Scale up cultivation of primary human umbilical vein endothelial cells on microcarriers from spinner vessels to bioreactor fermentation

Five types of dextran-based microcarriers (Dormacell, Pfeifer and Langen) with different concentrations of dimeric DEAE anion-exchange groups (nitrogen contents from 1.2 up to 2.9%) were tested as growth substrates for the cultivation of human umbilical vein endothelial cells (HUVECs). All microcarriers were gelatinized before use to improve cell adhesion. The one with the highest DEAE-group density was found to be most suitable for HUVEC propagation reaching final cell densities of 8×10⁵ viable cells ml^-1 (95% viability) using microcarrier concentrations of 3 g l^–1. Furthermore, metabolic data of glucose/lactate and amino acid metabolism are presented in this study. The concentrations of 18 amino acids were monitored throughout cultivation. A considerable decrease of glutamine and inverse increase of glutamate was observed. Cultivation with initial glucose concentration of 16.5 mmol l^–1 resulted in high glutamine consumption rates, whereas high glucose-supplemented starting culture medium (30 mmol l^-1) gave considerably lowered rates, indicating altered glutamine metabolism due to different glucose feeding. The glucose consumption and lactate production rates increased 2.6 fold and 3.5 fold, respectively, due to switch over from low to high glucose supplemented cultures. The rate of glucose metabolism was found not to be directly related to cell growth, because almost identical growth rates and doubling times were obtained. Considering the remaining 16 amino acids measured, serine concentrations considerably declined and glycine as well as alanine concentrations raised strongly. Most amino acid values were found insignificantly altered during 14 days of cultivation. Spinner vessel cultures served as inoculum for up scale propagation of HUVECs in membrane stirred 2 liter bioreactors. About 5×10⁹ HUVECs were produced, which were used for the isolation and structural characterization of glycosphingolipids, cell membrane compounds, which are suggested to be involved in e.g. selectin-carbohydrate interaction (cell-cell adhesion), carcinogenesis and atherogenesis.Abbreviations HUVECs human umbilical vein endothelial cells - PBS phosphate buffered saline     

Expansion of human mesenchymal stem cells on microcarriers

The effects on human mesenchymal stem cell growth of choosing either of two spinner flask impeller geometries, two microcarrier concentrations and two cell concentrations (seeding densities) were investigated. Cytodex 3 microcarriers were not damaged when held at the minimum speed, N_JS, for their suspension, using either impeller, nor was there any observable damage to the cells. The maximum cell density was achieved after 8–10 days of culture with up to a 20-fold expansion in terms of cells per microcarrier. An increase in microcarrier concentration or seeding density generally had a deleterious or neutral effect, as previously observed for human fibroblast cultures. The choice of impeller was significant, as was incorporation of a 1 day delay before agitation to allow initial attachment of cells. The best conditions for cell expansion on the microcarriers in the flasks were 3,000 microcarriers ml⁻¹ (ca. 1 g dry weight l⁻¹), a seeding density of 5 cells per microcarrier with a 1 day delay before agitation began at N_JS (30 rpm), using a horizontally suspended flea impeller with an added vertical paddle. These findings were interpreted using Kolmogorov’s theory of isotropic turbulence.     

Growth of Fish Cell Lines on Microcarriers

Microcarrier beads were evaluated as substrates for the propagation of five anchorage-dependent fish cell lines. Growth of rainbow trout gonad (RTG-2) and Atlantic salmon cells was limited on microcarriers maintained in suspension. However, stationary microcarriers were suitable substrates for the growth of RTG-2, AS, Chinook salmon embryo (CHSE-214), and fathead minnow cells. Cell yields ranged from 2 × 10⁶ to 2.9 × 10⁶ cells per ml, representing 7- to 10-fold increases over the initial cell concentrations. The yield of new RTG-2 cells per unit volume of growth medium was 2.8 times greater in microcarrier cultures than in standard monolayer cultures. Northern pike cells failed to grow on microcarriers. Yields of infectious pancreatic necrosis virus propagated in microcarrier cultures of RTG-2 cells were more than twice the yields in standard monolayer cultures. The greater economy of microcarrier cultures in terms of growth vessel and medium requirements holds great promise for the large-scale production of anchorage-dependent fish cell cultures and fish viruses.     

Bead-to-bead transfer of chinese hamster ovary cells using macroporous microcarriers

Chinese hamster ovary cells (CHO-K1) were cultivated in macroporous gelatin microcarriers (CultiSpher G and CultiSpher S) in spinner flasks and a 5 1 bioreactor. Near-to-confluent cultures were harvested by bead-to-bead transfer where intact microcarriers with cells were transferred from a spinner flask to another spinner flask or to the bioreactor with naked microcarrier beads. Successful bead-to-bead transfer was achieved in various split ratios. The duration of attachment seemed to be important where the direct contact of beads to each other can be achieved by intermittent stirring. Repeated transfers were performed and at least four transfers in spinner flasks were achieved.Two variations of bead-to-bead transfer were performed in the 5 1 bioreactor either by seeding the bioreactor with near-to-confluent beads cultivated in spinner flasks orin situ transfer by adding fresh beads to the bioreactor. As in the spinner case, attachment was achieved by intermittent stirring where donor beads were in close proximity to the acceptor beads. Again successful transfers were obtained as evidenced by the good growth on acceptor beads where cell yields were in the range of 3100–4500 cells/bead.The results suggest that bead-to-bead transfer of CHO-K1 cells can be easily performed and do provide an alternative route to applications where dissolution techniques may not offer an efficient solution.     

Pure gelatin microcarriers: Synthesis and use in cell attachment and growth of fibroblast and endothelial cells

Summary A new type of microcarrier was described using bead emulsion-polymerization techniques. An aqueous solution of gelatin and glutaraldehyde was dispersed in a hydrophobic phase of mineral oil, using Triton X-114 as an emulsifier, and polymerization was initiated. The resultant spherical beads, composed entirely of gelatin, showed excellent mechanical stability to ethanol drying, sterilization, and long-term use in microcarrier spinner cultures. The solid gelatin microcarriers supported the growth of L-929 fibroblast, swine aorta endothelial, human umbilical endothelial, and HeLa-S₃ cultures with no adverse effects on cell morphology or growth. The beads were transparent in growth medium and attached cells were clearly visualized without staining. The beads were also compatible with techniques for scanning electron microscopy. Collagenase could be used to entirely digest the gelatin beads, leaving the cells free from microcarriers and suspended in solution while retaining 98% cell viability. The results further showed that after collagenase treatment the cells would populate fresh gelatin microcarriers and grow to confluence. Cell attachment kinetics revealed that the endothelial cells attached to the gelatin beads at the same rate as to tissue culture plates, whereas the fibroblast cells attached to the beads more slowly. However, once the fibroblast cells were attached to the gelatin microcarriers they spread and grew normally. This research was supported in part by the National Institutes of Health (GN 29127) and Ventrex Laboratories, Portland, Maine.     

Human diploid fibroblast growth on polystyrene microcarriers in aggregates

Polystyrene microcarriers were prepared in four size ranges (53–63 m, 90–125 m, 150–180 m and 300–355 m) and examined for ability to support attachment and growth of human diploid fibroblasts. Cells attached rapidly to the microcarriers and there was a direct relationship between cell attachment and microcarrier aggregation. Phasecontrast and scanning electron microscopic studies revealed that while aggregation was extensive, most of the aggregate consisted of void volume. Cell growth studies demonstrated that human diploid fibroblasts proliferated well in microcarrier aggregates, reaching densities of 2.5–3×10⁶ cells per 2 ml dish after 6 days from an inoculum of 0.5×10⁶ cells per dish. When cells were added to the microcarriers at higher density (up to 5×10⁶ cells per 2-ml culture), there was little net growth but the cells remained viable over a 7-day period. In contrast, cells died when plated under the same conditions in monolayer culture. When the microcarriers were used in suspension culture, rapid cell attachment and rapid microcarrier aggregation also occurred. In 100-ml suspension culture, a cell density of 0.7×10⁶ cells per ml was reached after 7 days from an inoculum of 0.1×10⁶ cells. Based on these data, we conclude that microcarrier aggregation is not detrimental to fibroblast growth. These data also indicate that small microcarriers (53–63 m) (previously thought to be too small to support the growth of diploid fibroblasts) can support fibroblast growth and this occurs primarily because microcarriers in this size range efficiently form aggregates with the cells.     

Hydrodynamic behaviour of animal cell microcarrier suspensions in split-cylinder airlift bioreactors

Hydrodynamic characteristics of suspensions of microcarriers used for culturing anchorage dependent animal cells are reported in split-cylinder internal-loop airlift bioreactors. Cell culture media are simulated using salt solutions that duplicate the ionic strengths of typical media. Effects of solids loading (0–30 kg·m^–3), microcarrier particle size (150–300×10^–6 m diameter) and density (1030–1050 kg·m^–3) on gas induced circulation of the slurry, mixing time, gas holdup and gas velocity requirements to attain complete suspension of solids are discussed for two reactors with aspect ratios of 7.6 and 14.5, but equal riser-to-downcomer cross-sectional area ratios of 1.0, aerated at low air flow rates (0–8×10^–6 m³·s^–1) through a sintered glass sparger with 110×10^–6 m diameter pores. The study covers the ranges of solids concentrations, types, densities, particle sizes and aeration rates that are of relevance in animal cell culture applications.Airlift bioreactors displayed suitable hydrodynamic characteristics for potentially supporting anchorage dependent cell cultures on microcarriers at carrier loadings similar to those that are currently used in stirred tank bioreactors. The minimum gas flow rates and the induced liquid circulation rates necessary to achieve and maintain suspension of the heaviest and the largest microcarriers were well within practicable limits, limits which have been shown to be withstood by animal cells in non-anchorage dependent suspension culture in airlift bioreactors. No floatation problems were encountered with the carriers, nor was sedimentation a problem so long as the identified minimum suspension criteria were met. Chisti's liquid circulation equation, originally intended for two-phase flow, applied to the three-phase gas-liquid-microcarrier systems.     

Improvement of the culture stability of non-anchorage-dependent animal cells grown in serum-free media through immobilization

A murine hybridoma cell line producing a monoclonal antibody against penicillin-G-amidase and a murine transfectoma cell line secreting a monovalent chimeric human/mouse Fab-antibody fragment were cultivated in three different media (serum-containing, low protein serum-free, and iron-rich protein-free) in flask cultures, stirred reactors and a fixed bed reactor. In static batch cultures in flasks both cell lines showed similar good growth in all three media.In suspension in a stirred reactor, the hybridoma cell line could be cultivated satisfactory only in serum-containing medium. In low protein serum-free medium, Pluronic F68 had to be added to protect the hybridoma cells against shear stress. But even with this supplement only batch, not chemostat mode was possible. In iron-rich protein-free medium the hybridoma cells grew also in continuous chemostat mode, but the stability of the culture was low. The transfectoma cell line did not grow in stirred reactors in any of the three media.Good results with both cell lines were obtained in fixed bed experiments, where the cells were immobilized in macroporous Siran^®-carriers. The media, which were optimized in flask cultures, could be used without any further adaptation in the fixed bed reactor. Immobilization improved the stability and reliability of cultures of non-adherent animal cells in serum-free media tremendously compared to suspension cultures in stirred reactors. The volume-specific glucose uptake rate, an, indicator of the activity of the immobilized cells, was similar in all three media. Deviations in the metabolism of immobilized and suspended cells seem to be mainly due to low oxygen concentrations within the macroporous carriers, where the cells are supplied with oxygen only by diffusion.List of symbols c substrate or product concentration mmol l^–1 - c₀ substrate or product concentration in the feed mmol l^–1 - c_Glc glucose concentration mmol l^–1 - c_Gln glutamine concentration mmol l^–1 - c_Amm ammonia concentration mmol l^–1 - c_Lac lactate concentration mmol l^–1 - c_FAB concentration of Fab# 10 antibody fragment g l^–1 - c_MAb monoclonal antibody concentration mg l^–1 - D dilution rate d^–1 - q cell-specific substrate uptake or metabolite production rate mmol cell^–1 h^–1 - q_Glc cell-specific glucose uptake rate mmol cell^–1 h^–1 - q_Gln cell-specific glutamine uptake rate mmol cell^–1 h^–1 - q_MAb cell-specific MAb production rate mg cell^–1 h^–1 - q^* volume-specific substrate uptake or metabolite production rate mmol l^–1 h^–1 - q^*FB volume-specific substrate uptake or metabolite production rate related to the fixed bed volume mmol l_FB ^–1 h^–1 - q^*FB,Glc volume-specific glucose uptake rate related to the fixed bed volume mmol l_FB ^–1 h^–1 - q^*FB,Gln volume-specific glutamine uptake rate related to the fixed volume mmol l_FB ^–1 h^–1 - q^*FB,MAb volume-specific MAb production rate related to the fixed volume mg l_FB ^–1 h^–1 - q^*FB,02 volume-specific oxygen uptake rate related to the fixed bed volume mmol l_FB ^–1 h^–1 - t time h - U superficial flow velocity mm s^–1 - V medium volume in the conditioning vessel of the fixed bed reactor l - V_FB volume of the fixed bed l - x_v viable cell concentration cells ml^–1 - y_Amm,Gln yield of Ammonia from glutamine - y_Lac,Glc yield of lactate from glucose - specific growth rate h^–1 - _d specific death rate h^–1     

Production of vitamin B12 in an upflow anaerobic filter continuous reactor using Acetobacterium sp.

The accumulation of biofilm by Acetobacterium sp. during continuous culture in an upflow anaerobic filter (UAF) growing on methanol-formate was the result of space velocity and inlet concentrations of substrate and Co⁺². To achieve good development of biofilm, a space velocity of 0.38 h^–1, inlet substrate concentrations of 125 mM of both methanol and formate, and Co⁺² at 0.16 mM were required. Cell productivities in the effluent of the UAF-reactor were about 6-fold higher than in chemostat cultures (0.20 g l^–1 h^–1 for UAF and 0.035 g l^–1 h^–1 for chemostat) (previous studies), and the maximum vitamin B₁₂ specific concentration was 5.1 mg g cell^–1.     

Product quality of a recombinant fusion protein expressed in immobilised baby hamster kidney cells grown in protein-free medium

Baby hamster kidney cells producing a recombinant IgG-IL2 fusion protein were grown as spinner batch cultures in a protein-free medium, with cells immobilised in porous and non-porous supports at different support concentrations and agitation rates. Product quality, i.e., integrity, decreases up to 60% with the increase in agitation rate or support concentration and from porous to non-porous supports. LDH activity is a good indicator for the monitoring of product degradation, and thus product quality. Optimal conditions regarding titre of intact product were achieved at 60 rpm with 2 g porous support l^–1.     

人皮肤成纤维细胞在不同培养系统中的生长代谢特性

大面积烧伤病人及多种皮肤溃疡病人很难用自体皮肤移植来进行治疗.早期治疗方法采用尸体来源的皮肤移植,但由于来源有限、且有传播疾病的危险,因此应用组织工程技术构建生物活性人工皮肤已成为近十几年来在组织工程和创伤治疗领域的研究热点,目前已有几种人工皮肤成功地走向临床[1].然而,在构建大面积皮肤组织过程中,如何大量制备皮肤种子细胞仍然是一大棘手的难题,成为人体皮肤组织工程迫切需要解决的技术关键.获得大量扩增的皮肤细胞,解决种子细胞的供应问题,是构建人工皮肤的一个关键.     

High density microcarrier culture with a new device which allows oxygenation and perfusion of microcarrier cultures

A novel system useful for aeration and cell retention in continuous perfused microcarrier cultures is described. The system is based on a vibrating cage that separates cells and microcarriers from the oxygenation chamber and allows gas bubble free oxygen transfer. In the cultivation of monkey kidney cells (VERO) on gelatin coated microcarriers, using different concentrations (5, 10 and 15 g Cytodex 3/liter) cell densities up to 10⁷ cells per ml were obtained. The described system is scaleable.     

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.     

Defined Essential 8? Medium and Vitronectin Efficiently Support Scalable Xeno-Free Expansion of Human Induced Pluripotent Stem Cells in Stirred Microcarrier Culture Systems

Human induced pluripotent stem (hiPS) cell culture using Essential 8™ xeno-free medium and the defined xeno-free matrix vitronectin was successfully implemented under adherent conditions. This matrix was able to support hiPS cell expansion either in coated plates or on polystyrene-coated microcarriers, while maintaining hiPS cell functionality and pluripotency. Importantly, scale-up of the microcarrier-based system was accomplished using a 50 mL spinner flask, under dynamic conditions. A three-level factorial design experiment was performed to identify optimal conditions in terms of a) initial cell density b) agitation speed, and c) to maximize cell yield in spinner flask cultures. A maximum cell yield of 3.5 is achieved by inoculating 55,000 cells/cm² of microcarrier surface area and using 44 rpm, which generates a cell density of 1.4x10⁶ cells/mL after 10 days of culture. After dynamic culture, hiPS cells maintained their typical morphology upon re-plating, exhibited pluripotency-associated marker expression as well as tri-lineage differentiation capability, which was verified by inducing their spontaneous differentiation through embryoid body formation, and subsequent downstream differentiation to specific lineages such as neural and cardiac fates was successfully accomplished. In conclusion, a scalable, robust and cost-effective xeno-free culture system was successfully developed and implemented for the scale-up production of hiPS cells.     

Components in the inoculum determine the kinetics of Azotobacter vinelandii cultures and the molecular weight of its alginate

In cultures of Azotobacter vinelandii inoculated using washed cells (avoiding exhausted broth components) alginates of a higher molecular weight (1200 kDa) than those obtained in cultures conventionally inoculated (350 kDa), were produced. Also, when comparing conventionally inoculated cultures with those inoculated with washed-cells, the alginate lyase activity was delayed and the final polymer concentration decreased from 4.8 to 3.5 g l^–1. This suggests that components in the exhausted inoculum broth play important regulatory roles in alginate biosynthesis and needs to be taken into account when describing polymer biosynthesis.     

Repeated batch cultivation of rBHK cells on Cytodex 3 microcarriers: antithrombin III,amino acid,and fatty acid metabolic quotients

Anchorage-dependent human antithrombin III-producing recombinant baby hamster kidney (rBHK) cells were cultivated on Cytodex 3 microcarriers in repeated batch mode. During a 3-month experiment four different low-serum (0.025% fetal bovine serum) or serum-free medium formulations were evaluated for (a) the initial growth phase of cells and (b) the subsequent production phase, whereby two free fatty acid (FFA) supplements were examined with respect to their growth-promoting and product-formation-enhancing properties. Selected nutrient and (by)product consumption and production rates (including those for antithrombin III, amino acids, and fatty acids) are reported. The calculated metabolic quotients reflect the prevailing slow growth conditions ( approx. 0.06 day^–1) associated with microcarrier cultures. Specific antithrombin III productivities vary singificantly as a function of the feed medium supplementation with FFA. Correspondence to: G. Schmid     

Use of recombinant and synthetic peptides as attachment factors for cells on microcarriers

Polystyrene culture dishes and polystyrene microcarriers were coated with Pronectin-F and poly-l-lysine (polylysine), either alone or in combination. Pronectin-F is a recombinant peptide containing repeats of the RGD cell-attachment sequence from fibronectin. Polylysine is a polymer ofl-lysine. Pronectin-F supported attachment of Madin-Darby Canine Kidney (MDCK) cells at concentrations as low as 0.025 g/cm² of surface area. The cells rapidly spread after attachment. Polylysine at concentrations of 0.05–0.5 g/cm² also supported cell attachment but cells did not rapidly spread after attachment to this substrate. Higher concentrations of polylysine could not be used because of toxicity. When the two peptides were used in conjunction, MDCK cells attached and spread at lower peptide concentrations than they did when either substrate was used alone. These findings suggest that recombinant Pronectin-F alone or in conjunction with a cationic polymer could be a useful replacement for materials such as gelatin or collagen which are currently used as microcarrier surfaces.     

Production of a membrane-bound proteins,the human gamma-glutamyl transferase,by CHO cells cultivated on microcarriers,in aggregates and in suspension

Recombinant Chinese Hamster Ovary (CHO) cells, engineered for the production of human gamma-glutamyl transferase (GGT), have been grown on Cytodex 1 microcarriers, as aggregates, or as single cells in suspension after adaptation. GGT is a membrane bound enzyme which was not secreted during the culture period. The maximal enzyme activity was found to be directly related to the achieved maximal cell density. Culture of CHO on microcarriers yielded the fastest growth, with a specific growth rate of 0.04 h^–1, the highest cell density (near 1.3×10⁶ cells ml^–1), and the highest enzyme activity around 300 mU ml^–1, which corresponded to a specific cellular level of 20 mU 10^–5 cells. GGT could also be produced by growing CHO cells in suspension as single cells or as aggregates. Under these conditions, however, the specific CHO growth rate was significantly slower and the GGT level per cell was divided by a factor 6. Growing CHO cells without microcarriers also resulted in differences in cell metabolism, with a higher conversion yield of glutamine into ammonia, and a higher cell lysis. The catalytic kinetic constants of the enzyme were found identical for the three culture systems.     

Development of haploid asparagus embryos from liquid cultures of anther-derived calli is enhanced by ancymidol

Summary The effect of ancymidol concentration on the development of haploid asparagus embryos was determined. Liquid cultures from anther-derived calli were grown for three weeks in MS medium plus 1.0 mg l^–1 2,4-D, 0.1 mg l^–1 NAA, 0.2 mg l^–1 kinetin, 800 mg l^–1 glutamine, 500 mg l^–1 casein hydrolysate, 2% sucrose and 0.0–1.0 mg l^–1 ancymidol. Cell clumps (224–500 m) were plated on solid embryo maturation medium (MS medium plus 3% sucrose, 0.1 mg l^–1 NAA, 0.5 mg l^–1 kinetin and 0.0–1.0 mg l^–1 ancymidol) and grown for eight weeks. Ancymidol enhanced embryo maturation and germination and was more critical in the solid than liquid medium. Total embryo number did not vary among most treatments. The best response was observed when ancymidol concentrations were 0.1 and 0.5 mg l^–1 in the liquid and solid media, respectively; two-thirds of the embryos produced were bipolar and 35% of bipolar embryos germinated. Seven to 82% of plants recovered from different ancymidol treatments were haploid; the others were diploid, triploid or chimeric for ploidy level.Abbreviations NAA naphthaleneacetic acid - 2,4-D 2,4-dichlorophenoxyacetic acid - GA₃ gibberellic acid - MS Murashige and Skoog (1962)     

Enhanced Production of Human Recombinant Proteins from CHO cells Grown to High Densities in Macroporous Microcarriers

Macroporous microcarriers entrap cells in a mesh network allowing growth to high densities and protect them from high shear forces in stirred bioreactor cultures. We report the growth of Chinese hamster ovary (CHO) cells producing either recombinant human beta-interferon (β-IFN) or recombinant human tissue-plasminogen activator (t-PA) in suspension or embedded in macroporous microcarriers (Cytopore 1 or 2). The microcarriers enhanced the volumetric production of both β-IFN and t-PA by up to 2.5 fold compared to equivalent suspension cultures of CHO cells. Under each condition the cell specific productivity (Q _P) was determined as units of product/cell per day based upon immunological assays. Cells grown in Cytopore 1 microcarriers showed an increase in Q _P with increasing cell densities up to a threshold of >1 × 10⁸ cells/ml. At this point the specific productivity was 2.5 fold higher than equivalent cells grown in suspension but cell densities above this threshold did not enhance Q _P any further. A positive linear correlation (r ² = 0.93) was determined between the specific productivity of each recombinant protein and the corresponding cell density for CHO cells grown in Cytopore 2 cultures. With a cell density range of 25 × 10⁶ to 3 × 10⁸ cells/ml within the microcarriers there was a proportional increase in the specific productivity. The highest specific productivity measured from the microcarrier cultures was ×5 that of suspension cultures. The relationship between specific productivity and cell density within the microcarriers leads to higher yields of recombinant proteins in this culture system. This could be attributed to the environment within the microcarrier matrix that may influence the state of cells that could affect protein synthesis or secretion.