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.     

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.     

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).     

A strategy for an improved separation of mammalian spermatids

A collection procedure has been developed to improve the homogeneity of mammalian spermatid populations separated by elutriation. Trypsinizied ram testis cells were elutriated at 18C. Every cell population was eluted by progressive changes in the flow rate and/or rotor speed, instead of by abrupt changes, to reduce the contamination by cells from the next population. Pure populations were collected alternating with mixed populations corresponding to the overlap between two adjacent pure populations. Furthermore, each pure population was collected into two subfractions, the second of which, contamined by cells from the following population, was pooled with the following fraction. In less than 2 hr after castration, three populations of at least 1 × 10⁸ viable round or elongated or elongating spermatids were obtained with respective purities of 95%, 82%, and 99% of the nucleated cells. In addition, two mixed populations containing only two adjacent spermatid types (round plus elongating spermatids: 98%; elongated plus elongating spermatids: 98%) were obtained, as well as a population containing around 60% pachytene spermatocytes.     

Synchronization of 9L rat brain tumor cells by centrifugal elutriation

Asynchronous 9L cells were separated into relatively homogeneously-sized populations using centrifugal elutriation with both a conventional collection method and a long collection method. A substantial increase in the homogeneity of the volume distributions and in the degree of synchrony of the separated fractions was obtained using the long collection method. Autoradiographic data indicated that fractions containing ≥97% G₁ cells, ≥80% S cells, and 70–75% G₂ cells could be routinely recovered with this procedure. Recovery in these fractions varied from 5 to 8% of the total number of cells elutriated. The colony forming efficiency (CFE) of cells from fractions representing each phase of the cell cycle was a constant 60–70%, which was comparable to the 60–80% usually found for asynchronous 9L cells. The percentage of cells in the G₁, S, and G₂ phases in the elutriated fractions was more accurately determined from the volume distribution than from computer fits of the DNA histogram obtained from flow cytometry. In general, the degree of synchrony was related to the coefficient of variation (CV) of the volume distributions of the elutriated fractions. The CV was about 14% for all elutriated fractions. When the ≥97% G₁ population was allowed to progress to S and G₂, the CVs were about 17 and 20.2%, respectively. Thus, the best nonperturbing method for obtaining synchronous 9L cells in the S or G₂ phases was direct elutriation with the long collection method.     

An improved method for the isolation of type II and clara cells from mice

Identifying the causal events and temporal aspects of lung cancer development requires the ability to isolate target and nontarget cells for comparative analyses. Current methodology can either isolate only one pure specific cell population from a lung or multiple cell types at lower purity. Previous studies in our laboratory have identified the alveolar type II cell as the progenitor cell for tumor development in the A/J mouse. The purpose of this study was to develop new protocols for the isolation and culture of type II and Clara cells from the mouse lung. Both type II and Clara cells were obtained in high purity using a sequential centrifugal elutriation protocol. In the first elutriation, cell fractions were collected using a Standard chamber. The type II and Clara cell fractions were then elutriated separately (two different separations) using a Sanderson chamber. The final purity of the type II and Clara cell preparations was 73% and 76%, respectively. Colonies of 4 to 20 Clara cells exhibiting epithelial morphology were evident 1 wk after plating in low serum medium. The growth of type II cells required the addition of bronchioalveolar lavage fluid and acidic fibroblast growth factor to the medium. The isolation of viable mouse type II and Clara cells in high purity should facilitate the identification of cell-specific changes in gene expressions or in enzymatic pathways following in vivo or in vitro exposure to environmental carcinogens.     

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 regulations 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 degrees C. Fluctuations in the temperature of the centrifuge produced temperature variations of only 0.3 degrees 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.     

A new method for the preperative and analytical electrophoresis of cells

In this paper, a new method is described for the horizontal electrophoresis of cells on a density cushion under near-isopycnic conditions. When cell sedimentation is minimized, the electrophoresis of red blood cells (RBC) used as model cells within an anti-convective porous matrix (with pores over 300 μm in diameter) was capable of separating a mixture of human and chicken RBC according to their electrophoretic mobilities. Samples taken from the separated RBC bands show over 90% purity for each species. The simultaneous electrophoresis of several RBC samples carried out under identical conditions permitted the use of comparative data based on the electrophoretic mobility of cells which differ in their surface properties. We believe that this relatively simple system, in which cell sedimentation and convection are minimized, has the potential to be modified and adapted for the separation of other cell types/organelles.     

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.     

Separation of cells by velocity sedimentation

A system for fractionating populations of living cells by velocity sedimentation in the earth's gravitational field is described. The cells start in a thin band near the top of a shallow gradient of 3% to 30% fetal calf serum in phosphate buffered saline at 4°C. Cell separation takes place primarily on the basis of size and is approximately independent of cell shape. A sharply-defined upper limit, called the streaming limit, exists for the cell concentration in the starting band beyond which useful cell separations cannot be achieved. This limit, which varies with the type of cell being sedimented, can be significantly increased by proper choice of gradient shape. For sheep erythrocytes (sedimentation velocity of 1.6 mm/hour) it is 1.5 × 10⁷ cells/ml. Measured and calculated sedimentation velocities for sheep erythrocytes are shown to be in agreement. The technique is applied to a suspension of mouse spleen cells and it is shown, using an electronic cell counter and pulse height analyzer, that cells are fractionated according to size across the gradient such that the sedimentation velocity (in mm/hour) approximately equals r²/4 where r is the cell radius in microns. Since cells of differing function also often differ in size, the system appears to have useful biological applications.     

Relationship between cell size, cell cycle and specific recombinant protein productivity

Centrifugal elutriation was used to produce cell cycle enrichedfractions of four commercially relevant recombinant cell lines,chosen to allow for variation in properties due to construct,expression system and parent cell type, from normally growingheterogeneous batch cultures. As these fractions had identicalculture histories and had not been subjected to any insult orstress which was likely to have adversely affected cellularmetabolism, they were ideal for further study of cellularproperties. Specific productivity, cell size and cell cyclestate of replicate elutriated fractions were measured for eachcell line. Results showed that cell size was the major cellulardeterminant of productivity for all cell lines examined. Productformation was not restricted to any particular cell cycle phaseand in all cases, production occurred irrespective of cell cyclephase. Specific productivity was lowest when the majority ofcells in the fraction were G₁, intermediate when themajority of cells in the fraction were S phase and greater whenthe majority of cells in the fraction were in G₂/M. However, the evidence suggests that size is the major cellulardeterminant of productivity; the apparent relationship betweencell cycle and productivity is secondary and can simply beascribed to the increasing size of cells as they progress thoughthe cell cycle. Thus, in addition to cell density and viabilitycell size is the cellular parameter which should be incorporatednot only into mathematical models of recombinant mammalian cellproduction processes but also into process monitoring andcontrol strategies.     

Separation of mouse testis cells by equilibrium density centrifugation in Renografin gradients

Mouse testis cells have been separated by equilibrium density centrifugation in gradients of Renografin. Intact testis cells were not damaged by the separation procedure provided that, following separation, the osmolarity was reduced gradually. The various cell types were identified microscopically and by ³H-thymidine labelling with similar results. The present technique has demonstrated that significant variations in cell density occur during spermatogenesis. Approximately ten-fold enrichments of nearly all testis cell types were achieved by equilibrium density separation of testis cell suspensions. More homogeneous cell populations were prepared by density gradient centrifugation of cell fractions obtained from velocity sedimentation separations. Overall enrichments of spermatogonia, by 29-fold; pachytene spermatocytes, 45-fold; dividing meiotic cells, 170-fold; round spermatids, 30-fold; step 11–13 elongating spermatids, 12-fold; Leydig cells, 70-fold; and cytoplasmic fragments, 55-fold, were obtained. In this study, a method for preparation of cell suspensions was also developed to produce higher yields of spermatogonia and young primary spermatocytes; however, the density distribution of these cells was altered.     

Centrifugal elutriation (counterstreaming centrifugation) of cells

Lindahl first described the separation of cells by velocity sedimentation utilizing a special technique (counterstreaming centrifugation) that was later modified slightly and renamed centrifugal elutriation. Centrifugal elutriation has been applied, with variable degrees of success, to the separation of hemopoietic cells, mouse tumor cells, testicular cells, and a variety of other specialized cells as well as cells in particular phases of the cell cycle. The capacity of the elutriator to separate large numbers of cells is its chief advantage. The purities of the separated cells have not been compared with the purities of cells separated by other methods in most cases; such comparisons would permit more sophisticated comparison of elutriation with other techniques for velocity sedimentation.     

Centrifugal elutriation (counterstreaming centrifugation) of cells.

Lindahl first described the separation of cells by velocity sedimentation utilizing a special technique (counterstreaming centrifugation) that was later modified slightly and renamed centrifugal elutriation. Centrifugal elutriation has been applied, with variable degrees of success, to the separation of hemopoietic cells, mouse tumor cells, testicular cells, and a variety of other specialized cells as well as cells in particular phases of the cell cycle. The capacity of the elutriator to separate large numbers of cells is its chief advantage. The purities of the separated cells have not been compared with the purities of cells separated by other methods in most cases; such comparisons would permit more sophisticated comparison of elutriation with other techniques for velocity sedimentation.     

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.     

Separation of human and animal cells by steric field-flow fractionation

In this work, the feasibility of separating and characterizing cell populations by steric field-flow fractionation (steric FFF) is demonstrated by application to fixed human and avian red cells, fresh blood from several species, and viable HeLa cells. The basis for this work is established by means of a discussion of the role of steric FFF in the broad family of field-flow fractionation techniques. The behavior of steric FFF is then characterized by application to standard polystyrene latex beads and to fixed red blood cells. Studies of these standards and of the other cells noted under various conditions of field strength and flow velocity are used to improve the separation conditions and approach optimization. It is shown that the fixed human and avian red cells can be separated in a time of less than 15 min. In addition, it is shown that HeLa cells maintain their viability after passage through the separation channel.     

Very high density of CHO cells in perfusion by ATF or TFF in WAVE bioreactor™. Part I. Effect of the cell density on the process

High cell density perfusion process of antibody producing CHO cells was developed in disposable WAVE Bioreactor? using external hollow fiber filter as cell separation device. Both “classical” tangential flow filtration (TFF) and alternating tangential flow system (ATF) equipment were used and compared. Consistency of both TFF‐ and ATF‐based cultures was shown at 20–35 × 10⁶ cells/mL density stabilized by cell bleeds. To minimize the nutrients deprivation and by‐product accumulation, a perfusion rate correlated to the cell density was applied. The cells were maintained by cell bleeds at density 0.9–1.3 × 10⁸ cells/mL in growing state and at high viability for more than 2 weeks. Finally, with the present settings, maximal cell densities of 2.14 × 10⁸ cells/mL, achieved for the first time in a wave‐induced bioreactor, and 1.32 × 10⁸ cells/mL were reached using TFF and ATF systems, respectively. Using TFF, the cell density was limited by the membrane capacity for the encountered high viscosity and by the pCO₂ level. Using ATF, the cell density was limited by the vacuum capacity failing to pull the highly viscous fluid. Thus, the TFF system allowed reaching higher cell densities. The TFF inlet pressure was highly correlated to the viscosity leading to the development of a model of this pressure, which is a useful tool for hollow fiber design of TFF and ATF. At very high cell density, the viscosity introduced physical limitations. This led us to recommend cell densities under 1.46 × 10⁸ cell/mL based on the analysis of the theoretical distance between the cells for the present cell line. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:754–767, 2013     

Multiple subphases of DNA repair and poly (ADP-ribose) synthesis in Chinese hamster ovary (CHO-K1) cells

The two types of DNA synthesis as well as poly(ADP-ribose) biosynthesis were measured simultaneously in synchronized intact populations of CHO cells throughout the duration of S phase. Naturally occurring DNA fragmentation was detected by random primed oligonucleotide synthesis (ROPS assay). Fractions of synchronous cell populations were obtained by counterflow centrifugal elutriation. By gradually increasing the resolution of centrifugal elutriation multiple non-overlapping repair and replication peaks were obtained. The elutriation profile of DNA repair peaks corresponded to the DNA fragmentation pattern measured by ROPS assay. The number and position of poly(ADP-ribose) peaks during S phase resembled those seen in the DNA replication profile. Our results indicate that PAR synthesis is coupled to DNA replication serving the purpose of genomic stability.     

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.     

Breakdown of middle lamella pectin by ●OH during rapid abscission in Azolla

Azolla, a small water fern, abscises its roots and branches within 30 min upon treatment with various stresses. This study was conducted to test whether, in the rapid abscission that occurs in Azolla, breakdown of wall components of abscission zone cells by ^●OH is involved. Experimentally generated ^●OH caused the rapid separation of abscission zone cells from detached roots and the rapid shedding of roots from whole plants. Electron microscopic observations revealed that ^●OH rapidly and selectively dissolved a well‐developed middle lamella between abscission zone cells and resultantly caused rapid cell separation and shedding. Treatment of abscission zones of Impatiens leaf petiole with ^●OH also accelerated the separation of abscission zone cells. However, compared with that of Azolla roots, accelerative effects in Impatiens were weak. A large amount of ^●OH was cytochemically detected in abscission zone cells both of Azolla roots and of Impatiens leaf petioles. These results suggest that ^●OH is involved in the cell separation process not only in the rapid abscission in Azolla but also in the abscission of Impatiens. However, for rapid abscission to occur, a well‐developed middle lamella, a unique structure, which is sensitive to the attack of ^●OH, might be needed.