and robustness of an industrially relevant BHK-FVIII mammalian cell line over a wide range of perfusion rates.