The protective effect of serum against hydrodynamic damage of hybridoma cells in agitated and surface-aerated bioreactors.

The effect of serum on the growth rate and metabolism of CRL-8018 hybridoma cells in an agitated, surface-aerated bioreactor was examined. In the employed well-controlled bioreactors at high agitation rates, hybridoma cells in medium containing 1% fetal bovine serum rapidly die in the presence of a vortex with accompanying gas-bubble entrainment, whereas non-agitated control cultures grow normally in medium containing 1% serum. Serum levels greater than 5% counteract the detrimental hydrodynamic effects due to agitation and bubble entrainment. The protective effect is present after short-term (less than 1 h) exposure to 10% serum concentration, suggesting a protection mechanism which is, at least in part, of a physical nature. The apparent cell yields on glucose, lactate, and glutamine decreased with decreasing growth rate due to low serum concentrations. The results are incorporated into a simple model in which the apparent growth rate is the sum of an invariable growth rate and a changing death rate.     

Sparging and agitation-induced injury of cultured animals cells: Do cell-to-bubble interactions in the bulk liquid injure cells?

It has been established that the forces resulting from bubbles rupturing at the free air (gas)/liquid surface injure animal cells in agitated and/or sparged bioreactors. Although it has been suggested that bubble coalescence and breakup within agitated and sparged bioreactors (i.e., away from the free liquid surface) can be a source of cell injury as well, the evidence has been indirect. We have carried out experiments to examine this issue. The free air/liquid surface in a sparged and agitated bioractor was eliminated by completely filling the 2-L reactor and allowing sparged bubbles to escape through an outlet tube. Two identical bioreactors were run in parallel to make comparisons between cultures that were oxygenated via direct air sparging and the control culture in which silicone tubing was used for bubble-free oxygenation. Thus, cell damage from cell-to-bubble interactions due to processes (bubble coalescence and breakup) occurring in the bulk liquid could be isolated by eliminating damage due to bubbles rupturing at the free air/liquid surface of the bioreactor. We found that Chinese hamster ovary (CHO) cells grown in medium that does not contain shear-protecting additives can be agitated at rates up to 600 rpm without being damaged extensively by cell-to bubble interactions in the bulk of the bioreactor. We verified this using both batch and high-density perfusion cultures. We tested two impeller designs (pitched blade and Rushton) and found them not to affect cell damage under similar operational conditions. Sparger location (above vs. below the impeller) had no effect on cell damage at higher agitation rates but may affect the injury process at lower agitation intensities (here, below 250 rpm). In the absence of a headspace, we found less cell damage at higher agitation intensities (400 and 600 rpm), and we suggest that this nonintuitive finding derives from the important effect of bubble size and foam stability on the cell damage process. (c) 1996 John Wiley & Sons, Inc.     

Cell inactivation in the presence of sparging and mechanical agitation

Microbial cells are more readily rendered nonviable by the combined action of air sparging and mechanical agitation than by either action along. A. bubble breakup/coalescence model that incorporates the cell-bubble encounter rate, bubble breakup rate, and death probability is proposed to describe cell inactivation in the presence of bubbles maintained through the joint action of agitation and air, which is continually fed into the impeller stream region via passive vortex entrainment from the surface above or via active sparging from below. Experimental results obtained from a fragile algal (Ochromonas malhamensis) culture are consistent with the model prediction. In particular, the specific cell death rate is linearly related to the specific bubble interfacial surface area. It is shown that cells exhibit sparging-sensitive characteristics when agitation is mild, but become sensitive to surface vortexing when agitation turns vigorous enough to introduce air entrainment. Experimental data obtained from different stirrer sizes are in good agreement with the model (c) 1992 John Wiley & Sons, Inc.     

Mechanical agitation of hybridoma suspension cultures: Metabolic effects of serum, pluronic F68, and albumin supplements

Metabolic effects of the medium supplements, fetal bovine serum (FBS), Pluronic F68, and bovine serum albumin (BSA) were compared for agitated bioreactor cultures of hybridoma cells. Agitation speeds up to 600 rpm, without entrainment of gas bubbles by sparging or vortex formation, allowed examination of cell interactions with turbulent fluid forces. For cultures in FBS-supplemented RPMI media, there was no significant effect of intense turbulent fluid shear on cell growth, metabolism, or antibody, production. Serum-free cultures (Pluronic F68 or BSA supplements) at 600 rpm demonstrated greatly increased glycolysis rates during exponential growth relative to controls. Nutrient limitations caused increased rates of decline of the viable cell concentrations and a reduction in final antibody titers by around 70%. The Pluronic F68 and BSA supplements did not lead to cell protection by modifying metabolism under conditions of intense turbulent fluid shear. Supplementing the protein-free medium with FBS reduced glycolysis rates in exponential growth phase, but this did not prevent a high rate of viable cell decline and low antibody titers. We concluded that FBS does not have a metabolic effect on cells subjected to intense turbulent fluid shear. Although the agitation conditions employed in this study were more intense than generally required for agitated bioreactor culture of hybridomas, we have demonstrated the importance of considering metabolic effects of turbulent fluid forces on cultures using nutrient-rich basal media, in addition to the considerations of gas bubble effects described by other workers. (c) 1992 John Wiley & Sons, Inc.     

Agitation effects on microcarrier and suspension CHO cells

Summary The growth properties of attachment-dependent and attachment-independent CHO cells cultured in spinner-flask bioreactors were compared to investigate cell damage from rapid agitation. Damage was attributed to bulk-fluid turbulence for attachment-dependent CHO cells and bubble breakup associated with vortex formation for attachment-independent CHO cells. Radiolabeling demonstrated that cell damage included intrinsic changes in DNA synthesis.     

Agitation increases expansion of cord blood hematopoietic cells and promotes their differentiation into myeloid lineage

Mechanical stress caused by agitation is one of the factors that can affect hematopoietic stem cell expansion in suspension bioreactors. Therefore, we have investigated the effects of agitation on umbilical cord blood hematopoietic stem cell (UCB-HSC) growth and differentiation. A comparison was made between various agitation rates (20, 40 and 60 rpm) in spinner-flask and cells cultured in glass petri dish as a static culture. Moreover, the fluid dynamic at various agitation rates of spinner-flask was analyzed to determine shear stress. The spinner-flask contained a rotational moving mixer with glass ball and was kept in tissue culture incubator. To reduce consumption of cytokines, UCB-serum was used which widely decreased the costs. Our results determined that, agitation rate at 40 rpm promoted UCB-HSCs expansion and their colony forming potential. Myeloid progenitors were the main type of cells at 40 rpm agitation rate. The results of glucose consumption and lactic acid production were in complete agreement with colony assay and expansion data and indicated the superiority of culture in spinner-flask when agitated at 40 rpm over to other agitation speeds and also static culture. Cell viability and colony count was affected by changing the agitation speed. We assume that changes in cell growth resulted from the effect of shear stress directly on cell viability, and indirectly on signaling pathways that influence the cells to differentiate.     

The role of intercellular contacts in the initiation of growth and in the development of a transiently nonculturable state by the cultures of Rhodococcus rhodochrous grown in poor media

It was found that the growth of Rhodococcus rhodochrous cells in modified Saton's medium strongly depends on the rate of culture agitation in the flask: an agitation at 250 rpm in flasks with baffles stops cell multiplication, whereas slight agitation leads to pronounced culture growth. The growth retardation phenomenon was reversible and did not manifest itself in exponential-phase cultures or when the cells were grown in a rich medium; furthermore, it was not connected with the degree of culture aeration. When agitated at a moderate rate, the bacterial cells formed aggregates in the lag phase, which broke up into single cells in the exponential phase. The inhibitory effect of vigorous agitation was removed by the addition to the medium of the supernatant (SN) of a log-phase culture grown in the same medium with moderate agitation. Vigorous agitation is thought to interfere with the cell contacts, whose establishment is necessary for the development of an R. rhodochrous culture in a poor medium, which occurs in the form of (micro) cryptic growth. When grown in modified Saton's medium, R. rhodochrous cells were capable of transition, in the prolonged stationary phase, to a resting and transiently nonculturable state. Such cells could be resuscitated by incubation in a liquid medium with the addition of the supernatant or the Rpf secreted protein. The formation of transiently nonculturable cells was only possible under the conditions of a considerable agitation rate (250-300 rpm), which prevented secondary (cryptic) growth of the culture. This circumstance indicates the importance of intercellular contacts not only for the initiation of growth but also for the transition of the bacteria to a dormant state.     

Protection of human induced pluripotent stem cells against shear stress in suspension culture by Bingham plastic fluid

Suspension culture is an important method used in the industrial preparation of pluripotent stem cells (PSCs), for regenerative therapy and drug screening. Generally, a suspension culture requires agitation to keep PSC aggregates suspended and to promote mass transfer, but agitation also causes cell damage. In this study, we investigated the use of a Bingham plastic fluid, supplemented with a polysaccharide-based polymer, to preserve PSCs from cell damage in suspension culture. Rheometric analysis showed that the culture medium gained yield stress and became a Bingham plastic fluid, after supplementation with the polymer FP003. A growth/death analysis revealed that 2 days of aggregate formation and 2 days of suspension in the Bingham plastic medium improved cell growth and prevented cell death. After the initial aggregation step, whereas strong agitation (120 rpm) of a conventional culture medium resulted in massive cell death, in the Bingham plastic fluid we obtained the same growth as the normal culture with optimal agitation (90 rpm). This indicates that Bingham plastic fluid protected cells from shear stress in suspension culture and could be used to enhance their robustness when developing a large-scale.     

Sparged animal cell bioreactors: mechanism of cell damage and Pluronic F-68 protection.

Pluronic F-68 is a widely used protective agent in sparged animal cell bioreactors. In this study, the attachment-independent Spodoptera frugiperda Sf9 insect cell line was used to explore the mechanism of this protective effect and the nature of cell damage in sparged bioreactors. First, bubble incorporation via cavitation or vortexing was induced by increasing the agitation rate in a surface-aerated bioreactor; insect cells were rapidly killed under these conditions of the absence of polyols. Supplementing the medium with 0.2% (w/v) Pluronic F-68, however, fully protected the cells. Next, cell growth was compared in two airlift bioreactors with similar geometry but different sparger design; one of these bioreactors consisted of a thin membrane distributor, while the other consisted of a porous stainless steel distributor. The flow rates and bubble sizes were comparable in the two bioreactors. Supplementing the medium with 0.2% (w/v) Pluronic F-68 provided full protection to cells growing in the bioreactor with the membrane distributor but provided essentially no protection in the bioreactor with the stainless steel distributor. These results strongly suggest that cell damage can occur in the vicinity of the gas distributor. In addition, these results demonstrate that bubble size and gas flow rate are not the only important considerations of cell damage in sparged bioreactors. A model of cell death in sparged bioreactors is presented.     

Culture of human T cells in stirred bioreactors for cellular immunotherapy applications: shear, proliferation, and the IL-2 receptor

Ex vivo expansion of T cells is a key step of many cellular immunotherapy protocols, which require large numbers of immune cells to eradicate malignant or virally infected cells. The use of stirred culture systems for T cell expansion offers many potential advantages over the static culture systems commonly used today, including homogeneity of culture conditions, ease of sampling, and implementation of control systems. Primary human T cells as well as the transformed TALL103/2 T cell line were cultured in 100-mL spinner flasks as well as 2-L bioreactors to investigate the effects of shear forces produced by agitation and sparging-based aeration on the expansion of T cells. Primary T cells could be successfully grown at agitation rates of up to 120 rpm in the spinner flasks and to 180 rpm in the bioreactors with no immediate detrimental effects on proliferation. Exposure to agitation and sparging did, however, cause a significantly increased rate of downregulation of the interleukin-2 receptor (IL-2R), resulting in lower overall expansion potential from a single stimulation as compared to static controls, with faster IL-2R downregulation occurring at higher agitation rates. For the primary T cells, no significant effects of agitation were found on expression levels of other key surface receptors (CD3, CD28, or CD62L) examined. No significant effects of agitation were observed on primary T cell metabolism or levels of cellular apoptosis in the cultures. The TALL103/2 T cell line was found to be extremely sensitive to agitation, showing severely reduced growth at speeds above 30 rpm in 100-mL spinner flasks. This unexpected increased fragility in the transformed T cell line as compared to primary T cells points out the importance of carefully selecting a model cell line which will accurately represent the characteristics of the cell system of interest.     

The Role of Intercellular Contacts in the Initiation of Growth and in the Development of a Transiently Nonculturable State by Cultures of Rhodococcus rhodochrous Grown in Poor Media

It was found that the growth of Rhodococcus rhodochrous cells in a modified Saton’s medium strongly depends on the rate of culture agitation in the flask: agitation at 250 rpm in flasks with baffles stops cell multiplication, whereas slight agitation leads to pronounced culture growth. The growth retardation phenomenon was reversible and did not manifest itself in exponential-phase cultures or when the cells were grown in a rich medium; furthermore, it was not connected with the degree of culture aeration. When agitated at a moderate rate, the bacterial cells formed aggregates in the lag phase, which broke up into single cells in the exponential phase. The inhibitory effect of vigorous agitation was removed by the addition, to the medium, of the supernatant (SN) of a log-phase culture grown in the same medium with moderate agitation. Vigorous agitation is thought to interfere with cell contact, whose establishment is necessary for the development of an R. rhodochrous culture in a poor medium, which occurs in the form of (micro) cryptic growth. When grown in a modified Saton’s medium, R. rhodochrous cells were capable of transition, in the prolonged stationary phase, to a resting and transiently nonculturable state. Such cells could be resuscitated by incubation in a liquid medium with the addition of the supernatant or the Rpf secreted protein. The formation of transiently nonculturable cells was only possible under the conditions of a considerable agitation rate (250–300 rpm), which prevented secondary (cryptic) growth of the culture. This circumstance indicates the importance of intercellular contacts not only for the initiation of growth but also for the transition of the bacteria to a dormant state.__________Translated from Mikrobiologiya, Vol. 74, No. 4, 2005, pp. 489–797.Original Russian Text Copyright © 2005 by Voloshin, Shleeva, Syroeshkin, Kaprelyants.     

Effects of methocel A15LV, polyethylene glycol, and polyvinyl alcohol on CD13 and CD33 receptor surface content and metabolism of HL60 cells cultured in stirred tank bioreactors

Flow cytometry was used to examine the effect of hydrodynamic forces in a stirred tank bioreactor on the CD13 and CD33 receptor surface content of HL60 (human promyelocytic leukemia) cells. A step increase in agitation rate from 80 to 400 rpm reduced the HL60 cell apparent growth rate and increased the CD13 receptor surface content per cell, on average, by 95%. In contrast, this step increase in agitation rate to 400 rpm decreased the CD33 receptor surface content per cell, on average, by 10%. The protective effects of 0.1% Methocel A15LV, polyethylene glycol (PEG), and polyvinyl alcohol (PVA) on CD13 and CD33 receptor surface content were examined under agitation at 300 rpm in parallel 2 L bioreactor runs. The average CD33 receptor surface content was unaffected by the presence of Methocel A15LV or PEG, while PVA had a slight protective effect. In contrast, in terms of CD13 receptor content, HL60 cells agitated at 300 rpm with Methocel A15LV, PEG, or PVA behaved like cells agitated at 80 rpm with no media additives (McDowell and Papoutsakis, 1998). That is, Methocel A15LV, PEG, and PVA prevented the transduction of mechanical forces which affect CD13 cell content. HL60 cells cultured with 0.1% A15LV, PEG or PVA under conditions of mild agitation (60 rpm) in spinner flasks exhibited glucose consumption and lactate production rates that were approximately 20% lower than values of cultures containing no additive. Under conditions of agitation at 300 rpm in the 2 L bioreactor, the presence of A15LV, PEG, and PVA reduced the HL60 glucose consumption and lactate production rates by approximately 50%. Thus, media additives can dramatically reduce lactate accumulation in agitated bioreactors due to cell growth, in addition to providing protection from cellular injury.     

Effect of mixing rate on beta-carotene production and extraction by dunaliella salina in two-phase bioreactors

beta-Carotene has many applications in the food, cosmetic, and pharmaceutical industries; Dunaliella salina is currently the main source for natural beta-carotene. We have investigated the effect of mixing rate and whether it leads to the facilitated release of beta-carotene from the cells of Dunaliella salina in two-phase bioreactors. Three pairs of bioreactors were inoculated at the same time, operated at 100, 150, and 170 rounds per minute, respectively, and illuminated with a light intensity of 700 micromol m(-2) s(-1). Each pair consisted of one bioreactor containing only aqueous phase for the blank and one containing the water phase together with dodecane, which is biocompatible with the cells. Comparison of the viability and growth of the cells grown under different agitation rates shows that 170 rpm and 150 rpm are just as good as 100 rpm. The presence and absence of the organic phase also has no influence on the viability and growth of the cells. In contrast to the growth rate, the extraction rate of beta-carotene is influenced by the stirrer speed. The extraction rate increases at a higher stirring rate. The effectiveness of extraction with respect to power input is comparable for all the applied mixing rates, even though it is slightly lower for 100 rpm than the others. The chlorophyll concentration in the organic phase remained very low during the experiment, although at higher mixing rates, chlorophyll impurity increased up to 3% (w/w) of the total extracted pigments. At 170 rpm carotenoid and chlorophyll undergo the highest extraction rate for both pigments-0.5% of the chlorophyll and 6% of the carotenoid is extracted.     

Linoleic acid improves the robustness of cells in agitated cultures

The murine hybridoma (CC9C10) was subjected to high shear rates in a spinner flask to determine the effect of various culture additives on cell survival. At 500 rpm, the half-life of the viable cell concentration in a low protein serum-free medium was 50 min. Both bovine serum albumin and Pluronic F-68 had a significant effect in protecting cells under these conditions. The effects of the two supplements were additive, so that in the presence of both supplements there was minimal cell damage at 500 rpm. The survival rate of cells grown in media supplemented with linoleic acid improved significantly under high stirring rates. Cells grown for one passage in 50 μM linoleic acid and stirred at 500 rpm had a significantly higher survival rate than control cells. For cells grown over 5 passages in 25 μM linoleic acid, the survival rate at 470 rpm was ×3 greater than that determined for control cells. This difference gradually decreased at higher stirring rates up to 610 rpm when the half-life of the viable cell population was reduced to ∼10 min. Supplementation of cultures with linoleic acid has previously been shown to result in incorporation into all three cellular lipid fractions - polar, non-polar and free fatty acid (Butler et al., 1997). Our explanation for the increased survivability of the cells at high agitation rates in the presence of linoleic acid is that the structural lipid components of the cell including the outer membrane attained a higher unsaturated/saturated ratio which was more robust than that of control cells. This revised version was published online in July 2006 with corrections to the Cover Date.     

The effect of agitation and aeration on the synthesis and molecular weight of gellan in batch cultures of Sphingomonas paucimobilis

The effects of agitation and aeration upon synthesis and molecular weight of the biopolymer gellan were systematically investigated in batch fermenter cultures of the bacterium, Sphingomonas paucimobilis. High aeration rates and vigorous agitation enhanced growth of S. paucimobilis. Although gellan formation occurred mainly in parallel with cell growth, the increase in cells able to synthesise gellan did not always lead to high gellan production. For example, at very high agitation rates (1000 rpm) growth was stimulated at the expense of biopolymer synthesis.Maximal gellan concentration was obtained at 500 rpm agitation and either 1 or 2 vvm aeration (12.3 and 12.4 g/l gellan, respectively). An increase in aeration (from 1 to 2 vvm) enhanced gellan synthesis only at low agitation rates (250 rpm). However, high aeration or dissolved oxygen was not necessary for high gellan synthesis, in fact oxygen limitation always preceded the phase of maximum gellan production and probably enhanced polysaccharide biosynthesis.Some gellan was formed even after glucose exhaustion. This was attributed to the intracellular accumulation of polyhydroxyalkanoates, (such as polyxydroxybutyrate) which were found in S. paucimobilis cells indicating the existence of a carbon storage system, which may contribute to gellan biosynthesis under glucose-limiting conditions.The autolysis of the culture, which occurred at the late stages of the process, seemed to be triggered mainly by limitations in mass (nutrient) transfer, due to the highly viscous process fluid that gradually develops. Rheological measurements generally gave a very good near real time estimate of maximum biopolymer concentration offering the possibility of improved process control relative to time consuming gravimetric assay methods.While mechanical depolymerisation of gellan did not occur, high aeration rates (2 vvm) led to production of gellan of low molecular weight (at either 250 or 500 rpm). This effect of aeration rate upon gellan molecular weight is reported here for the first time, and is important for the properties and applications of gellan. Mechanisms which may have led to this are discussed, but control of molecular weight of the biopolymers is clearly an area needing further research.     

Human hematopoietic progenitor cells grow faster under rotational laminar flows

We report significant and reproducible growth acceleration of human progenitor cells when exposed to rotational flow when compared with stationary conditions. Nonenriched CD34+ umbilical cord derived human hematopoietic progenitor cells were cultured in Petri dishes located at different radial distances with respect to the central axis of a rotating platform. Growth dynamics under 3 or 5 rpm agitation was compared against that observed under typical stationary conditions. Cells cultured at 3 or 5 rpm exhibited (a) the absence of a latency phase, (b) an increase in final cell concentrations by 54–58.5%, and (c) reduced doubling time in their exponential phase by 12–16% in comparison with stationary culture. Cells grown under rotational agitation were confirmed to remain CD34+ by PCR. These results document a significant positive effect of exposure to laminar flow fields on the growth of human hematopoietic progenitor cells. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

The effects of cells on oxygen transfer in bioreactors

Cells may affect oxygen transfer rates by three mechanisms: respiration of cells accumulated at the gas/liquid interface, physical presence of cells as solid particles, and modification of the medium by cells. These effects were studied experimentally in bubble-aerated bioreactors using baker's yeast at different cell concentrations, agitation speeds, aeration rates, and specific oxygen uptake rates. The overall effect of cells was to enhance oxygen transfer rates. The physical presence of cells as solid particles was found to retard oxygen transfer, presumably due to the lower oxygen permeability in the cell layer accumulated near the bubble surfaces. Cell respiration and medium modification, on the other hand, enhanced oxygen transfer rates. The retardation by nonrespiring cells and the enhancement due to cell respiration were found stronger at higher agitation speeds and lower aeration rates employed. This was attributed to the higher interfacial cell accumulation associated with the smaller bubbles produced under these conditions in the systems studied.     

Scale-up of virus-like particles production: effects of sparging, agitation and bioreactor scale on cell growth, infection kinetics and productivity

The baculovirus-insect cells expression system was used for the production of self-forming Porcine parvovirus (PPV) like particles (virus-like particles, VLPs) in serum-free medium. At 2l bioreactor scale an efficient production was achieved by infecting the culture at a concentration of 1.5 x 10(6)cells/ml using a low multiplicity of infection of 0.05 pfu per cell. In a continuous bioreactor, it was shown that the uninfected insect cells were not sensitive to local shear stress values up to 2.25 N/m2 at high Reynolds numbers (1.5 x 10(4)) in sparging conditions. Uninfected insect cells can be grown at scaled-up bioreactor at high agitation and sparging rates as long as vortex formation is avoided and bubble entrapment is minimized. An efficient process scale-up to 25 l bioreactor was made using constant shear stress criteria for scale-up. The kinetics of baculovirus infection at low multiplicity of infection, either at different cell concentration or at different scales, are very reproducible, despite the different turbulence conditions present in the bioreactor milieu. The results suggest that the infection kinetics is controlled by the rate of baculovirus-cell receptor attachment and is independent of the bioreactor hydrodynamic conditions. Furthermore, the achieved specific and volumetric productivities were higher at the 25 l scale when compared to the smaller scale bioreactor. Different rates of cell lysis after infection were observed and seem to fully explain both the shift in optimal harvest time and the increase in cell specific productivity. The results emphasize the importance of integrated strategies and engineering concepts in process development at bioreactor stage with the baculovirus insect cell system.     

Damaging agitation intensities increase DNA synthesis rate and alter cell-cycle phase distributions of CHO cells

The effects of fluid-mechanical force (agitation) on the cell cycle kinetics of Chinese hamster ovary (CHO) cells cultured in suspension in 2-L bioreactors has been examined. A two-color flow cytometry method was used to determine the fraction rate of DNA synthesis. With increased agitation intensity, cell viability decreased as a result of increased cell death. However, increased agitation induced the viable cells of the culture to a higher proliferative state relative to a control culture. The fraction of viable cells of the high-agitation culture (250 rpm) in S phase was higher (up to 45%) and in G1 phase was lower (up to 50%) compared with the viable cells of the control culture (80 rpm). The DNA synthesis rate per viable S-phase cell of the high-agitation culture was confirmed by recovery experiments, which were conducted to measure the apparent specific growth rate and the cell cycle kinetics of the high-agitation culture upon reduction in the agitation rate from 250 rpm back to 80 rpm. The apparent specific growth rate of the test culture, calculated for the first 12 h of the recovery period, was greater than the apparent specific growth rate of the control culture. Furthermore, the proliferative state of the viable cells of the test culture, which had become higher relative to the control culture during the high agitation period, gradually approached the level of the control culture during recovery. Results also show that the magnitude of the agitation intensity; the culture agitated at 250 rpm attained a greater proliferative state than a parallel culture agitated at 235 rpm. The 250-rpm culture had a higher fraction of S-phase and a lower fraction of G1-phase cells than the 235-rpm culture. The DNA sunthesis rate per viable S-phase cell of the 250-rpm culture was greater than of the 235-rpm culture. (c) 1992 John Wiley & Sons, Inc.