FLUID SHEAR-STIMULATED DINOFLAGELLATE BIOLUMINESCENCE

Bioluminescence studies provide insight into the properties of water motion that are stimulatory to flow-sensitive organisms such as dinoflagellates, the most common sources of near-surface oceanic bioluminescence. Previous laboratory studies employing steady flows have characterized the luminescent response of dinoflagellates in terms of shear stress. In the present study, computational and experimental approaches were used to investigate the contributions of shear and acceleration to cells responding in a laminar converging flow field, where regions of high acceleration and shear are spatially separated. Flow-stimulated flashes by the dinoflagellates Lingulodinium polyedrum and Ceratocorys horrida were used as a near-instantaneous monitor of cell response. By combining video analysis of flash trajectories with computational methods, the location of each stimulated cell was determined and flow parameters at that location were calculated. Based on several criteria, shear stress was considered the flow parameter most stimulatory to cells. For both dinoflagellates species and for all flow rates, essentially all cells responded downstream near the wall where shear stress levels were maximal, and levels of acceleration and extensional stress were as much as two orders of magnitude less than locations away from the wall. Minimum shear stress levels at the cell positions were consistent with response thresholds based on previous studies. Bioluminescence is an excellent tool for examining how organisms respond to flow at the small temporal and spatial scales relevant to planktonic organisms.     

Variability in the bioluminescence response of the dinoflagellate Pyrocystis lunula

Light emission in dinoflagellates is induced by water motions. But although it is known that mechanical stimulations of these organisms trigger the bioluminescent response, the exact mechanism that involves some cell membrane excitations by fluid motions is not yet fully understood and is still controversial. We show in this experimental study that the accelerated shear flow, created by abrupt rotations of one or both co-axial cylinders of a Couette shearing chamber excites the light emission from cultured dinoflagellates Pyrocystis lunula. Following our first results published earlier that state that pure laminar shear does not excite the main bioluminescent response in dinoflagellates, our present experiments show that both shear and acceleration in the flow are needed to trigger the bioluminescent response. Besides, the probability to stimulate this bioluminescent response under acceleration and shear is deduced from the response curves. This response follows a Gaussian distribution that traduces a heterogeneity in individual cell thresholds for the stimulation of bioluminescence in a dinoflagellate population. All these results will have a repercussion in the possible applications of dinoflagellate bioluminescence in flow visualizations and measurements. Moreover, this study opens a new way in studying mechanically-induced stimulus thresholds at the cell level.     

Shear-stress dependence of dinoflagellate bioluminescence

Fluid flow stimulates bioluminescence in dinoflagellates. However, many aspects of the cellular mechanotransduction are incompletely known. The objective of our study was to formally test the hypothesis that flow-stimulated dinoflagellate bioluminescence is dependent on shear stress, signifying that organisms are responding to the applied fluid force. The dinoflagellate Lingulodinium polyedrum was exposed to steady shear using simple Couette flow in which fluid viscosity was manipulated to alter shear stress. At a constant shear rate, a higher shear stress due to increased viscosity increased both bioluminescence intensity and decay rate, supporting our hypothesis that bioluminescence is shear-stress dependent. Although the flow response of non-marine attached cells is known to be mediated through shear stress, our results indicate that suspended cells such as dinoflagellates also sense and respond to shear stress. Shear-stress dependence of flow-stimulated bioluminescence in dinoflagellates is consistent with mechanical stimulation due to direct predator handling in the context of predator-prey interactions.     

Determination of shear stress thresholds in toxic dinoflagellates cultured in shaken flasks: Implications in bioprocess engineering

Marine dinoflagellates are potentially important innovative sources of high-value toxins in biomedical, toxicological and chemical research programs. However, little is known about the difficulties related to dinoflagellate cultures. In this article, we demonstrate that the shear sensitivity of cells may be one of the main causes. The red-tide Protoceratium reticulatum, a producer of yessotoxins, was used to examine the effect of hydromechanical shear stress associated with intermittent fluid agitation on cell growth. Shaken flasks, widely used in biotechnological process research, were used as model bioreactors, as hydrodynamic shear stress is relatively easy to quantify in them. Intermittent turbulence regime was characterized by three key operating variables: shear stress, cycle time or shaking frequency, and fraction of time shaken per agitation cycle. The light/dark cycle was also used as another variable. Cell damage depended on the combination of the above-mentioned variables. A damage threshold was observed at an average shear stress of approximately 0.16 mN m⁻² (equivalent shear rate of 0.12 s⁻¹). Cell damage from exposure to average detrimental shear stress was also shown to be greater in the dark than in the light period. Preliminary experiments demonstrated that dinoflagellates are also much more sensitive to bubbling than the majority of common fragile microalgae. Although slight toxicity of Pluronic F-68 was observed at a concentration of 0.05% (w/v), this protective medium additive considerably reduced cell breakage. On the other hand, no cell adaptation to stronger shear stress was observed. Finally, the implications of the proposed approach for the hypothetical mass culture of dinoflagellates in bioreactors were also thoroughly assessed.     

Bubble stimulation efficiency of dinoflagellate bioluminescence

Dinoflagellate bioluminescence , a common source of bioluminescence in coastal waters , is stimulated by flow agitation . Although bubbles are anecdotally known to be stimulatory , the process has never been experimentally investigated . This study quantified the flash response of the bioluminescent dinoflagellate Lingulodinium polyedrum to stimulation by bubbles rising through still seawater . Cells were stimulated by isolated bubbles of 0 . 3–3 mm radii rising at their terminal velocity , and also by bubble clouds containing bubbles of 0 . 06–10 mm radii for different air flow rates . Stimulation efficiency , the proportion of cells producing a flash within the volume of water swept out by a rising bubble , decreased with decreasing bubble radius for radii less than approximately 1 mm . Bubbles smaller than a critical radius in the range 0 . 275–0 . 325 mm did not stimulate a flash response . The fraction of cells stimulated by bubble clouds was proportional to the volume of air in the bubble cloud , with lower stimulation levels observed for clouds with smaller bubbles . An empirical model for bubble cloud stimulation based on the isolated bubble observations successfully reproduced the observed stimulation by bubble clouds for low air flow rates . High air flow rates stimulated more light emission than expected , presumably because of additional fluid shear stress associated with collective buoyancy effects generated by the high air fraction bubble cloud . These results are relevant to bioluminescence stimulation by bubbles in two‐phase flows , such as in ship wakes , breaking waves , and sparged bioreactors . Copyright © 2015 John Wiley & Sons, Ltd.     

Hydrodynamic effects on cells in agitated tissue culture reactors

Tissue cells are known to be sensitive to mechanical stresses imposed on them by agitation in bioreactors. The amount of agitation provided in a microcarrier or suspension bioreactor should be only enough to provide an effective homogeneity. Three distinct flow regions can be identified in the reactor: bulk turbulent flow, bulk laminar flow, and boundary-layer flows. Possible mechanisms of cell damage are examined by analyzing the motion of microcarriers or free cells relative to the surrounding fluid, to each other, and to moving or stationary solid surfaces. The primary mechanisms of cell damage appear to result from (a) direct interaction between microcarriers and turbulent eddies, (b) collisions between microcarriers in turbulent flow, and (c) collisions against the impeller or other stationary surfaces. If the smallest eddies of turbulent flow are of the same size as the microcarrier beads, they may cause high shear stresses on the cells. Eddies the size of the average interbead spacing may cause bead-bead collisions which damage cells. The severity of the collisions increases when the eddies are also of the same size as the beads. Bead size and the interbead distance are virtually equal in typical microcarrier suspensions. Impeller collisions occur when the beads cannot avoid the impeller leading edge as it advances through the liquid. The implications of the results of this analysis on the design and operation of tissue culture bioreactors are also discussed.     

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.     

Integrating a 250 mL-spinner flask with other stirred bench-scale cell culture devices: a mass transfer perspective

The bioprocess development cycle is a complex task that requires a complete understanding of the engineering of the process (e.g., mass transfer, mixing, CO(2) removal, process monitoring, and control) and its affect on cell biology and product quality. Despite their widespread use in bioprocess development, spinner flasks generally lack engineering characterization of critical physical parameters such as k(L)a, P/V, or mixing time. In this study, mass transfer characterization of a 250-mL spinner flask using optical patch-based sensors is presented. The results quantitatively show the effect of the impeller type, liquid filling volume, and agitation speed on the volumetric mass transfer coefficient (k(L)a) in a 250-mL spinner flask, and how they can be manipulated to match mass transfer capability at large culture devices. Thus, process understanding in spinner flasks can be improved, and these devices can be seamlessly integrated in a rational scale-up strategy from cell thawing to bench-scale bioreactors (and beyond) in biomanufacturing.     

Bioluminescence of the dinoflagellate Pyrocystis noctiluca induced by laminar and turbulent Couette flow

The excitation of bioluminescence by different flow regimes generated within a Couette chamber was examined using the dinoflagellates Pyrocystis noctiluca. Cultured cells of P. noctiluca were gently transferred into a cylindrical Couette chamber in a dark room. In initial experiments, the velocity of the outer Couette cylinder was then gradually increased. The bioluminescence emissions in response to stationary-laminar and turbulent flows were quantified using a photomultiplier tube. Video images were also recorded in order to identify the location of bioluminescence emissions within the Couette chamber. Reflective flake flow visualizations were used to correlate these locations to the flow regimes in those parts of the chamber. These experiments clearly demonstrated that the strongest bioluminescence emissions were only triggered by the onset of turbulence at high rotation speeds. Below the turbulence threshold, much lower bioluminescence emissions were detected and appeared to be in response to a nonhomogeneity in the stationary-laminar flow (end cap effects and Ekman cells). In a second set of experiments, the excitation of bioluminescence in response to acceleration was studied by abrupt starts of the rotating Couette cylinder. These experiments also triggered massive bioluminescence emissions. We conclude that pure laminar-stationary, homogenous shear flow excites very little bioluminescence in P. noctiluca. The bulk of bioluminescence emissions primarily occurred under nonhomogenous or nonstationary flow conditions, where the cells experience velocity changes as they move through the flow. These findings are discussed in relation to the theory that bioluminescence in dinoflagellates is an antipredation mechanism.     

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.     

TEMPERATURE INDUCED PHOTOINHIBITION IN OUTDOOR CULTURES OF MONODUS SUBTERRANEUS

Many marine planktonic dinoflagellates emit flashes of light in response to either laminar or turbulent flows as well as direct mechanical stimulation. The production of a flash of light is known to be mediated by a proton-mediated action potential across the vacuolar membrane; the mechanotransduction process initiating this action potential is unknown. Here we report on an investigation into the role of Ca⁺² in the mechanotransduction process regulating bioluminescence in the red tide dinoflagellate Lingulodinium polyedrum. Calcium ionophores and low concentrations of the membrane-disrupting agent digitonin stimulated bioluminescence only when calcium was present in the media or added with the agent, indicating that the flash-triggering vacuolar action potential is specifically stimulated by a calcium influx. A variety of known calcium channel blockers or antagonists inhibited mechanically stimulated bioluminescence but did not affect cellular bioluminescent capacity. In many cases the inhibitory affect occurred after only a brief exposure. In addition, gadolinium (Gd⁺³), a blocker of many stretch-activated ion channels, caused potent inhibition of mechanically stimulated bioluminescence. The order of potency of the transition metals tested was La⁺³ > Gd⁺³ > Co⁺² > Mn⁺² > Ni⁺², similar to their potency as blockers of known calcium channels. Experiments with a quantified shear flow demonstrated that flow-stimulated bioluminescence depended on the level of extracellular calcium. Future work will elucidate the signaling pathway involving calcium-mediated flow-stimulated mechanotransduction. Our goal is to use bioluminescence as a proxy for the initial cellular mechanotransduction events triggered by fluid flow.     

Physical mechanisms of cell damage in microcarrier cell culture bioreactors

The negative effects of excessive agitation on tissue cells in microcarrier culture have often been ascribed to "shear." Analysis of the fluid mechanics occurring suggests that there are actually three potential damage mechanisms: collisions of a cell-covered microcarrier with other beads, collisions with parts of the reactor (primarily the impeller), and interaction with turbulent eddies the size of the microcarrier beads. Review of the available quantitative information on agitation effects in cell cultures does not establish which mechanism is predominant; the range of experimental variables reported emphasizes power input over the other reactor and impeller parameters. The bead-bead collision model is tentatively supported by the available data, but the other mechanisms may still be significant in some systems. The formation of bead aggregates by cellular bridging provides a parallel means of damaging cells. Breaking of these bridges by any of the three means identified earlier can cause cell destruction and/or the net transfer of cells to formerly bare beads. High concentrations of bridges are favored by lower agitation rates, presumably because the bridges are not as quickly destroyed after formation.     

Effect of agitation rate and impeller design on oxygen transfer coefficients in small bioreactors using surface aeration

The effects of agitation rate and impeller type on the combined oxygen mass-transfer coefficient (kL a) in four different benchtop bioreactors have been examined. Surface oxygenation of a cell culture medium supplemented with fetal bovine serum and distilled deionized water has been studied by passing air through the bioreactor headspace at approximately one headspace volume per minute. A new ribbon-type impeller design using strips of Teflon has been shown to be superior to conventional impeller designs for oxygen transfer.     

THE ROLE OF CALCIUM IN FLOW‐STIMULATED BIOLUMINESCENCE OF THE RED TIDE DINOFLAGELLATE LINGULODINIUM POLYEDRUM

Many marine planktonic dinoflagellates emit flashes of light in response to either laminar or turbulent flows as well as direct mechanical stimulation. The production of a flash of light is known to be mediated by a proton‐mediated action potential across the vacuolar membrane; the mechanotransduction process initiating this action potential is unknown. Here we report on an investigation into the role of Ca⁺² in the mechanotransduction process regulating bioluminescence in the red tide dinoflagellate Lingulodinium polyedrum. Calcium ionophores and low concentrations of the membrane‐disrupting agent digitonin stimulated bioluminescence only when calcium was present in the media or added with the agent, indicating that the flash‐triggering vacuolar action potential is specifically stimulated by a calcium influx. A variety of known calcium channel blockers or antagonists inhibited mechanically stimulated bioluminescence but did not affect cellular bioluminescent capacity. In many cases the inhibitory affect occurred after only a brief exposure. In addition, gadolinium (Gd⁺³), a blocker of many stretch‐activated ion channels, caused potent inhibition of mechanically stimulated bioluminescence. The order of potency of the transition metals tested was La⁺³ > Gd⁺³ > Co⁺² > Mn⁺² > Ni⁺², similar to their potency as blockers of known calcium channels. Experiments with a quantified shear flow demonstrated that flow‐stimulated bioluminescence depended on the level of extracellular calcium. Future work will elucidate the signaling pathway involving calcium‐mediated flow‐stimulated mechanotransduction. Our goal is to use bioluminescence as a proxy for the initial cellular mechanotransduction events triggered by fluid flow.     

Periodic-peristole agitation for process enhancement of butanol fermentation

Background

Mass transfer plays an important role in determining the efficiency of the biofuel conversion. However, adverse effect of shear stress from traditional agitation inhibits the cell growth and production of biofuels. How to enhance the mass transfer with less adverse effect is considered as one of the important bioengineering issues.

Results

In this study, a novel agitation type, named periodic-peristole was applied to butanol fermentation with Clostridium acetobutylicum ATCC 824. Meanwhile, the enhancement mechanism was studied. Initially, the fermentation performance of periodic-peristole agitation was compared with the traditional Rushton impeller and stationary cultivation. Result showed that the biomass, butanol and total solvent in periodic-peristole group (PPG) was enhanced to 1.92-, 2.06-, and 2.4-fold of those in the traditional Rushton impeller group (TIG), as well as 1.64-, 1.19- and 1.41-fold of those in the stationary group (SG). Subsequently, to get in-depth insight into enhancement mechanism, hydromechanics analysis and metabolic flux analysis (MFA) were carried out. The periodic-peristole agitation exhibits significant difference on velocity distribution, shear force, and mixing efficiency from the traditional Rushton impeller agitation. And the shear force in PPG is only 74 % of that in TIG. According to MFA result, fructose 6-phosphate, pyruvate, acetyl-CoA, oxaloacetate and α-ketoglutarate were determined the key nodes of cells in response to hydrodynamic mechanical stress. Based on such key information, rational enhancement strategies were proposed and butanol production was further improved.

Conclusion

The agitation associated with three issues which resulted in significant changes in cell metabolic behaviors: first, a rebalanced redox status; second, the energy (ATP) acquirement and consumption; third, the tolerance mechanism of the cell for survival of solvent. Periodic-peristole agitation provides an answer to address a long-standing problem of biofuel engineering. Key information derived from current study deepens the understanding of agitation, which can guide the designment of new bioreactors and development of enhancement strategies for biofuel refinery.

     

Growth of Trichoderma reesei RUT C-30 in stirred tank and reciprocating plate bioreactors

A series of fed-batch experiments at different agitation speeds were performed using the industrially important strain Trichoderma reesei RUT C-30 in two different bioreactors to understand the close relationship that exists between the shear field within a bioreactor, the morphology of the microorganism, the rheology of cultivation broth, and the process performance. The two bioreactors, stirred tank bioreactor (STB) and reciprocating plate bioreactor (RPB), are characterized by a significantly different shear field to which microorganisms are exposed. Highest biomass concentration (ca. 15 g l⁻¹) was obtained at higher agitation rates in both bioreactors due to better oxygen supply. However, better filter paper activities per mg of protein were obtained at lower agitation in both bioreactors. In both bioreactors, young and healthier fungi in the batch phase were not affected by shear even at higher agitation rates. However, during the fed-batch phase, higher degree of fragmentation of clump morphology at high agitation intensity was confirmed by image analysis. Also, the rheological analysis showed an increase in apparent viscosity during the batch phase and early fed-batch phase due to the increase in the biomass concentration. During the late stages of cultivation, the apparent viscosity decreased due to cell lysis and spore formation.     

Biological responses of hybridoma cells to hydrodynamic shear in an agitated bioreactor.

Effects of long-term hydrodynamic shear on hybridoma cells were investigated in a 250-ml continuous stirred-tank reactor (CSTR). Cells grown at steady state were subjected to step changes in agitation rates. Cell viability, glucose consumption, and monoclonal antibody (MAb) production were determined at high agitation rates and compared with the control (100 rev min-1). Impeller tip speeds higher than 40 cm s-1 caused a significant drop in cell concentration and respiration activity, and increased lactate dehydrogenase (LDH) release to the culture medium. Also, high agitation speeds caused a decrease in MAb concentration and an increase in specific glucose consumption rate. The effects of dilution rate and serum concentration on the sensitivity of hybridoma cells to hydrodynamic shear were determined. Serum was found to protect the cells against shear damage and had a significant positive effect on hybridoma growth and MAb production. Shear damage on cells in CSTR was approximated to first-order kinetics. The death rate constant increased sharply at impeller tip speeds above 40 cm s-1.     

Improvement of foam breaking and oxygen-transfer performance in a stirred-tank fermenter

This study examined a stirred-tank fermenter (STF) containing low-viscosity foaming liquids with an agitation impeller and foam-breaking impeller mounted on the same shaft. Results showed that the performance of the foam-breaking impeller can be improved by changing a conventional six-blade turbine impeller into a rod impeller as the agitation impeller. The volumetric oxygen-transfer coefficient, k _L a, in the mechanical foam-control method (MFM) using a six-blade vaned disk as the foam-breaking impeller in the STF with the rod impeller was approximately five times greater than that of the chemical foam-control method (CFM) adding an anti-foaming agent in the STF with the six-blade turbine impeller. Application of the present method to the cultivation of Saccharomyces cerevisiae K-7 demonstrated that the cultivation time up to the maximum cell concentration was remarkably shorter than that achieved using a conventional CFM.     

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.     

Large-scale production of monoclonal antibodies in suspension culture

Monoclonal antibodies are being manufactured for clinical trials in suspension culture at the 1300-L scale. Suspension culture offers some advantages relative to high-density mammalian cell culture methods; in particular, the ability to closely monitor the behavior of cells in a homogeneous environment. Computer control and on-line mass spectrography of exit gases provide instantaneous information about the culture metabolic activity. Air sparging and agitation by marine impeller provide aeration sufficient to maintain a constant dissolved oxygen tension at cell concentrations up to 5.0 x 10(6) cells/mL without causing apparent cell damage.