Effect of growth factors and antigen on hybridoma cell culture dynamics

The cell growth and monoclonal antibody production kinetics of hybridoma cell cultures continuously exposed to growth factors and the cognate antigen were investigated. The growth factors were the epidermal growth factor, fibroblast growth factor, and interleukin-2, whereas the antigen was the trinitrophenyl group conjugated to a carrier protein. The cultures were carried out in a protein-free medium in batch operation. During the entire cultivation period there was continuously available free, antibody-unbound antigen to interact with the cells. The produced antibody was measured with an ELISA after it was released from the antigen-protein conjugate by competitive elution with non-protein-conjugated antigen. Cultures with growth factors and without antigen increased the total antibody produced by up to 30%, whereas cell growth remained unaffacted. Soluble antigen-protein conjugates had no effect on the hybridoma cultures. In contrast, immobilized antigen-protein on sepharose beads in cultures with growth factors induced significant changes. Total antibody produced was higher by up to 40%. More importantly, the specific antibody production shifted from a growth-phase-independent to a growth-phase-dependent profile, with approximately twice as much specific antibody production during the late growth-early stationary phase relative to constant specific antibody production in the antigen-free, factor-free culture. The culture changes induced by the presence of immobilized antigen and growth factors were reversed when the antigen and the growth factors were removed from the cells' environment. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 357-364, 1997.     

Enhancement of monoclonal antibody production by immobilized hybridoma cell culture with hyperosmolar medium

To determine the effect of hyperosmotic stress on the monoclonal antibody (MAb) production by calcium-alginate-immobilized S3H5/gamma2bA2 hybridoma cells, the osmolalities of medium in the MAb production stage were varied through the addition of NaCI. The specific MAb productivity (q(MAb)) of immobilized cells exposed to abrupt hyperosmotic stress (398 mOsm/kg) was increased by 55% when compared with that of immobilized cells in the control culture (286 mOsm/kg). Furthermore, this enhancement of q(MAb) was not transient. Abrupt increase in osmolality, however, inhibited cell growth, resulting in no increase in volumetric MAb productivity (r(MAb)). On the other hand, gradual increase in osmolality allowed further cell growth while maintaining the enhanced q(MAb) immobilized cells. The q(MAb) immobilized cells at 395 mOsm/kg was 0.661 +/- 0.019 mug/10(6) cells/h, which is almost identical to that of immobilized cells exposed to abrupt osmotic stress. Accordingly, the r(MAb) was increased by ca. 40% when compared with that in the control immobilized cell culture. This enhancement in i(MAb) of immobilized S3H5/gamma2bA2 hybridoma cells by applying gradual osmotic stress suggests the potential of using hyperosmolar medium in other perfusion culture systems for improved MAb production. (c) 1995 John Wiley & Sons, Inc.     

The production of monoclonal antibody in growth-arrested hybridomas cultivated in suspension and immobilized modes.

The effects of the microenvironment and the nature of the limiting nutrient on culture viability and overall MAb productivity were explored using a hybridoma cell line which characteristically produces MAb in the stationary phase. A direct comparison was made of the changes in the metabolic profiles of suspension and PEG-alginate immobilized (0.8 mm beads) batch cultures upon entry into the stationary phase. The shifts in glucose, glutamine, and amino acid metabolism upon entry into the stationary phase were similar for both microenvironments. While the utilization of most nutrients in the stationary phase decreased to below 20% of that in the growth phase, antibody production was not dramatically affected. The immobilized culture did exhibit a 1.5-fold increase in the specific antibody rate over the suspension culture in both the growth and stationary phases. The role of limiting nutrient on MAb production and cell viability was assessed by artificially depleting a specific nutrient to 1% of its control concentration. An exponentially growing population of HB121 cells exposed to these various depletions responded with dramatically different viability profiles and MAb production kinetics. All depletions resulted in growth-arrested cultures and nongrowth-associated MAb production. Depletions in energy sources (glucose, glutamine) or essential amino acids (isoleucine) resulted in either poor viability or low antibody productivity. A phosphate or serum depletion maintained antibody production over at least a six day period with each resulting in a 3-fold higher antibody production rate than in growing batch cultures. These results were translated to a high-density perfusion culture of immobilized cells in the growth-arrested state with continued MAb expression for 20 days at a specific rate equal to that observed in the phosphate- and serum-depleted batch cultures.     

On-line immunoanalysis of monoclonal antibodies during a continuous culture of hybridoma cells

The monoclonal-antibody production of an immobilized hybridoma cell line cultivated in a fluidized-bed reactor was monitored on-line for nearly 900 h. The monoclonal antibody concentration was determined by an immuno affinity-chromatography method (ABICAP). Antibodies directed against the product, e.g. IgG, were immobilized on a micro-porous gel and packed in small columns. After all IgG present in the sample was bound to the immobilized antibodies, unbound proteins were removed by rinsing the column. Elution of the bound antibodies followed and the antibodies were determined by fluorescence. The analytical procedure was automated with a robotic device to enable on-line measurements. The correlation between the on-line determined data and antibody concentrations measured by HPLC was linear. A sampling system was constructed, which was based on a pneumatically actuated in-line membrane valve integrated into the circulation loop of the reactor. Separation of the cells from the sample stream was achieved by a depth filter made of glass-fibre, situated outside the reactor. Rapid obstruction of the filter by cells or cell debris and contamination of the sample system was avoided by intermittent rinsing of the sample system with a chemical solution. The intermittent rinsing of the filter, which had a surface of 4.8 cm², resulted in an operational capacity of up to 40 samples (1.0 l total sample volume). Both the sampling system and the analytical device functioned without failure during this long-term culture. The culture temperature was varied between 34 and 40 °C. Raising the temperature from 34 up to 37 °C resulted in a simultaneous increase of growth and specific antibody production rate. Specific metabolic rates of glucose, lactate, glutamine and ammonium stayed constant in this temperature range. A further enhancement of temperature up to 40 °C had a negative effect on the growth rate, whereas the specific monoclonal antibody production rate showed a small increase. The other specific metabolic rates also increased in the temperature range between 38 to 40 °C. This revised version was published online in July 2006 with corrections to the Cover Date.     

Evaluation of CNBr, FMP and hydrazide resins for immunoaffinity purification of factor IX.

The American Red Cross has developed an immunoaffinity chromatography method to purify human coagulation Factor IX to high levels of purity for therapeutic treatment of hemophilia B. The resin currently used in this process is Sepharose CL2B, a cross-linked 2% agarose, which is activated with cyanogen bromide to immobilize an anti-Factor IX monoclonal antibody. This study evaluated two alternative resins and coupling chemistries, a synthetic polymer bead activated by 2-fluoro-1-methyl-pyridinium toluene 4-sulfonate (FMP) and a cross-linked 2% agarose bead with free hydrazide groups for site-specific coupling. The cyanogen bromide and FMP chemistries immobilize the monoclonal antibody in a random orientation. In hydrazide coupling, the monoclonal antibody is immobilized by the non-antigen-binding part of the molecule which, theoretically, should increase the amount of immobilized monoclonal antibody able to bind antigen. To examine this, the capacity of the resins to bind Factor IX and the purity and recovery of Factor IX eluted from the resins were measured. The FMP-activated resin exhibited the lowest capacity, binding only 2% of the Factor IX feed. Sepharose CL2B bound 87% of the loaded protein, while the hydrazide resin bound 43%. These results suggest that (a) hydrazide activation may be insufficient to orient monoclonal antibody and (b) other factors such as steric hindrances and diffusional resistances during immobilization may be important. Neither of the other resins tested demonstrated improved performance compared with cyanogen bromide-activated Sepharose CL2B for the immunoaffinity purification of Factor IX.     

Effects of high cell density on growth-associated monoclonal antibody production by hybridoma T0405 cells immobilized in macroporous cellulose carriers

Relationship between monoclonal antibody (MAb) productivity and growth rate, and effects of high cell density on MAb production of hybridoma T0405 cells immobilized in macroporous cellulose carriers were investigated in continuous and batch cultures. The results showing, that the specific MAb production rate increased with increasing specific growth rate in both suspended and immobilized continuous cultures indicate a positively growth-associated relationship between MAb productivity and growth rate. Moreover, the specific production rate was higher in the immobilized cell culture than that in suspended one at all dilution rates. In order to clarify these phenomena, MAb mRNA expression and cell cycle distribution were investigated in batch cultures with immobilized cells and suspended cells. RT-PCR was used for observation of MAb mRNA expression and a two-color bromode-oxyuridine (BrdU)/propidium iodide (PI) flow cytometry method for determination of cell cycle distribution. The results revealed that MAb mRNA expression reached the peak during the exponential growth phase, suggest a positively growth-associated MAb production. And the immobilized cells continued the MAb mRNA expression until dead phase, which was longer than that in suspended cells. The cell cycle distribution patterns were observed almost the same for both immobilized and suspended cells. Such results may imply that a high cell density state has positive influence on the mRNA expression and on growth-associated MAb productivity of T0405 cells.     

Comparison of culture methods for human-human hybridomas secreting anti-HBsAg human monoclonal antibodies

Human-human hybridomas which secrete a human monoclonal antibody (h-MoAb) against hepatitis B virus surface antigen showed growth associated production kinetics. The rate of h-MoAb production rapidly decreased after cell growth was arrested in a perfusion culture, even if the perfusion rate was increased. A continuous suspended-perfusion culture, in which both culture broth and culture supernatant are continuously harvested and the same volume of fresh medium is continuously fed into the reactor, was developed to maintain continuous growing conditions during cultivation. In this culture system, the production of h-MoAb continued for more than 50 days with an average productivity of 5.0 mg/l of working volume/day. A semicontinuous immobilized-perfusion culture in which parts of the cells are repeatedly removed from the immobilized reactor was another useful technique for the long term cultivation of these h-h hybridomas. As an average h-MoAb production rate, 62 mg/l of immobilized-bed volume/day was achieved for 65 days of cultivation using a ceramic matrix reactor, and 327 mg/l/day was achieved over 47 days of cultivation using a hollow fiber reactor equipped with Cultureflo M^TM Thus, the antibody productivity per reactor volume per day by the semicontinuous immobilized-perfusion culture was much higher than that of the continuous perfusion culture in an agitation reactor.     

Production of monoclonal antibody using free-suspended and immobilized hybridoma cells: Effect of serum

The effect of serum on cell growth and monoclonal antibody (MAb) productivity was studied in a repeated fedbatch mode using both free-suspended and immobilized S3H5/gamma2bA2 hybridoma cells. In the suspension culture, serum influenced the cell growth rate but not the specific MAb productivity. The average specific growth rate of the suspension culture in medium containing 10% serum was approximately 0.99 +/- 0.12 day(-1) (+/-standard deviation), while that in medium containing 1% serum was approximately 0.73 +/- 0.12 day(-1). The specific MAb productivity was almost constant at 3.69 +/- 0.57 mug/10(6) cells/day irrespective of serum concentration reached a maximum at ca. 1.8 x 10(6) cells/mL of medium in 10% serum medium, and the cell concentration was gradually reduced to 1%. The specific MAb productivity of the immobilized cells was more than three times higher than that of the free-suspended cells. The amount of serum in the medium did not influence the specific MAb production rate of the immobilized cells. The maintenance of high cell concentration and the enhanced specific MAb productivity of the immobilized cell culture resulted in a higher volumetric MAb productivity. In addition, MAb yield in the immobilized cell culture with medium containing 1% serum was 2.2 mg/mL of serum, which was approximately three times higher than that in the suspension culture.     

Enzymatic splitting of antibodies bound to immobilized antigen as a means of Fab fragments preparation]

A method of Fab fragments preparation by enzymatic splitting of antibodies bound to specific antigen immobilized on an insoluble support is described. The complex of rat muscle glyceraldehyde-3-phosphate dehydrogenase (GAPD), immobilized on Sepharose 4B, with anti-rat GAPD rabbit antibodies was digested with papain. The antigen was inaccessible to proteolysis under conditions employed. After 4 hrs of incubation with papain the antibody was completely split into non-precipitating fragments. The products of proteolysis not bound to Sepharose, were eluted with 0.1 M givcine buffer pH 2.5, and shown to correspond to Fab fragments.     

New immobilization method of mammalian cells using alginate and polyacrylate

Mouse-mouse hybridoma cells were immobilized in polyacrylate-alginate gels. The immobilized hybridoma cells were cultured semi-continuously using a fluidized bed reactor, and allowed continuous antibody production without any gel destruction for one month. It has been proved that the polyacrylate-alginate gels were tolerant against physical stress. The composition of the gels suitable for cell growth and antibody production was given as follows; viscosity of alginate at 1% solution: 60–100 cP, alginate concentration: 0.8%, and polyacrylate concentration: 0.2%. In the semi-continuous culture using gels prepared under suitable conditions, the viable cell number was estimated as 2.5×10⁷ cells/ml-gel, and the antibody production rate was 2.2 mg/ml-gel/d, at maximum.     

Expression of a human anti-rabies virus monoclonal antibody in tobacco cell culture

A Nicotiana tabacum cv. Xanthi cell culture was initiated from a transgenic plant expressing a human anti-rabies virus monoclonal antibody. Within 3 months, plant cell suspension cultures were established and recombinant protein expression was examined. The antibody was stably produced during culture growth. ELISA, protein G purification, Western blotting, and neutralization assay confirmed that the antibody was fully processed, with association of light and heavy-chains, and that it was able to bind and neutralize rabies virus. Quantification of antibody production in plant cell suspension culture revealed 30 microg/g of cell dry weight for the highest-producing culture (0.5 mg/L), 3 times higher than from the original transgenic plant. The same production level was observed 3 months after cell culture initiation. Plant cell suspension cultures were successfully grown in a new disposable plastic bioreactor, with a growth rate and production level similar to that of cultures in Erlenmeyer flasks.     

An online, non-invasive fluorescence probe for immobilized cell culture process development

An online, analytical technology was developed that utilized fluorescence to detect cells during an immobilized cell culture process. Chinese hamster ovary (CHO) cells that produced monoclonal antibodies (mAb) were transfected to express green fluorescent protein (GFP), and stable, fluorescence-positive cells were obtained by fluorescence-activated cell sorting (FACS). The immobilized cell culture process was then used to test the effects of sodium butyrate on cells. In this study, cells were cultured in porous, fibrous matrices that were placed in spinner flasks. A lab-scale, perfusion bioreactor with computer-controlled, online fluorescence sensors that continuously detected GFP fluorescence and quantified cell growth was utilized. In addition, the level of GFP fluorescence was used to predict mAb production in the culture without sampling for cell counting and protein analysis. Thus, non-invasive, fluorescence detection of cells provided a rapid, reliable and robust approach for developing an immobilized cell culture process.     

Production of polygalacturonase from <Emphasis Type="Italic">Coriolus versicolor</Emphasis> grown on tomato pomace and its chromatographic behaviour on immobilized metal chelates

Tomato pomace and pectin were used as the sole carbon sources for the production of polygalacturonase from a strain of Coriolus versicolor in submerged culture. The culture of C. versicolor grown on tomato pomace exhibited a peak of polygalacturonase activity (1,427 U/l) on the third day of culture with a specific activity of 14.5 U/mg protein. The production of polygalacturonase by C. versicolor grown on pectin as a sole carbon source increased with the time of cultivation, reaching a maximum activity of 3,207 U/l of fermentation broth with a specific activity of 248 U/mg protein. The levels of different isoenzymes of polygalacturonase produced during the culture growth were analysed by native PAGE. Differential chromatographic behaviour of lignocellulosic enzymes produced by C. versicolor (i.e. polygalacturonase, xylanase and laccase) was studied on immobilized metal chelates. The effect of ligand concentration, pH, the length of spacer arm and the nature of metal ion were studied for enzyme adsorption on immobilized metal affinity chromatography (IMAC). The adsorption of these lignocellulosic enzymes onto immobilized metal chelates was pH-dependent since an increase in protein adsorption was observed as the pH was increased from 6.0 to 8.0. The adsorption of polygalacturonase as well as other enzymes to immobilized metal chelates was due to coordination of histidine residues which are available at the protein surface since the presence of imidazole in the equilibration buffer abolished the adsorption of the enzyme to immobilized metal chelates. A one-step purification of polygalacturonase from C. versicolor was devised by using a column of Sepharose 6B-EPI 30-IDA-Cu(II) and purified enzyme exhibited a specific activity of about 150 U/mg protein, final recovery of enzyme activity of 100% and a purification factor of about 10. The use of short spacer arm and the presence of imidazole in equilibration buffer exhibited a higher selectivity for purification of polygalacturonase on this column with a high purification factor. The purified enzyme preparation was analysed by SDS-PAGE as well as by "in situ" detection of enzyme activity.     

Hepatitis B surface antigen (HBsAg) expression in plant cell culture: Kinetics of antigen accumulation in batch culture and its intracellular form

The production of edible vaccines in transgenic plants and plant cell culture may be improved through a better understanding of antigen processing and assembly. The hepatitis B surface antigen (HBsAg) was chosen for study because it undergoes substantial and complex post-translational modifications, which are necessary for its immunogenicity. This antigen was expressed in soybean (Glycine max L. Merr. cv Williams 82) and tobacco NT1 (Nicotiana tabacum L.) cell suspension cultures, and HBsAg production in batch culture was characterized. The plant-derived antigen consisted predominantly of disulfide cross-linked HBsAg protein (p24(s)) dimers, which were all membrane associated. Similar to yeast, the plant-expressed HBsAg was retained intracellularly. The maximal HBsAg titers were obtained with soybean suspension cultures (20-22 mg/L) with titers in tobacco cultures being approximately 10-fold lower. For soybean cells, electron microscopy and immunolocalization demonstrated that all the HBsAg was localized to the endoplasmic reticulum (ER) and provoked dilation and proliferation of the ER network. Sucrose gradient analysis of crude extracts showed that HBsAg had a complex size distribution uncharacteristic of the antigen's normal structure of uniform 22-nm virus-like particles. The extent of authentic epitope formation was assessed by comparing total p24(s) synthesized to that reactive by polyclonal and monoclonal immunoassays. Depending on culture age, between 40% and 100% of total p24(s) was polyclonal antibody reactive whereas between 6% and 37% was recognized by a commercial monoclonal antibody assay. Possible strategies to increase HBsAg production and improve post-translational processing are discussed.     

Immunoaffinity chromatography using electroelution.

Immunoaffinity chromatography and electroelution of protein from solid-phase matrices are two powerful tools often used to purify proteins. In this study, we combined these two techniques and found that antigen was effectively recovered from immunoaffinity resins by electroelution. Yields ranged from 90.5% to 62.8%, with a mean of 74.0 +/- 7.4% (mean +/- standard deviation). A major portion of the eluate, 79.4 +/- 13.1%, was concentrated in a volume of 100 microliters and 94.0 +/- 2.0% was recovered in 200 microliters, even when 1 ml of resin was used. Electroelution had no major effect on the electrophoretic mobility of the antigen. Two distinct antigens, a relatively hydrophilic 230-kDa protein and a hydrophobic 28-kDa protein were successfully electroeluted. In addition two types of immunoaffinity resins, monoclonal antibody covalently linked to CNBr-activated Sepharose or immobilized protein A, were found to be compatible with this method.     

Ethanol production by nitrogen-deficient yeast cells immobilized in a hollow-fiber membrane bioreactor

Summary Cells ofSaccharomyces cerevisiae ATCC 4126, immobilized within the macroporous walls of asymmetric hollow-fiber membranes, were alternately perfused with 10% glucose complex medium and with 10% glucose defined medium which was deficient in nitrogen. Using complex growth medium, ethanol productivities during the initial 10 h of culture attained a maximum level of 133 g/l-h based on the total fiber volume (3% ethanol). Productivities during nitrogen deficiency stabilized at 10 g/l-h (0.5 ethanol). In subsequent growth phases, ethanol production rates increased to levels 40–70% of initial growth-phase values, but the ability to regenerate the fermentation activity decreased with culture age. During nitrogen deficiency, the fermentation efficiency declined with a concomitant reduction in the total protein concentration of immobilized cells within the hollow-fiber membranes. The molar ratio of acetaldehyde to ethanol increased seven-fold during nitrogen deficiency, indicating that the overall decline in glycolytic activity was accompanied by preferential reduction in alcohol dehydrogenase activity. The molar ratio of glycerol to ethanol increased two-fold during nitrogen deficiency, and large lipid-like droplets accumulated within the nitrogen-deficient cells. In addition to these findings, we conclude that current hollow-fiber membrane reactors should be limited to cell cultures having low growth rates, low O₂ requirements, and low CO₂ production rates.     

Overexpression of bcl-2 inhibits sodium butyrate-induced apoptosis in Chinese hamster ovary cells resulting in enhanced humanized antibody production

Sodium butyrate (NaBu) can enhance the expression of genes from some of the mammalian promoters including cytomegalovirus (CMV) and simian virus 40 (SV40), but it can also inhibit cell growth and induce cellular apoptosis. Thus, the beneficial effect of using a higher concentration of NaBu on a foreign protein expression is compromised by its cytotoxic effect on cell growth. To overcome this cytotoxic effect of NaBu, a survival protein, human Bcl-2, was overexpressed in recombinant Chinese hamster ovary (CHO) cells (SH2-0.32), producing a humanized antibody directed against the S surface antigen of hepatitis B virus. When batch cultures of both control cells transfected with bcl-2-deficient plasmid (SH2-0.32-Deltabcl-2) and cells transfected with bcl-2 expression plasmid (14C6-bcl-2) were performed in the absence of NaBu, both cells showed similar profiles of cell viability and antibody production. Compared with the SH2-0.32-Deltabcl-2 culture, under the condition of NaBu addition at the exponential growth phase, overexpression of the bcl-2 gene considerably suppressed the NaBu-induced apoptosis of 14C6-bcl-2 by inhibiting caspase 3 activity and extending culture longevity by >2 days. As a result, the final antibody concentration of 14C6-bcl-2 culture was twofold higher than that of SH2-0.32-Deltabcl-2 culture in the presence of NaBu and threefold higher than that of SH2-0.32-Deltabcl-2 and 14C6-bcl-2 cultures in the absence of NaBu.     

Comparison of specific rates of hybridoma growth and metabolism in batch and continuous cultures

For the mouse hybridoma cell line VO 208, kinetics of growth, consumption of glucose and glutamine, and production of lactate, ammonia and antibodies were compared in batch and continuous cultures. At a given specific growth rate, different metabolic activities were observed: a 40% lower glucose and glutamine consumption rate, but a 70% higher antibody production rate in continuous than in batch culture. Much higher metabolic rates were also measured during the initial lag phase of the batch culture. When representing the variation of the specific antibody production rate as a function of the specific growth rate, there was a positive association between growth and antibody production in the batch culture, but a negative association during the transient phase of the continuous culture. The kinetic differences between cellular metabolism in batch and continuous cultures may be result of modifications in the physiology and metabolism of cells which, in continuous cultures, were extensively exposed to glucose limitations.Institut National Polytechnique de Lorraine, ENSAIA BP 172, 2 avenue de la forêt de Haye, 54505, Vandoeuvre Cedex France     

Enhanced monoclonal antibody production in hybridoma cells by LPS and Anti-mIgG

This paper reports on a methodology for increasing proliferation and monoclonal antibody (mAb) production in hybridoma cultures. The 55-6 murine B cell hybridoma line (CD40 and CD19-deficient expression) was treated with increasing concentrations of lipopolysaccharide (LPS). Expression of CD69, CD40, and CD19 surface antigens on 55-6 cells did not show significant changes from untreated cells. The specific growth rate decreased at higher concentrations of LPS, but the monoclonal antibody production rate was highest at the highest LPS concentration assayed. These data are in agreement with the lowest growth rate found at this concentration of LPS. Furthermore, cells were cultured with anti-mouse surface immunoglobulin G antibody (anti-mIgG) plus LPS to find out whether LPS-derived signals and anti-mIgG stimuli are synergistic. CD69, CD40, and CD19 expression was greater than for either untreated cells (control culture) or cells stimulated with LPS alone. Moreover, LPS stimulation in combination with anti-mIgG enhanced both the growth rate and IgG2a production over the control culture and cells stimulated with LPS alone. Maximum antibody concentration increased almost 500% compared to the control and about 100% with respect to culture stimulated with LPS alone. The maximum specific IgG2a production rate was about 300% higher than in the control culture and about 30% higher than in culture stimulated only with LPS.     

Preparation and characterization of an 125I-labeled Sendai virus ligand

In an attempt to prepare a radioviral ligand that was effective both as an antigen in binding to antibody and as a ligand that effectively binds to receptor-bearing cells, inactivated Sendai virus was adsorbed to immobilized fetuin at 4°C and recovered by temperature elevation at 37°C. The eluted virus was iodinated using the chloramine-T procedure and free iodine and labeled virus were separated on a Sepharose 4B column. Radiolabeted virus contained 1000 to 5000 cpm per hemagglutination unit and over 90% of the counts were sedimented following high-speed centrifugation. Radioviral ligand was 80% reactive with immobilized Sendai virus antibody, 70% reactive with sheep red blood cells,and 1% reactive with receptor-negative horse red blood cells. Pretreatment of the cells with neuraminidase completely inhibited the virus binding reaction. The reaction with receptor-bearing cells was competitively inhibited by unlabeled Sendai virus, but not by murine leukemia virus or T-2 coliphage. Radioviral ligand binding to human lymphoblastic cell line CCL-119 was a saturable reaction, a result that demonstrates the absence of virus-virus aggregates. The preparation of an effective cell-reactive radioviral ligand was dependent on the initial purification from immobilized receptor-containing proteins.