Generation Time and Growth Rate of the Human Intestinal Parasite Blastocystis hominis

ABSTRACT. Blastocystis hominis , an anaerobic intestinal protozoan parasite of man, has a generation time (GT) in axenic culture of 8.5–19.4 h, depending on the strain tested. Average GT of the eight strains was 11.7 h. Zero growth time cell counts of 5.0 × 10⁵/ml to 2.0 × 10⁶/ml rose in 3–5 days to 1 × 10⁷ or 1 × 10⁸ cells/ml. The GT was determined for the 24-h period during which the most rapid growth occurred; about 2% of the B. hominis cells were in division during this time. Division under the culture conditions provided was by binary fission, the usual mode for B. hominis in vitro as well as in vivo. Division times were determined also by direct observation of individual dividing cells in slide cultures. These were usually ca. 40–60 min but sometimes as low as 20 min.     

Anchorage-dependent mammalian cell culture using polyurethane foam as a new substratum for cell attachment

Summary Anchorage-dependent mammalian cells were cultivated at high cell density in a novel culture system using polyurethane foam (PUF) as a substratum for cell attachment. PUF has a macroporous structure giving a high surface area to volume ratio. Monkey kidney cells (Vero) and Chinese hamster ovary cells (CHO-K1) attached to the internal surface of PUF and grew to a high cell density (1.04 × 10⁸ cells/ cm³ PUF and 3.5 × 10⁷ cells/ cm³ PUF, respectively) in PUF stationary cultures. In addition, we have designed a PUF-particle packed-bed culture system for high density mass cell culture. A maximum cell density of 2.4 × 10⁷ cells/cm³ culture vessel volume was obtained in a packed-bed culture of Vero cells. Offprint requests to: K. Funatsu     

High density culture of anchorage-dependent animal cells by polyurethane foam packed-bed culture systems

Summary Monkey kidney cells (Vero) and Chinese hamster ovary cells (CHO-K1) attached to the internal surface of polyurethane foam (PUF) and grew to a high cell density (1.1 × 10⁸ cells/cm³ PUF and 4.2 × 10⁷ cells/cm³ PUF, respectively) in a PUF-plates packed-bed culture system. This density of Vero cells was twice that obtained previously with a PUF-particles packed-bed culture system. A maximum cell density of 6.7 × 10⁷ cells/cm³ culture vessel volume was obtained in a PUF-disc packed-bed culture of Vero cells. From the cell density of CHO-K1, growing in a monolayer on the surface of PUF and a petri dish, per bulk volume of PUF, we estimated that a surface area to volume ratio of PUF plates effective for cell growth was about 109 cm²/cm³.Offprint requests to: K. Funatsu     

Lysis by interleukin 2-stimulated tumor-infiltrating lymphocytes of autologous and allogeneic tumor target cells

Summary Stepwise counterflow centrifugal elutriation of leukapheresed human mononuclear cells (MNC) in a Beckman JE-6B rotor and J6-M/E centrifuge yielded a population highly enriched in natural killer (NK) cells (70–75% large granular lymphocytes with 10–13 times greater NK activity) at a flow rate of 38–44 ml/min using a fixed rotor speed of 3000 rpm at 27° C. However, the mean cell recovery was <1%. To obtain sufficient numbers of purified NK cells for adoptive immunotherapy, a strategy combining counterflow centrifugal elutriation with adherence of recombinant interleukin-2(rIL-2)-activated NK cells to plastic was developed. First, MNC were elutriated to give a twofold enrichment in NK cells, containing 22% Leu19⁺ cells, 18% large granular lymphocytes and 51 lytic units of activity against K562 targets as opposed to the unfractionated MNC containing 10% Leu19⁺ cells, 7% large granular lymphocytes and 26 lytic units of activity. The mean recovery was 80±15% (n=10). Further enrichment was obtained by isolation of the elutriated cells that adhered to plastic after culture for 24 h in the presence of 1000 U/ml rIL-2. The initial adherent lymphokine-activated killer (A-LAK) cells represented 1–4% of total MNC, but their subsequent expansion was at least 10–22-fold during 8–14 days in culture with 1000 U/ml rIL-2. Using this strategy, 2 × 10⁹ normal MNC, obtained by leukapheresis, yielded 5 × 10⁸ A-LAK cells with a total of 5.7 × 10⁵ lytic units of cytotoxicity against K562 and a total of 3.3 × 10⁵ lytic units against Daudi targets. This enrichment method has yielded sufficient numbers of A-LAK cells to form the basis for a phase I clinical trial of adoptive immunotherapy in patients with advanced cancer.     

High cell density perfusion culture of mouse-human hybridomas

Summary Five mouse-human hybridomas, H2, H3, V1, V2 and V6 cells secreting anti-virus human monoclonal immunoglobulin G (IgG) were cultured in serum-free media at high density in a settling perfusion culture vessel with an inner cell sedimentation zone. The H2, H3 and V6 cells reached a density of 10⁷ cells/ml in 0.5% (w/v) BSA-ITES-eRDF (see Materials and methods). The H2 cells reached only 6.8 × 10⁶ cells/ml in the absence of bovine serum albumin (BSA), but the addition of 0.2% (w/v) Pluronic F68 increased the maximum cell density to 1.1 × 10⁷ cells/ml, which was the same level as in BSA including medium. On the other hand, Pluronic F68 showed no stimulative effect on the growth of H2 cells in static culture. Pluronic F68 also increased the maximum cell density of V2 cells from 4.6 × 10⁶ cells/ml to 6.9 × 10⁶ cells/ml even in the presence of 0.5% (w/v) BSA.     

Hydroxyapatite-pulp composite fiber sheet bed: A new material for the immobilization of CHO-K1 cells

A new immobilization material for cell culture, ahydroxyapatite-pulp composite fiber (HAPC) sheet bed, was usedto grow CHO-K1 cells. The sheet bed for cell culture wasprepared from HAPC fiber by paper-making techniques. Scanning electron microscopic analysis revealed that the HAPCsheet bed had a structure consisting of piled fibers with spaces 10–200 m in diameter and a pore surface area of 0.32 m² g^-1. Using a 25 × 25 mm² squareHAPC sheet bed 0.41 mm in thickness (85 g m^-2 basis weight) for cell culture, CHO-K1 cells grew to a cell densityof 3.7 × 10⁷ cells cm^-3 in a 60 mm plastic dish over a 6-day culture period. High-density culture of CHO-K1 cells was successfully performed using the HAPC sheet bed in a 500 ml spinner flask over a 21-day culture period. The HAPC sheet bed, wound around the stirrer paddle, was rotated in the spinner flask in order to supply nutrientsand remove waste products efficiently. The HAPC sheet bedhas a large surface area to support cell growth and there islarge diffusion space inside of the bed. This newautoclavable substrate for anchorage-dependent cells can be easily scaled-up.     

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.     

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

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

Large-scale perfusion culture process for suspended mammalian cells that uses a centrifuge with multiple settling zones

A high-cell-density perfusion culture process, using a novel centrifuge, was developed. The centrifuge has spiral multiple settling zones to separate cells from culture medium. Because of the multiple zones, the separation area can be efficiently increased without enlarging the diameter of the centrifuge. The centrifuge used in this study had a separation capacity of 2600 ml culture medium min^–1 at 100g of the centrifugal force. A new cell separation and withdrawal method was also developed. The cells separated in the centrifuge can be withdrawn easily from the centrifuge with no cell clogging by feeding a liquid carrier such as a perfluorocarbon into the centrifuge and pushing the cells out with the liquid carrier. By this culture process, monoclonal antibodies were produced with mouse-human hybridoma X87X at a cell density of about 8 × 10⁶ cells ml^–1 for 25 days. This centrifuge culture shows promise as a large-scale perfusion culture process.     

Nucleus image properties and cell death in MCF-10F cells grown on slide substrates differing in nature and size

Summary The immortalized human breast epithelial cell line MCF-10F is an important tool for studies on experimental tumorigenesis induced by drugs, transfected Ha-ras oncogene, and hormones. Considering that many relevant data have thus far been established only for MCF-10F cells cultivated on glass, and that there are data showing different cell death ratios for tumorigenic cells obtained from benzo[a]pyrene (BP)-transformed MCF-10F cells cultivated on plastic compared with glass, nuclear parameters estimated by image analysis and cell death ratios were compared for cells grown on plastic and glass substrates differing in chamber surface sizes and working culture medium volumes. It was concluded that for slides with a growth size equal to 9.4 cm², plastic substrate was more advantageous than glass for growing MCF-10F cells because although the apoptotic ratios (AR) for the cells grown on plastic are low as it would be expected for nontransformed cells, they are bigger than those reported for the BP-transformed MCF-10F cells cultivated on the same substrate but closer to those of the BP-transformed MCF-10F cells receiving a normal chromosome 17. In addition, the plastic substrate did not induce variable nuclear image results as those found in the latter. The 0.5-cm²-sized chambers on plastic slides proved to be inadequate for cell nuclear image analysis and cell death studies on account of the variable geometric, densitometric, and textural results and ARs produced and the unpublished consideration of a very slow growth rate generated under this growth condition.     

Attachment, spreading and growth of VERO cells on microcarriers for the optimization of large scale cultures

The VERO cell attachment, spreading and growth were measured as a function of the substrate and temperature used for cell cultivation, the presence of fetal calf serum (FCS) in the medium and the initial cell inoculum used for cultivation on MCs. The data show that the cell attachment kinetics were comparable at RT or 37v°C, a higher rate of cell attachment occurred to MCs and the presence of FCS inhibited the cell attachment to glass or plastic but not to MCs. The cell spreading, in general higher at 37v°C, was dependent on the presence of FCS, comparable on glass or plastic substrate and lower on MCs. The spread of VERO cells over MCs was fully dependent on the presence of FCS and decreases progressively with a delayed addition of FCS into the medium. The cell detachment by trypsin was slower from MCs and the cells recovered showed lower viability and reattachment. Better results of detachment, viability and reattachment were obtained by treatment with the trypsin at pH of 8 instead of 7. The lower was the number of cells/MC for the initial inoculum, the higher was the percent of unoccupied MCs (with 1 cell/MC we had 35.6% of unoccupied MCs), which were shown to remain uncovered during the whole period of culture. With an initial inoculum of 4, 6 and 8 VERO cells/MC, respectively 46%, 76% and 83% of the MCs were totally covered by cells after 7 days, the cultures showing at this time, respectively, 5.1 2 10⁵, 8.8 2 10⁵ and 1.8 2 10⁶ cells/ml, which represented a biomass production of respectively 8.5x, 9.7x and 15.5x. When compared to 175 cm² T-flasks, using the same amount of medium, a VERO cell culture on 2 mg/ml of MCs offers about 10 times more available surface for cell growth and allowed the obtention of 7 times more cells. The optimization procedures concerning initial steps of VERO cell cultures, such as the attachment, spreading and growth as a function of parameters like initial cell inoculum and medium supplementation are of special interest mainly due to the perspective of a large use of VERO cell cultures for human viral vaccine production.     

Microbial carrying capacity and carbon biomass of plastic marine debris

Trillions of plastic debris fragments are floating at sea, presenting a substantial surface area for microbial colonization. Numerous cultivation-independent surveys have characterized plastic-associated microbial biofilms, however, quantitative studies addressing microbial carbon biomass are lacking. Our confocal laser scanning microscopy data show that early biofilm development on polyethylene, polypropylene, polystyrene, and glass substrates displayed variable cell size, abundance, and carbon biomass, whereas these parameters stabilized in mature biofilms. Unexpectedly, plastic substrates presented lower volume proportions of photosynthetic cells after 8 weeks, compared to glass. Early biofilms displayed the highest proportions of diatoms, which could influence the vertical transport of plastic debris. In total, conservative estimates suggest 2.1 × 10²¹ to 3.4 × 10²¹ cells, corresponding to about 1% of the microbial cells in the ocean surface microlayer (1.5 × 10³ to 1.1 × 10⁴ tons of carbon biomass), inhabit plastic debris globally. As an unnatural addition to sea surface waters, the large quantity of cells and biomass carried by plastic debris has the potential to impact biodiversity, autochthonous ecological functions, and biogeochemical cycles within the ocean.Subject terms: Microbial ecology, Environmental sciences     

Fixed bed porous glass sphere (porosphere) bioreactors for animal cells

Process intensity of fixed bed glass sphere culture systems is increased considerably by replacing solid glass spheres with open pore glass spheres. This technique demonstrates the possibility of having a system capable of both volumetric and cell density scale up and being suitable for substrate attached and suspension cells. The yields achieved for a number of attached cell lines (approximately 10⁷/ml) demonstrate an increase approaching one order of magnitude over solid glass spheres (approximately 10⁶/ml). Also suspension cells were successfully entrapped in the open pore structure with similar yields.     

Quantitative Microbiological Analysis of Bacterial Community Shifts in a High-Rate Anaerobic Bioreactor Treating Sulfite Evaporator Condensate

The bacterial population of a high-rate, anaerobic, fixed-bed loop reactor treating sulfite evaporator condensate from the pulp industry was studied over a 14-month period. This period was divided into seven cycles that included a startup at the beginning of each cycle. Some 82% of the total biomass was immobilized on and between the porous glass rings filling the reactor. The range of the total number of microorganisms in these biofilms was 2 × 10⁹ to 7 × 10⁹ cells per ml. Enumeration and characterization by microbiological methods and by phase-contrast, epifluorescence, and electron microscopy showed that the samples consisted mainly of the following methanogens: a Methanobacterium sp., a Methanosarcina sp., a Methanobrevibacter sp., and a Methanothrix sp., as well as furfural-degrading sulfate-reducing bacteria resembling Desulfovibrio furfuralis. Viable counts of hydrogenotrophic methanogens were relatively stable (mostly within the range of 3.2 × 10⁸ to 7.5 × 10⁸ cells per ml), but Methanobrevibacter cells increased from <5 to 30% of the total hydrogenotrophic count after transfer of the fixed bed into a second reactor vessel. Acetotrophic methanogens reached their highest numbers of 1.3 × 10⁸ to 2.6 × 10⁸ cells per ml in the last fermentation cycles. They showed a morphological shift from sarcinalike packets in early samples to single coccoid forms in later phases of the fermentation. Furfural-degrading sulfate reducers reached counts of 1 × 10⁷ to 5.8 × 10⁷ cells per ml. The distribution of the chief metabolic groups between free fluid and biofilms was analyzed in the fifth fermentation cycle: 4.5 times more furfural degraders were found in the free fluid than in the biofilms. In contrast, 5.8 times more acetotrophic and 16.6 times more hydrogenotrophic methanogens were found in the biofilms than in the free liquid. The data concerning time shifts of morphotypes among the trophic groups of methanogens corroborated the trends observed by using immunological assays on the same samples.     

Technique for the Determination of the Rate of Ethylene Production by Pseudomonas solanacearum

A tube culture system was designed for measurement of ethylene evolved by the phytopathogenic bacterium, Pseudomonas solanacearum. The system consisted of 10 glass tubes joined together in series and coated on the inside surface with a dextrose-peptone-casamino acids agar medium. The system provided a large surface for bacterial growth in relation to the volume of air. The system was seeded with a bacterial suspension (7 × 10⁸ cells/ml) drawn through all the tubes by vacuum applied at one end and was then placed in a water bath at 30 C. Air was pumped through the system at 3 ml/min; the outlet was connected directly to the inlet port of a gas sampling loop and ethylene in the sample was determined by gas chromatography.     

Microencapsulation with poly(vinyl amine) and alginate

Summary Poly(vinyl amine) and alginate were used as the materials for microencapsulation. IW32 (a murine erythroleukemia cell line) cells were cultured within the capsules to a density of 8×10⁷ cells/ml, 40 times that obtained in the free-cell culture. Erythropoietin accumulated in the microcapsule to a concentration of 7.0 U/ml, about three times that in the extra-capsular medium and 14 times the concentration found in the medium of free-cell culture.     

Assessment of mass transfer and mixing in rigid lab‐scale disposable bioreactors at low power input levels

Mass transfer, mixing times and power consumption were measured in rigid disposable stirred tank bioreactors and compared to those of a traditional glass bioreactor. The volumetric mass transfer coefficient and mixing times are usually determined at high agitation speeds in combination with sparged aeration as used for single cell suspension and most bacterial cultures. In contrast, here low agitation speeds combined with headspace aeration were applied. These settings are generally used for cultivation of mammalian cells growing adherent to microcarriers. The rigid disposable vessels showed similar engineering characteristics compared to a traditional glass bioreactor. On the basis of the presented results appropriate settings for adherent cell culture, normally operated at a maximum power input level of 5 W m^?3, can be selected. Depending on the disposable bioreactor used, a stirrer speed ranging from 38 to 147 rpm will result in such a power input of 5 W m^?3. This power input will mix the fluid to a degree of 95% in 22 ± 1 s and produce a volumetric mass transfer coefficient of 0.46 ± 0.07 h^?1. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1269–1276, 2014     

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

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

Generation of lymphokine activated killer cells in a new high density dialyzing culture apparatus

In order to establish an efficient culture system for the generation of lymphokine activated killer (LAK) cells, we have developed a new device which is essentially based on a continuous dialyzing culture vessel. LAK cells grown in such a system showed higher cytotoxicity than those grown under conventional culture conditions. By using this new apparatus with continuous regulation of infused interleukin 2, nutritional medium, and pO₂ and pCO₂, yields of 2×10⁷ cells/ml were achieved and maintained for more than 21 days. These cells also showed a significant increase of LAK activity on a per cell basis.     

Resistance to the Brownian movement of red blood cells on flat horizontal surfaces

The movements of red blood cells (RBC), suspended in plasma, on plastic, glass, rhodium metal plate, siliconized glass, and siliconized rhodium were recorded on cinéfilm and analyzed. Values for the drag coefficient were calculated, using Einstein's theory of Brownian movement, and compared with the theoretical Stokes' hydrodynamic drag. The difference between the computed and Stokes' values gave the frictional coefficient or resistance resulting from the interaction of the cells, with the test surface. Of the three uncoated test surfaces, plastic was found to have the least interaction with the RBC. The frictional coefficient for plastic was found to be 1.75×10⁻⁷ N s m⁻¹ compared with a value of 2.82×10⁻⁷ N s m⁻¹ for rhodium metal, which had the largest interaction. Upon siliconization of the test surfaces, the interaction decreased by 40%. Reduction in the pH of the suspending plasma increased the interaction between the cells and the uncoated test surfaces, but the pH effect of diminished when the surfaces were siliconized.