Temperature regulation during centrifugal elutriation and its effect on cell separation

Centrifugal elutriation appears to be a promising method for cell separation. The quality of the separation may be limited by the control of temperature within the separation chamber, which affects the fluid viscosity and rotor speed. The factors affecting the temperature regulation have been re-examined. At flow rates between 10 and 40 mL/min the temperature within the chamber was primarily dependent on the temperature of the fluid flowing into the rotor. Increases in the temperature of the fluid while it flowed through the rotor were observed and were greater at higher rotor speeds and lower flow rates. This heating, caused by friction at the rotating seal, could raise the fluid temperature within the chamber by as much as 6°C. Fluctuations in the temperature of the centrifuge produced temperature variations of only 0.3°C in the fluid in the elutriation chamber. Small increases in the rate of elutriation of cells, concomitant with centrifuge cooling and speed fluctuations, were detected by optical density measurements. However, neither the modal volume nor coefficient of variation of the collected cells were affected.     

Resolution of cells by centrifugal elutriation

Cell separation using the Beckman elutriator depends upon the flow rate of the medium and the centrifugal field employed. Changes in either the centrifugal field or the flow rate can be used to elute fractions of cells based on size. Even when these variables are held constant in the Beckman J21C centrifuge, a periodic pulse of cells is eluted. We have found that this anomolous elution is related to the temperature control system which gave a periodically pulsed temperature drop in the centrifuge well. The elution resulting from this change in temperature caused a shift in the modal cell size of the fraction eluted at a particular flow rate and centrifugal field. Because of this, the fractions have a larger size dispersion than fractions collected under conditions where refrigeration-related temperature fluctuations do not occur. We conclude that the temperature control system of the Beckman J21C centrifuge used with the Beckman elutriation rotor produces temperature fluctuations which prevent maximum resolution of cells.     

Characterization of the separation properties of the beckman elutriator system

The role of fluid flow in the elutriation process was visualized by pumping dye solution through the Beckman JE-6 elutriator rotor. Three major fluid flow disturbances were observed in the separation chambers, namely; jet-streaming, ripple flow, and whirl flow. In order to evaluate the effects of these non-ideal fluid flow patterns on the separation of homogeneous populations of particles or cells, 12–35 μm diameter latex spheres and 9L rat brain tumor cells were fractionated with the Beckman elutriator system. The elutriator system was evaluated on the basis of: (1) recovery, (2) elution loss during loading, (3) homogeneity of the size distributions, and (4) the relationship of the median volume of eluted particles or cells to the rotor speed and the collection fluid velocity. Both a conventional collection method (two 40-mL fractions at each collection rotor speed) and a long collection method (10–15 40-mL fractions at several collection rotor speeds) were compared to determine if collection procedures could compensate for some of the difficulties caused by the non-ideal fluid flow patterns. Although more than 90% of the particles or cells were always recovered, about 5% eluted during the loading procedure. Neither collection method altered this phenomenon. The collected populations, but this was accompanied by a reduction in cell yield. The median particle or cell volume of each fraction agreed with that expected under ideal fluid flow conditions except at high and low rotor speeds when the conventional collection method was used.     

Characterization of the separation properties of the Beckman elutriator system

The role of fluid flow in the elutriation process was visualized by pumping dye solution through the Beckman JE-6 elutriator rotor. Three major fluid flow disturbances were observed in the separation chambers, namely; jet-streaming, ripple flow, and whirl flow. In order to evaluate the effects of these non-ideal fluid flow patterns on the separation of homogeneous populations of particles or cells, 12--35 micron diameter latex spheres and 9L rat brain tumor cells were fractionated with the Beckman elutriator system. The elutriator system was evaluated on the basis of: (1) recovery, (2) elution loss during loading, (3) homogeneity of the size distributions, and (4) the relationship of the median volume of eluted particles or cells to the rotor speed and the collection fluid velocity. Both a conventional collection method (two 40-mL fractions at ech collection rotor speed) and a long collection method (10--15 40-mL fractions at several collection rotor speeds) were compared to determine if collection procedures could compensate for some of the difficulties caused by the non-ideal fluid flow patterns. Although more than 90% of the particles or cells were always recovered, about 5% eluted during the loading procedure. Neither collection method altered this phenomenon. The long collection method significantly improved the homogeneity of the collected populations, but this was accompanied by a reduction in cell yield. The median particle or cell volume of each fraction agreed with that expected under ideal fluid flow conditions except at high and low rotor speeds when the conventional collection method was used.     

Theory and practice of centrifugal elutriation (CE). Factors influencing the separation of human blood cells

Centrifugal elutriation (CE) is currently a widely used preparative cell separation technique. In order to optimize the separation of cells that show only small differences in sedimentation velocity, several conditions that might influence the resolution capacity, such as rotor speed, counterflow, jetstream, cell load, density, and viscosity of the elutriation medium, were analyzed. Experiments carried out with human red blood cells (rbc) indicated that selective losses of rbc from the rotor caused by the jetstream, could be prevented if the separations were carried out at high rotor speeds, as predicted by the theory. In addition, high cell loads (5 X 10(8) rbc) resulted in better separations than low cell loads (5 X 10(7) rbc). Human monocytes were separated into subpopulations that differed only about 0.003 g/mL in density, but have virtually the same size. The separation was carried out either by increasing the density or viscosity of the elutriation medium or by decreasing the rotor speed. In all cases similar results were obtained. These results indicated that under optimal conditions CE can be applied for the separation of cells that differ only slightly in sedimentation velocity.     

Theory and practice of centrifugal elutriation (CE)

Centrifugal elutriation (CE) is currently a widely used preparative cell separation technique. In order to optimize the separation of cells that show only small differences in sedimentation velocity, several conditions that might influence the resolution capacity, such as rotor speed, counterflow, jetstream, cell load, density, and viscosity of the elutriation medium, were analyzed. Experiments carried out with human red blood cells (rbc) indicated that aselective losses of rbc from the rotor caused by the jetstream, could be prevented if the separations were carried out at high rotor speeds, as predicted by the theory. In addition, high cell loads (5×10⁸ rbc) resulted in better separations than low cell loads (5×10⁷ rbc). Human monocytes were separated into subpopulations that differed only about 0.003 g/mL in density, but have virtually the same size. The separation was carried out either by increasing the density or viscosity of the elutriation medium or by decreasing the rotor speed. In all cases similar results were obtained. These results indicated that under optimal conditions CE can be applied for the separation of cells that differ only slightly in sedimentation velocity.     

Subcellular fractionation of wheat leaf protoplasts by centrifugal elutriation

A new method using centrifugal elutriation for subcellular fractionation of plant cells has been developed. This method takes advantage of the fact that particles sedimenting in a gravitational field can be eluted by flow against the field. A wheat protoplast homogenate was fed into an elutriation rotor spinning at high speed and the flow rate into the rotor was gradually increased. The smaller and less dense materials such as mitochondria, microbodies, endoplasmic reticulum, and cytoplasm were elutriated earlier than the larger and denser nuclei and chloroplasts. The intact chloroplasts, free of mitochondria, microbodies, endoplasmic reticulum, and cytoplasm, could be obtained within 40 min following the rupture of protoplasts. The chlorophyll-free mitochondria could be obtained within 80 min.     

Force and velocity of mycoplasma mobile gliding

The effects of temperature and force on the gliding speed of Mycoplasma mobile were examined. Gliding speed increased linearly as a function of temperature from 0.46 microm/s at 11.5 degrees C to 4.0 microm/s at 36.5 degrees C. A polystyrene bead was attached to the tail of M. mobile using a polyclonal antibody raised against whole M. mobile cells. Cells attached to beads glided at the same speed as cells without beads. When liquid flow was applied in a flow chamber, cells reoriented and moved upstream with reduced speeds. Forces generated by cells at various gliding speeds were calculated by multiplying their estimated frictional drag coefficients with their velocities relative to the liquid. The gliding speed decreased linearly with force. At zero speed, the force measurements extrapolated to 26 pN at 22.5 and 27.5 degrees C. At zero force, the speed extrapolated to 2.3 and 3.3 microm/s at 22.5 and 27.5 degrees C, respectively--the same speeds as those observed for free gliding cells. Cells attached to beads were also trapped by an optical tweezer, and the stall force was measured to be 26 to 28 pN (17.5 to 27.5 degrees C). The gliding speed depended on temperature, but the maximum force did not, suggesting that the mechanism is composed of at least two steps, one that generates force and another that allows displacement. Other implications of these results are discussed.     

One-step isolation of neutrophils using an elutriator

Summary To simplify the isolation of neutrophils, we developed a one-step procedure using elutriation. The perfusate (0.2% gelatin and 0.1% glucose in phosphate buffered saline) was pumped through an elutriator rotor at 4 ml/min (25° C) with the rotor speed at 2370 rpm. Twenty milliliters of anticoagulated porcine venous blood were mixed with 60 ml of perfusate and loaded into the elutriator chamber. The flow rate was increased by 2 ml/min increments and 100-ml fractions of effluent were collected at each increment. Concentrations of neutrophils and mononuclear cells were measured in each fraction, and the percentage of total neutrophils or mononuclear cells was plotted against flow rate. The optimal yield (46%) and purity (95.1%) of neutrophils (n=8) was obtained in pooled fractions at flow rates greater than 20 ml/min. Neutrophils in this preparation were round, the granules were intact, and the nuclei were lobulated. In addition, the cells produced superoxide in the presence of phorbol myristate acetate and phagocytosed zymosan particles. These characteristics were similar to those of porcine neutrophils prepared by a conventional sedimentation method. The yield (43%) and purity (94%) of human neutrophils isolated using the elutriator method was similar to that for porcine cells. This one-step method provides a moderate yield of pure neutrophils that have retained their morphology and function. This work was supported by the Canadian Heart Foundation.     

Isolation of alveolar type II cells by centrifugal elutriation.

Centrifugal elutriation (counterflow centrifugation) was used to develop a reproducible method for obtaining a nearly pure population of isolated alveolar type II cells. Lung was dissociated into individual cells with recrystallized trypsin, and the type II cells were partially purified by centrifugation on a discontinuous density gradient. The alveolar type II cells were finally purified by centrifugal elutriation. Cells were collected from the elutriator rotor by stepwise increases in flow rates. Cells obtained at flow rates of 7 and 14 ml per min were lymphocytes, other small cells, a few type II cells and cell debris; cells collected at flow rates of 18 and 22 ml per min were mainly type II cells; and cells collected at flow rates of 28, 34 and 43 ml per min were macrophages, some type II cells, other lung cells and cell aggregates. At flow rates of 18 and 22 ml per min, 1.9 +/- 1.0 x 10(6) cells per rat lung (mean +/- S.D., n=30) were recovered of which 86 +/- 6% were type II cells. At these flow rates, 94% of the cells excluded the vital dye erythrosin B from their cytoplasm. They consumed oxygen at a rate of 101 +/- 21 nmol per hr . 10(6) cells (mean +/- S.D., n=4), and their oxygen consumption increased only 10% after 10 mM sodium succinate was added. The cells incorporated [14C]leucine into protein and lipid for 4 hr. Electron micrographs of the cells collected at flow rates of 18 and 22 ml per min show a high percentage of morphologically intact alveolar type II cells. We conclude that centrifugral elutriation is a reproducible method for obtaining nearly pure, metabolically active alveolar type II cells.     

Analytical techniques for cell fractions. XVI. Preparation of protein-free supernatants with a "Z"-path rotor

A new “Z”-path centrifuge rotor is described for the separation of pellets from supernatants in up to 15 samples simultaneously. The samples and precipitating solutions are stored in separate chambers at rest, and are transferred to a sedimentation chamber by centrifugal force during rotation, where mixing occurs during rapid changes in speed, followed by sedimentation of the precipitate. The supernatant decants itself at rest into a third series of chambers, where it may be transferred centrifugally into radially disposed measuring devices, transferred with suitable pipettes, or used as a sample ring for conventional analyzers.     

Use of a modified rotor and enlarged separation chamber for isolation of human granulocytes by counterflow centrifugation-elutriation

Human granulocytes were isolated from leukapheresis blood by counterflow centrifugation-elutriation using the Beckman J21B centrifuge and JE6 rotor. Attempts to increase the absolute number of human granulocytes recovered by a single- or double-chamber procedure revealed the physical limitations of the chamber capacity in granulocyte isolation. To improve the absolute number of granulocytes from leukapheresis blood, an enlarged separation chamber and accompanying rotor were fabricated. The enlarged chamger has three times the capacity of the standard 4.5-ml Beckman chamber. Aside from increased yield of granulocytes, the 13.2-ml chamber affords a 25% saving in isolation time compared to the Beckman chamber for isolation of a comparable number of cells. In vitro analysis of the isolated granulocytes for viability, latex bead ingestion, and chemotactic response indicate no apparent loss of granulocyte function as a result of the isolation procedure.     

A separation chamber to sort cells,nuclei, and chromosomes at moderate g forces. II. Studies on velocity sedimentation and equilibrium density centrifugation of mammalian cells

A separation chamber having a surface of 50 cm² and a height of 2 cm is described for the rapid separation of cells and cell organelles at acceleration forces from 10 to 90g. To eliminate wall sedimentation artifacts, the chamber was positioned 20 cm from the rotor axis in a speed-controlled centrifuge. The chamber has flow deflectors for the undisturbed introduction of the sample layer and the gradient; an antivortex cross prevents swirling upon acceleration and deceleration. To illustrate the use of the separation chamber, examples of velocity sedimentation and of equilibrium density centrifugation are given: (i) human monocytes (70% were 90% pure) are separated from lymphocytes in 10 min at 20g; (ii) nonparenchymal rat liver cells are separated in 10 min at 16g in 97% pure endothelial cells and 99% pure Kupffer cells; (iii) equilibrium density centrifugation of human peripheral blood cells at about 90g permits the separation of erythrocytes, monocytes, lymphocytes, neutrophils, eosinophils, and basophils in one run. B cells are separated from T cells. The movement of swinging buckets is analyzed in mathematical terms and a simple method is offered to determine the position of cells in density gradients with the use of a small programmable calculator.     

Isolation of human mononuclear cell subsets by counterflow centrifugal elutriation (CCE). I. Characterization of B-lymphocyte-, T-lymphocyte-, and monocyte-enriched fractions by flow cytometric analysis

Rapid separation of large numbers of human peripheral blood mononuclear cells into fractions enriched for B lymphocytes, T lymphocytes, or monocytes was accomplished by counterflow centrifugal elutriation (CCE). The first fraction contained 98% of the platelets. Ten additional fractions containing subpopulations of mononuclear cells were collected by sequential increases in the flow rate while maintaining a constant centrifuge speed. Analysis of the fractions using monoclonal antibodies revealed that fraction 2, which was free of esterase-positive monocytes, was highly enriched for B cells. T lymphocytes (OKT3+) were the predominant cell type found in fraction 4. No enrichment for T-lymphocyte-helper (OKT4+) or -suppressor (OKT8+) subpopulations was observed in the lymphocyte containing fractions. Three fractions (7-9), highly enriched for esterase-positive cells, were predominantly OKM1+ monocytes with no evidence of selective separation of monocyte subpopulations. Thus, cell fractions enriched for B cells, T cells, and monocytes could be obtained, by utilizing CCE, in large enough quantities to enable analysis of their functional properties. Of particular interest was the ability to separate small, resting B lymphocytes from monocytes.     

Cell separator operation within temperature ranges to minimize effects on Chinese hamster ovary cell perfusion culture

A cell retention device that provides reliable high-separation efficiency with minimal negative effects on the cell culture is essential for robust perfusion culture processes. External separation devices generally expose cells to periodic variations in temperature, most commonly temperatures below 37 degrees C, while the cells are outside the bioreactor. To examine this phenomenon, aliquots of approximately 5% of a CHO cell culture were exposed to 60 s cyclic variations of temperature simulating an acoustic separator environment. It was found that, for average exposure temperatures between 31.5 and 38.5 degrees C, there were no significant impacts on the rates of growth, glucose consumption, or t-PA production, defining an acceptable range of operating temperatures. These results were subsequently confirmed in perfusion culture experiments for average exposure temperatures between 31.6 and 38.1 degrees C. A 2(5-1) central composite factorial design experiment was then performed to systematically evaluate the effects of different operating variables on the inlet and outlet temperatures of a 10L acoustic separator. The power input, ambient temperature, as well as the perfusion and recycle flow rates significantly influenced the temperature, while the cell concentration did not. An empirical model was developed that predicted the temperature changes between the inlet and the outlet of the acoustic separator within +/-0.5 degrees C. A series of perfusion experiments determined the ranges of the significant operational settings that maintained the acoustic separator inlet and outlet temperatures within the acceptable range. For example, these objectives were always met by using the manufacturer-recommended operational settings as long as the recirculation flow rate was maintained above 15 L day(-1) and the ambient temperature was near 22 degrees C.     

Isolation of alveolar type II cells by centrifugal elutriation

Summary Centrifugal elutriation (counterflow centrifugation) was used to develop a reproducible method for obtaining a nearly pure population of isolated alveolar type II cells. Lung was dissociated into individual cells with recrystallized trypsin, and the type II cells were partially purified by centrifugation on a discontinuous density gradient. The alveolar type II cells were finally purified by centrifugal elutriation. Cells were collected from the elutriator rotor by stepwise increases in flow rates. Cells obtained at flow rates of 7 and 14 ml per min were lymphocytes, other small cells, a few type II cells and cell debris; cells collected at flow rates of 18 and 22 ml per min were mainly type II cells; and cells collected at flow rates of 28, 34 and 43 ml per min were macrophages, some type II cells, other lung cells and cell aggregates. At flow rates of 18 and 22 ml per min, 1.9±1.0×10⁶ cells per rat lung (mean±S.D.,n=30) were recovered of which 86±6% were type II cells. At these flow rates, 94% of the cells excluded the vital dye erythrosin B from their cytoplasm. They consumed oxygen at a rate of 101±21 nmol per hr·10⁶ cells (mean±S.D.,n=4), and their oxygen consumption increased only 10% after 10mm sodium succinate was added. The cells incorporated [¹⁴C]leucine into protein and lipid for 4 hr. Electron micrographs of the cells collected at flow rates of 18 and 22 ml per min show a high percentage of morphologically intact alveolar type II cells. We conclude that centrifugal elutriation is a reproducible method for obtaining nearly pure, metabolically active alveolar type II cells. Postdoctoral trainee supported by Grants HL-05251 and HL-07192 from the National Heart, Lung and Blood Institute. This work was supported by U.S. Public Health Service Grants Program-Project HL-06285 and Pediatric Pulmonary SCOR HL-19185, and by a grant-in-aid from the American Heart Association (77-1098).     

Limited use of Centritech Lab II Centrifuge in perfusion culture of rCHO cells for the production of recombinant antibody

Perfusion cultures of recombinant Chinese hamster ovary cells, producing recombinant antibody against the S surface antigen of Hepatitis B virus, were carried out in continuous and intermittent mode using a Centritech Lab II Centrifuge. In the continuous perfusion process, despite the absence of shear stress from the pump head, long-term operation was not possible because of continuously repeated exposure to oxygen limitation and low temperature, as well as shear stress from centrifugal force. In the intermittent perfusion processes, the frequency of cell-passage through the centrifuge was substantially reduced, compared with the continuous perfusion mode; however, the degree of reduction could not guarantee stable long-term operation. Although various operating parameters were applied in the intermittent perfusion cultures, high cell densities could not be maintained stably. In a single bioreactor culture system, a specific cell that is returned from the centrifuge to the bioreactor could be transferred from the bioreactor to the centrifuge again in the next cycle. These repetitive damages, caused by shear stress from the pump head and centrifugal force, as well as exposure to suboptimal conditions such as oxygen limitation and low temperature below 37 degrees C, were more serious at higher perfusion rates. Subsequently, damaged cells and dead cells were continuously accumulated in the bioreactor. Culture temperature shift from 37 to 33 degrees C increased antibody concentrations but showed inhibitory effects on cell growth. The negative effects of lowering culture temperature on cell growth overwhelmed the positive effects on antibody production. To protect cells from shear stress, Pluronic F-68 was 2-fold concentrated in the culture medium; nevertheless, a significantly higher concentration of Pluronic F-68 (2 g/L) may have inhibitory effects on cell growth.     

Zonal unit-gravity elutriation

A new and simple technique, zonal unit-gravity elutriation, has been devised for separating very large cells, multicellular complexes, or small organisms from suspensions consisting mainly of small cells. The separation vessel is a conical chamber with an entrance at the lower, narrower part of the cone and an exit at the upper, wider part of the cone via a dome-shaped lid. A baffle at the entrance prevents turbulence from incoming fluid. Chambers of differing widths and wall slopes are chosen depending on the sedimentation rate of the particles to be separated. A small volume of the cell suspension is placed in the chamber on the bench in a cold-room. Medium stabilized by a shallow density gradient is pumped into the base of the chamber and ascends, creating a decreasing velocity gradient. Cells sediment at unit-gravity against this ascending counterstream, and are separated into bands according to sedimentation velocity. By adjusting the flow rate of the medium, different sizes of cells can be separated. Tumor cells can be enriched, and larger blast cells can be separated from small cells in lymphoid cell suspensions. The procedure produces complete separation of thymic nurse cells (epithelial-lymphoid complexes) from free thymocytes in digested thymus suspensions and produces substantial enrichment of thymic rosettes (macrophage-lymphoid complexes). A very favorable situation for applying this technique is the isolation ofTaenia taeniaformis larvae, which can be completely purified from infected liver suspensions, representing a 4×10⁵-fold enrichment of the parasites, with high recovery, in a single 30 min operation.     

Zonal unit-gravity elutriation. A new technique for separating large cells and multicellular complexes from cell suspensions

A new and simple technique, zonal unit-gravity elutriation, has been devised for separating very large cells, multicellular complexes, or small organisms from suspensions consisting mainly of small cells. The separation vessel is a conical chamber with an entrance at the lower, narrower part of the cone and an exit at the upper, wider part of the cone via a dome-shaped lid. A baffle at the entrance prevents turbulence from incoming fluid. Chambers of differing widths and wall slopes are chosen depending on the sedimentation rate of the particles to be separated. A small volume of the cell suspension is placed in the chamber on the bench in a cold-room. Medium stabilized by a shallow density gradient is pumped into the base of the chamber and ascends, creating a decreasing velocity gradient. Cells sediment at unit-gravity against this ascending counterstream, and are separated into bands according to sedimentation velocity. By adjusting the flow rate of the medium, different sizes of cells can be separated. Tumor cells can be enriched, and larger blast cells can be separated from small cells in lymphoid cell suspensions. The procedure produces complete separation of thymic nurse cells (epithelial-lymphoid complexes) from free thymocytes in digested thymus suspensions and produces substantial enrichment of thymic rosettes (macrophage-lymphoid complexes). A very favorable situation for applying this technique is the isolation of Taenia taeniaformis larvae, which can be completely purified from infected liver suspensions, representing a 4 X 10(5)-fold enrichment of the parasites, with high recovery, in a single 30 min operation.     

Cell cycle synchronization of animal cells and nuclei by centrifugal elutriation

Synchronization of cells and nuclei is a powerful technique for the exact study of regulatory mechanisms and for understanding cell cycle events. Counterflow centrifugal elutriation is a biophysical cell separation technique in which cell size and sedimentation density differences of living cells are exploited to isolate subpopulations in various stages of cell cycle. Here, a protocol is described for the separation of phase-enriched subpopulations from exponentially growing Chinese hamster ovary cells at high-resolution power of elutriation. The efficiency of elutriation is confirmed by measuring the DNA content fluorimetrically and by flow cytometry. The resolution power of elutriation is demonstrated by the ability to fractionate nuclei of murine pre-B cells. The installation and elutriation by collecting 16-30 synchronized fractions, including particle size analysis, can be achieved in 4-5 h.