Enhancement of the attachment on microcarriers and tPA production by fibroblast cells in a serum-free medium by the addition of the extracts ofCentella asiatica

The addition of ethanol extracts ofCentella asiatica showed a remarkable enhancement of fibroblast cells attachment to Cytodex beads in serum-free (SF) medium. It also improves tPA production in both batch and perfusion cultivations. The optimal concentration for SF medium was determined as 2 ppm of the extracts when using Cytodex III. In batch cultivation a high specific tPA production rate was obtained, compared to that from 5% FBS containing medium. However, a fast specific growth rate was observed in 5% FBS medium. In perfusion cultivation a reasonably good cell density and tPA production was achieved at a perfusion rate of 2.4×10⁶ (viable cell/ml) and 0.65 (g/ml), respectively at 22 ml/min.     

High cell density perfusion cultures of anchorage-dependent Vero cells in a depth filter perfusion system

A depth filter perfusion system (DFPS) with polypropylene fibers had been demonstrated to support high density cultures of anchorage-independent hybridoma cells. The DFPS provides advantages of high surface-to-volume ratio of 450–600 cm²/cm³, low cost set-up, easy operation and scale-up. To test the feasibility of using DFPS for high density cultures of anchorage-dependent cells, Vero cells were cultivated in the DFPS. Gelatin coating on polypropylene fibers in the DFPS was necessary to promote cell attachment and growth. Dissolved oxygen (DO) concentrations could be controlled by sparging air into the reservoir vessel through a filter sparger. When DO concentration was controlled above 40% of air saturation in the DFPS with 40 m pore size, the maximum cell concentration as estimated on specific lactate production rate, was 3.81×10⁷ cells/ml of the total reactor volume. This viable cell concentration is approximately 18 times higher than that obtained in a T-flask batch culture. Taken together, the results obtained here showed the potential of DFPS for high-density cultures of anchorage-dependent cells.     

An investigation of cell density effects on hybridoma metabolism in a homogeneous perfusion reactor

In this work, metabolite and antibody production kinetics of hybridoma cultures were investigated as a function of cell density and growth rate in a homogeneous perfusion reactor. Hydrophilized hollow fiber polypropylene membranes with a pore size of 0.2 m were used for medium perfusion. Oxygen was supplied to the cells through thin walled silicone tubing. The mouse-mouse hybridoma cells were grown in three identical bioreactors at perfusion rates of 1.1, 2.0, and 3.2/day for a period of eight days during which the viable cell concentrations reached stable values of 2.6×10⁶, 3.5×10⁶, and 5.2×10⁶ cells/ml, respectively. Total cell densities reached values ranging from 8×10⁶ to 1×10⁶ cells/ml. Specific substrate consumption and product formation rates responded differently to changes in cell density and apparent specific growth rate, which were not varied independently. Using multiple regression analysis, the specific glucose consumption rate was found to vary with viable cell density while the specific glutamine uptake and lactate production rates varied with both viable cell density and apparent specific growth rate. These results suggest that cell density dictates the rate of glucose consumption while the cell growth rate influences how glucose is metabolized, i.e., through glycolysis or the TCA cycle. The specific antibody production rate was found to be a strong function of cell density, increasing as cell density increased, but was essentially independent of the specific growth rate for the cell line under study.List of Symbols MAb monoclonal antibody - X _v viable cell density (cells/ml) - X _d nonviable cell density (cells/ml) - specific growth rate (1/day) - k _d specific death rate (1/day) - D dilution rate (1/day) - S _f substrate concentration in feed (g/l or mM) - S substrate concentration (g/l or mM) - P _f product concentration in feed (g/l or g/ml) - P product concentration (g/l or ug/ml) - q _s specific consumption rate of substrate (g/hr/cell or mmol/hr/cell) - q _p specific production rate of product (g/hr/cell) - q _MAb specific production rate of monoclonal antibody (g/hr/cell) This work was supported in part by a grant for the National Science Foundation (BCS-9157851) and by matching funds from Merck and Monsanto. We sincerely thank Mr. Roland Buchele of Akzo Inc. (Germany) for donation of the polypropylene membranes, Dr. Michael Fanger (Dartmouth Medical School) for the hybridoma cell line, Dr. Sadettin Ozturk (Verax Corp., Lebanon, NH) for technical discussions regarding reactor design, and Dr. Derrick Rollins (Iowa State University) for advice on statistical methods.     

Quantification of citrate lyase by enzyme-linked immunosorbent assay for determining the population of Lactococcus lactis subsp. Lactis biovar diacetylactis in pure and mixed cultures

Citrate lyase production by Lactococcus lactis subsp. lactis biovar diacetylactis DRC2 was quantified by an enzyme-linked immunosorbent assay (ELISA). The citrate lyase reached a concentration equivalent to 41 ± 4 g/ml purified citrate lyase in pure culture. When the strain DRC2, grown in mixed culture with L. lactis subsp. cremoris AM2, represented around 70% (DC culture) or 30% (CD culture) of the total initial population, the level of citrate lyase decreased to 21 ± 7 g/ml and 4.5 ± 1.5 g/ml respectively. The maximum bacterial concentration of strain DRC2 in pure culture reached 2.6 × 10⁹ cfu/ml and decreased to 1.5 (± 0.2) × 10⁹ cfu/ml and 0.5 (± 0.3) × 10⁹ cfu/ml in DC and CD mixed cultures respectively. In mixed cultures, the proportion of the strain DRC2 was 8.5 ± 5.0% lower at the end of the fermentation than immediately after inoculation, thus showing that this strain was clearly inhibited. However, the maximum rate of citrate consumption was the same during pure DRC2 culture and CD mixed culture (2.5 ± 0.3 mmol/h) and slightly highre in DC culture (3.07 mmol/h). The maximum rate of acidification was 0.37 ± 0.04 pH unit/h regardless of the culture. A good correlation was obtained between the population of the strain DRC2 and the citrate lyase concentration determined by ELISA but no relationship was found between citrate consumption and citrate lyase synthesis. Therefore an ELISA test of this kind can be used to monitor the growth of L. lactis subsp. lactis biovar diacetylactis in mixed cultures.     

Conversion of cellulose into fungal cell mass

Summary Chaetomium cellulolyticum (ATCC 32319) was cultivated on glucose, Avicel and/or Sigmacell in a 20-1 stirred tank batch reactor. The substrate (cellulose) concentration, the cell mass concentration (through protein and/or nitrogen content), reducing sugar concentration, the enzyme activity, the alkali consumption rate, the dissolved O₂ and CO₂ concentrations in the outlet gas were measured. The specific growth rate, the substrate yield coefficient, cell productivity, the oxygen consumption rate, the CO₂ production rate and the volumetric mass transfer coefficient were determined. At the beginning of the growth phase the oxygen utilization rate exhibits a sharp maximum. This maximum could be used to start process control. Because of the long lag phase periodic batch operation is recommended.Symbols CP cell protein concentration (g l^–1) - FPA FP enzyme activity (IU l^–1) - GP dissolved protein concentration (g l^–1) - IU international unit of enzyme activity - k_La volumetric mass tranfer coefficient (h^–1) - LG alkali (1 n NaOH) consumption (ml) - LGX specific alkali consumption rate per cell mass (ml g^–1 h^–1) - P cell mass productivity (g l^–1 h^–1) - specific oxygen consumption rate per cell mass (g g^–1 h^–1) - Q aeration rate (volumetric gas flow rate per volume of medium, vvm) (min^–1) - N impeller speed (revolution per minute, rpm) (min^–1) - S substrate concentration (g l^–1) - S⁰ S at t_F=0 (g l^–1) - S₀ S in feed (g l^–1) - SR acid consumption (ml) - TDW total dry weight (g l^–1) - T temperature (° C) - t_F cultivation time (h) - U substrate conversion - X cell mass concentration (g l^–1) - Y_X/S vield coefficient - specific growth rate (h^–1) - _m maximum specific growth rate (h^–1)     

Metabolic rates during sporulation of Saccharomyces cerevisiae on acetate

We have quantified yeast carbon and oxygen consumption fluxes and estimated anabolic fluxes through glyoxylate and gluconeogenic pathways under various conditions of sporulation on acetate. The percentage of sporulation reached a maximum of 55% to 60% after 48 h in sporulation medium, for cells harvested from logarithmic growth in acetate minimal medium. When cells were harvested in the stationary phase of growth before transfer to sporulation medium, the maximum percentage of sporulation decreased to 40% along with the occurrence of meiosis as could be judged by counting of bi- and tetra-nucleated cells. In both experiments, the rates of acetate and oxygen consumption decreased as a function of time when exposed to sporulation medium. Apparently, the decrease of metabolic rates was not due to alkalinization. By systematically varying the cell concentration in sporulation medium from 1.4×10⁷ to 20×10⁷ cell ml^-1, the percentage of sporulating cells was found to decrease in parallel with the rate of acetate consumption. When the sporulation efficiency attained under the different experimental conditions was plotted as a function of the rate of acetate consumption, a linear correlation was found. Anabolic fluxes estimation revealed a decrease of the rate through gluconeogenic and glyoxylate pathways occurring during sporulation progression. The pattern of metabolic fluxes progressively evolved toward a predominance of more oxidative catabolic fluxes than those exhibited under growth conditions. The results obtained are discussed in terms of a characteristic pattern of metabolic fluxes and energetics, associated to the development of yeast sporulation.Abbreviations DAPI 4,6-diamidino-2-phenylindole - dw dry weight - OD₅₄₀ optical density at 540 nm - SEM standard error of the mean - RQ respiratory quotient     

Production of tPA in recombinant CHO cells under oxygen-limited conditions

Animal cell bioreactors are often limited by the oxygen supply. The reduction in oxygen consumption per cell that occurs under hypoxic conditions may be exploited as a method for increasing reactor capacity if additional glucose is provided to offset increased glycolytic activity. The effects of oxygen deprivation on recombinant tPA (tissue-type plasminogen activator) production were investigated using midexponential and slowly growing CHO cells. The specific oxygen consumption rate can be reduced by at least 50% (mild hypoxic conditions) without affecting the cell growth rate, maximum cell concentration, tPA production rate, or tPA quality (as characterized by the tPA-specific activity and SDS-PAGE analysis). This suggests that mild-hypoxic conditions (with sufficient glucose) can be used to double the cell concentration and volumetric tPA production rate (at a constant volumetric oxygen supply rate) without sacrificing product quality. However, anoxic conditions should be avoided. When slowly growing cultures were exposed to anoxia, the tPA production rate decreased by 80% without affecting tPA quality. However, when midexponential cultures were exposed to anoxia, the drop in tPA production was accompanied by a decrease in tPA quality that ranged from a 40% decrease in tPA specific activity to extensive tPA degradation. (c) 1993 John Wiley & Sons, Inc.     

Below-halocline oxygen consumption in the Kattegat

Sediment and seston oxygen consumption rates below the sharp halocline in the south-eastern part of the shallow Kattegat were measured and compared to calculated rates of carbon addition through the halocline. The mean rate of decrease in deep-water oxygen concentrations between March and September 1988 was 1.0 ml O₂ M^–3 h^–1. Measurements of benthic oxygen uptake using laboratory-incubated sediment cores from depths 30 m gave a mean value of 7.8 ml O₂ m^–2 h^–1. Below-halocline water (from 20 m, 30 m and 1 m above bottom) incubated in bottles showed oxygen consumption rates varying from 0.5 ml O₂ m ^–3 h^–1 in March to 2.8 ml O₂ M^–3 h^-1 in late August. The sum of benthic and deep-water oxygen consumption was equivalent to a mean oxygen decrease rate of 1.7 ml O₂ m^–3 h^–1 below the halocline. Of the total oxygen consumption below the halocline 65% was due to oxygen up-take in the water and 35% was due to benthic oxygen consumption. The sum of oxygen consumption measured in sediment cores and in bottles corresponds to a carbon utilisation of 80.1 g C m^–2 (respiratory quotient (RQ), assumed 1.0 and 1.4 for water and sediment, respectively), while the decrease in deep-water oxygen concentration was equivalent to 43.0 g C m^–2 (RQ assumed = 1.0). Using published values for the external N loading (including deep-water supply), ¹⁵NO₃-uptake, ¹⁴CO₂-uptake in combination with % ¹⁵NO₃-uptake of total ¹⁵N-uptake (nitrate, ammonia and urea) and a Redfield C/N ratio of 6.6, rates of carbon addition (new or export production) through the halocline were calculated to 31.9, 46.7 and 36.3 g C m^–2, respectively, with a mean value of 38.3 g C m^–2 for the 8 month period March–September. This is somewhat less than the value (50.5 g C m^–2) calculated from a published empirical relationship between total and export production. The fact that the calculated carbon addition through the halocline was appreciably less than the carbon equivalent of the measured below-halocline respiration may be an effect of sediment focusing (horizontal transport of sedimenting material to deeper areas), since the bottom area below the halocline is much smaller than the total area of the Kattegat. A lower observed decrease in the oxygen concentration below the halocline compared to the sum of measured sediment and deep-water oxygen consumption on the other hand indicates oxygen supply to below-halocline waters through advection and/or vertical entrainment.     

The economic production of anti-microbial factor from human promyelocytes in low serum containing medium under chemostat cultivation

It proves that a purifed Anti-Microbial Factor (AMF) from human promyelocytes has strong activity on Gram(–) and Gram(+) bacteria, showing 0.5 (g/ml) of Minimal Bacterical Concentration (MBC) on bothE. coli andS. aureus. For mass production of AMF, chemostat cultivation is recommended to accumulate cells out of the reactor since it is an intracellular protein and its system requires only 1% serum in the medium. Its production process proves to be closely growth-related. 1.7×10^–8 (g/viable cell/day) of maximum specific AMF production rate is estimated at 0.026 h^–1 of dilution rate, maintaining 6×10⁶ (viable cell/ml). Ca. 300 (mg/ml) of crude AMF can be obtained for 50 days of continuous cultivation under optimal conditions. The cell growth reaches relatively fast steady state.     

Benthic oxygen flux in the highly productive subarctic Lake Myvatn, Iceland: In situ benthic flux chamber study

In situ paired light and dark-stirred benthic flux chambers were used to estimate dissolved oxygen flux across the sediment–water interface in Lake Mývatn, Iceland. Three sampling stations were selected, each station reflecting a specific sedimentary environment, benthic communities, and water depth. During this study the phytoplankton density was low. Spatial and seasonal variations of bottom DO concentration and DO flux have been observed during this study. The oxygen consumption rate at all study sites had a mean of –89 (±44) mmol m^–2 d^–1 while the oxygen production rate due to benthic algae had a mean of 131 (±103) mmol m^–2 d^–1. There was a strong correlation (r=0.91) between oxygen consumption rate and temperature. This was presumably because of the temperature influence on rates of microbial and macrobenthic processes. The mean benthic primary production rate at all study sites was 1216 (±957) mg C m^–2 d^–1 between June 2000 and February 2001. Annual gross benthic primary production was estimated from the gross mean daily benthic DO production (P) and Redfield's C:O₂ ratio of 106:138 to be 420 g C m^–2 y^–1 at station HO, 250 g C m^–2 y^–1 at B2 and 340 g C m^–2 y^–1 at station 95. Thus, the mean gross benthic primary production was estimated as 1151 mg C m^–2 d^–1 at station HO, 685 mg C m^–2 d^–1 at station B2, and 932 mg C m^–2 d^–1 at station 95.     

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.     

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.     

The effect of dissolved oxygen tension and the utility of oxygen uptake rate in insect cell culture

Dissolved oxygen tension and oxygen uptake rate are critical parameters in animal cell culture. However, only scarce information of such variables is available for insect cell culture. In this work, the effect of dissolved oxygen tension (DOT) and the utility of on-line oxygen uptake rate (OUR) measurements in monitoring Spodoptera frugiperda (Sf9) cultures were determined. Sf9 cells were grown at constant dissolved oxygen tensions in the range of 0 to 30%. Sf9 metabolism was affected only at DOT below 10%, as no significant differences on specific growth rate, cell concentration, amino acid consumption/production nor carbohydrates consumption rates were found at DOT between 10 and 30%. The specific growth rate and specific oxygen uptake rate followed typical Monod kinetics with respect to DOT. The calculated _max and max were 0.033 h^-1 and 3.82×10^-10 mole cell^-1h^-1, respectively, and the corresponding saturation constants were 1.91 and 1.57%, respectively. In all aerated cultures, lactate was consumed only after glucose and fructose had been exhausted. The yield of lactate increased with decreasing DOT. It is proposed, that an apparent DOT in non-instrumented cultures can be inferred from the lactate yield of bioreactors as a function of DOT. Such a concept, can be a useful and important tool for determining the average dissolved oxygen tension in non-instrumented cultures. It was shown that the dynamic behavior of OUR can be correlated with monosaccharide (fructose and glucose) depletion and viable cell concentration. Accordingly, OUR can have two important applications in insect cell culture: for on-line estimation of viable cells, and as a possible feed-back control variable in automatic strategies of nutrient addition.Abbreviations DOT Dissolved oxygen tension - OUR Oxygen uptake rate - specific oxygen uptake rate - specific growth rate - X_v viable cell concentration - C_L, C^*, and oxygen concentrations in liquid phase, in equilibrium with gas phase, and medium molar concentration, respectively - H Henry's constant - K_La volumetric oxygen transfer coefficient - P_T total pressure - oxygen partial pressure - oxygen molar fraction - i discrete element     

The optimization of serum-free medium for the production of the scu-PA by the addition of algal extracts

The addition of 2.8 g/ml algal extracts enhanced both scu-PA production and cell growth in a serum-free medium, compared to a conventional serum-free medium for the cultivation of recombinant CHO cells. The growth rate and scu-PA production were relatively lower in the serum-free medium than 5% serum containing medium: however, specific scu-PA production rate was higher in the serum-free medium due to the long-term period of cultivation (3.66×10^–4 vs. 2.48×10^–4 IU/cell/day). Overall scu-PA production rate was also greater in an enforced serum-free medium as 25,000 IU/day over 50 d of perfusion cultivation. The conversion ratio of scu-PA to tcu-PA was greatly reduced in the serum-free medium during perfusion cultivation (10% compared to 20% conversion in a serum containing medium).     

The effect of specific growth rates on the recovery of amino acids

Three specific growth rates, 0.23, 0.45 and 0.51 h^–1, were used to cultivate Corynebacterium glutamicum in a pH-auxostat. The specific formation rates of most amino acids increased by raising the specific growth rates. The highest specific growth rate, 0.51 h^–1, favors the production of LEU; whereas the highest production yield for ALA and GLU were at = 0.23 h^–1. A correlation among specific growth rates, glucose consumption rate, and production yields of amino acids was obtained.     

Improving the dynamic response of a mediator-less microbial fuel cell as a biochemical oxygen demand (BOD) sensor

The dynamic behavior of a mediator-less, microbial fuel cell (MFC) was studied as a continuous biochemical oxygen demand (BOD) sensor. The response time and the sensitivity were analyzed through the step-change testing of the fuel concentration. The MFC of 25 ml had the shortest response time of 36± 2 min at the fuel-feeding rate of 0.53 ml min^–1 and the resistance of 10 A smaller MFC of 5 ml had a response time of 5± 1 min.     

High density culture of the freshwater rotifer,Brachionus calyciflorus

The freshwater rotifer, Brachionus calyciflorus is one of the live food organisms used for the mass production of larval fish. In this study possibility of obtaining high density cultures of the freshwater rotifer B. calyciflorus were investigated. The two culture systems used differed in their air and dissolved oxygen supplies using three temperatures in each case: 24, 28 and 32 °C. Rotifers were batch-cultured using 5 l-vessels and fed with the freshwater Chlorella. The growth rate of rotifers significantly increased with an increase in temperature. The maximum density of the rotifers with air-supply at 24 °C, 6500 ind. ml^–1, was significantly lower than those cultured at 28 and 32 °C, i.e. 8600 and 8100 ind. ml^–1, respectively. Dissolved oxygen levels decreased with time and ranged from 0.8 to 1.4 mg l^–1 when the density of freshwater rotifer was the highest at each temperature. The highest density (19200 ind. ml^–1) of freshwater rotifer was obtained in cultures with a supply of oxygen at 28 °C. Densities of 13500 and 17200 ind. ml^–1 were found at 24 and 32 °C, respectively. Levels of NH₃-N increased with time and a dramatic increase of NH₃-N was observed at high temperatures. Levels of NH₃-N at 24, 28 and 32 °C were 13.2, 18.5 and 24.5 mg l^–1, respectively. These levels coincided with the highest rotifer density at each of the three temperatures. When rotifers were cultured with an oxygen-supply and pH was adjusted to 7, the maximum density of rotifer reached 33500 ind. ml^–1 at 32 °C . These results suggested that high density culture of freshwater rotifer, B. calyciflorus could be achieved under optimal conditions with DO value of exceeding 5 mg l^–1 and NH₃-N values of lower than 12.0 mg l^–1.     

Observations consistent with autocrine stimulation of hybridoma cell growth and implications for large-scale antibody production

Existence of autocrine growth factors (aGFs) may influence the serum requirement for growth of hybridoma cells and thus significantly influence process economics. For the murine hybridoma cell line S3H5/2bA2, critical inoculum density (cID) and serum requirement for growth were inversely related for cultivation in both T flasks and spinner flasks. In spinner flasks, an inoculum density of 10⁶ cells/ml was necessary for the cells to grow in RPMI 1640 medium without serum supplement, and an inoculum density of 10³ cell/ml was necessary in RPMI 1640 medium with 10% serum. In T flasks, where the local cell density is higher than in spinner flasks, an inoculum density of 10⁶ cells/ml was necessary for the cells to grow in RPMI 1640 medium without serum supplement, and an inoculum density of 1 cell/ml was also necessary in RPMI 1640 medium with 10% serum. Further, immobilized cells at high local cell density could grow under conditions where cells in T flasks at corresponding overall cell density could not grow. The cells at high inoculum density were less sensitive to shear induced by mechanical agitation than the cells at low inoculum density. Taken together these observations support the existence of secreted aGF(s) by the hybridoma cell line used. Since the specific MAb production rate was independent of cultivation method and inoculum density, the existence of autocrine growth factors would suggest that the use of immobilized cells should improve the economics of MAb production.     

Physiological effects of the presence and absence of gas vacuoles in the blue-green alga,Microcystis aeruginosa Kuetz. emend. Elenkin

Physiological evidence was obtained for a light shielding role for gas vacuoles inMicrocystis aeruginosa Kuetz. emend. Elenkin, by comparing photosynthetic oxygen evolution, growth behaviour and pigment composition of cells with intact or collapsed gas vacuoles. The oxygen evolution rates were strongly dependent on cell concentration, a maximum rate for cells with intact gas vacuoles occurring at about 1.4×10⁹ cells/ml and for cells with collapsed gas vacuoles at about 2.5×10⁹ cells/ml. By using light saturation curves for oxygen evolution, it was estimated that at low light intensities up to 30% of the photosynthetically useable light was shielded at a cell concentration of 6×10⁸ cells/ml. Collapsing the gas vacuoles twice daily did not alter the initial growth rate of the cultures, but enabled them to reach a higher final cell density. Collapsing of gas vacuoles during growth for about four generations resulted in a lower level of all acetone soluble pigments with a greater relative reduction in carotenoids than in chlorophyll a. Collapse of the gas vacuoles does not alter the cell volume. Various optical interactions which could account for light shielding are discussed.     

The effect of O2 and pressure on thiosulfate oxidation by Thiomicrospira thermophila

Microbial sulfur cycling in marine sediments often occurs in environments characterized by transient chemical gradients that affect both the availability of nutrients and the activity of microbes. High turnover rates of intermediate valence sulfur compounds and the intermittent availability of oxygen in these systems greatly impact the activity of sulfur‐oxidizing micro‐organisms in particular. In this study, the thiosulfate‐oxidizing hydrothermal vent bacterium Thiomicrospira thermophila strain EPR85 was grown in continuous culture at a range of dissolved oxygen concentrations (0.04–1.9 mM) and high pressure (5–10 MPa) in medium buffered at pH 8. Thiosulfate oxidation under these conditions produced tetrathionate, sulfate, and elemental sulfur, in contrast to previous closed‐system experiments at ambient pressure during which thiosulfate was quantitatively oxidized to sulfate. The maximum observed specific growth rate at 5 MPa pressure under unlimited O₂ was 0.25 hr^?1. This is comparable to the μ_max (0.28 hr^?1) observed at low pH (<6) at ambient pressure when T. thermophila produces the same mix of sulfur species. The half‐saturation constant for O₂ () estimated from this study was 0.2 mM (at a cell density of 10⁵ cells/ml) and was robust at all pressures tested (0.4–10 MPa), consistent with piezotolerant behavior of this strain. The cell‐specific was determined to be 1.5 pmol O₂/cell. The concentrations of products formed were correlated with oxygen availability, with tetrathionate production in excess of sulfate production at all pressure conditions tested. This study provides evidence for transient sulfur storage during times when substrate concentration exceeds cell‐specific and subsequent consumption when oxygen dropped below that threshold. These results may be common among sulfur oxidizers in a variety of environments (e.g., deep marine sediments to photosynthetic microbial mats).