Effect of serum concentration on hybridoma viable cell density and production of monoclonal antibodies in CSTRs and on shear sensitivity in air-lift loop reactors

The death rate of hybridoma cells, grown in a continuous culture, has been studied in a small air-lift loop reactor as a function of reactor height and injected gas flow rate. The first-order death-rate constant was found to be proportional to the reciprocal height and to the gas flow rate, in accordance with the hypothetical killing volume model for insect cells in bubble columns. Furthermore, the effect of the serum concentration on viable cell concentration and cell productivity has been investigated in a continuous culture. A serum component became growth limiting when the serum concentration was decreased from 2% to 1%. No effect of the serum concentration on specific cell productivity could be measured. Samples from this culture were also studied in the air-lift loop reactor to determine the effect of serum concentration on the shear sensitivity. The cells' shear sensitivity increased with decreasing serum concentration. The protective effect of serum was found to be physical as well as physiological.     

Effect of serum concentration on production of monoclonal antibodies and on shear sensitivity of a hybridoma

The effect of serum content of culture medium on the specific production rate of monoclonal antibodies (Mab's) and on shear sensitivity has been studied with hybridoma's, cultured in a continuous stirred tank reactor (CSTR). No decrease in specific Mab-production was found when the serum concentration was reduced from 10 to 2.5%, while steady state cell concentrations were hardly affected as well. In contrast the cell death rate in a bubble column strongly increased when the serum concentration was lowered, which could be ascribed to a reduced physical protective effect by the serum.List of Symbols k _d s^–1 death-rate constant - k _g s^–1 growth-rate constant - D m diameter of bubble column - d m diameter of air bubble - H m height of bubble column - X m³ hypothetical killing volume - X (m³/m³) specific hypothetical killing volume - F m³/s volumetric air-flow rate - C cells/m³ number of viable cells - C₀ cells/m³ number of viable cells at t=0 - t s time     

Isolation and purification of protease from human placenta by foam fractionation

The effect of operating parameters like pH, protein concentration, column geometry, and gas flow rate on the separation efficiency of proteolytic enzymes from crude human placental homogenate has been studied in a batch foam column. Purification has been found to be optimum at pH 8.0, close to the isoelectric pH, at which the surface adsorption of the protein on the foam bubbles is maximum. Both purification and recovery varied significantly with total protein concentration. Stable bubble formation was hindered at lower protein concentrations, while extraneous proteins rather than the protease were preferentially adsorbed at higher protein concentrations, decreasing the purification efficiency. Column diameter and column height should be optimized for any specific feed protein concentration and gas flow rate. However, the enrichment ratio was found to decrease with the increase in flow rate. The results indicate that foam fractionation is an effective separation process for recovering valuable biochemicals from biological materials.     

The protective effect of serum against hydrodynamic damage of hybridoma cells in agitated and surface-aerated bioreactors.

The effect of serum on the growth rate and metabolism of CRL-8018 hybridoma cells in an agitated, surface-aerated bioreactor was examined. In the employed well-controlled bioreactors at high agitation rates, hybridoma cells in medium containing 1% fetal bovine serum rapidly die in the presence of a vortex with accompanying gas-bubble entrainment, whereas non-agitated control cultures grow normally in medium containing 1% serum. Serum levels greater than 5% counteract the detrimental hydrodynamic effects due to agitation and bubble entrainment. The protective effect is present after short-term (less than 1 h) exposure to 10% serum concentration, suggesting a protection mechanism which is, at least in part, of a physical nature. The apparent cell yields on glucose, lactate, and glutamine decreased with decreasing growth rate due to low serum concentrations. The results are incorporated into a simple model in which the apparent growth rate is the sum of an invariable growth rate and a changing death rate.     

Improved production of phenylethanoid glycosides by Cistanche deserticola cells cultured in an internal loop airlift bioreactor with sifter riser

An internal loop airlift bioreactor with sifter riser (ILABSR) was composed of a bubble column and a draught-tube rolled with 40-mesh sifter that placed 5 cm above the bottom at the center of the column. A 2 L ILABSR was used for the suspension cultivation of Cistanche deserticola cells and its performance was compared with shake flask culture and a bubble column. Under the optimum culture conditions with the air flowrate of 0.075 m³/h and the inoculation size of 4.7%, about one-fifth cells were attached to the sifter draught-tube. PeG content in these cells was 16.3%, which was 104% higher than that of suspension cells. The production of phenylethanoid glycosides reached 0.85 g/L, which was 102 and 4% higher than those cultured in a 2 L bubble column and shake flasks respectively under their optimal culture conditions.     

Improved medium for clonal growth of human diploid fibroblasts at low concentrations of serum protein.

A new medium (MCDB 104) has been developed which will support clonal growth of WI-38 cells at concentrations of serum protein as low as 25 micrograms per ml (equivalent to 0.05% serum). The principal factors responsible for reduction of the protein requirement are: (a) adjustment of all nutrient concentrations in medium F12 to experimentally determined optimum values for WI-38 cells; (b) supplementation with trace elements; (c) replacement of hypoxanthine and folic acid with adenine and folinic acid; and (d) coating of the culture surface with polylysine. Individually, many of these modifications exert only a small effect on cellular growth at reduced protein concentrations, but collectively their effect has been very substantial. Other strains of fibroblast-like human diploid cells from amniotic fluid, fetal lung and newborn foreskin also will grow at reduced concentrations of serum protein in the new medium.     

Foam fractionation of globular proteins

Foam fractionation of bovine serum albumin (BSA) was studied as a model system for potato wastewater. The effects of feed concentration, superficial gas velocity, feed flow rate, bubble size, pH, and ionic strength on the enrichment and recovery of BSA were investigated in a single-stage continuous foam fractionation column. Enrichments ranged from 1.5 to 6.0 and recoveries from 5 to 85%. The feed concentrations were varied from 0.01 to 0.2 wt %, and enrichments were found to increase with lower feed concentrations. Enrichments also increased with lower superficial gas velocities and larger bubble sizes. At sufficiently low feed flow rates, enrichment was found to increase with an increase in the flow rate, eventually becoming insensitive to the feed flow rate at higher values. The pH was varied from 3.5 to 7.0 and ionic strength from 0.001M to 0.2M. The effects of pH and ionic strength were found to be coupled with bubble size. A minimum bubble size was found at pH 4.8, the isoelectric point of BSA, resulting in a minimum in the enrichment. Bubble size, and thus enrichment, was found to increase as the ionic strength decreased from 0.2M to 0.01M. Previous models(1,2) for the hydrodynamics of foam column were extended for a singlestage continuous foam fractionation column for the prediction of enrichment and recovery. The model assumed adsorption equilibrium, infinite surface viscosity, and bubbles of the same size. Though coalescence was formally accounted for in the model by considering bubble size as a function of foam height, calculations for the experimental runs were performed only for the case of no coalescence. Quantitative predictions of enrichment and recovery could not be made with a single representative bubble size because of the broad inlet bubble size distribution as well as broadening of the distribution as a result of coalescence. The experimental enrichments were higher and recoveries were lower than the model predictions, the discrepancy being more pronounced at lower feed concentrations because of increased coalescence. The higher enrichments are due to the predominant effect of internal reflux as a result of coalescence whereas the lower recoveries are a result of detrimental effects of broadening bubble size distributions.     

Growth of Artemisia annua hairy roots in liquid- and gas-phase reactors

Artemisia annua hairy roots were grown in liquid-phase bubble column and gas-phase nutrient mist reactors. In most cases the bubble column reactor accumulated more biomass than the mist reactor; the highest final biomass concentrations observed were 15.3 g DW/L in the bubble column reactor and 14.4 g DW/L in the mist reactor. Further analysis showed that the average specific growth rate in the mist reactors was essentially constant and independent of the biomass concentration at the beginning of the mist mode. In contrast, at low packing densities the average growth rate in the bubble column reactors was higher than in the mist reactors, decreasing to comparable rates at high packing densities. Finally, an aerosol deposition model was used to compare the volume of medium captured by the root bed in the mist reactor to the volume of medium required to maintain a specified growth rate. The results suggest that under the current operating conditions, lower growth rates in the mist reactor may be due to insufficient nutrient availability.     

Improvement of Panax notoginseng cell culture for production of ginseng saponin and polysaccharide by high density cultivation in pneumatically agitated bioreactors

A Panax notoginseng cell culture was successfully scaled up from shake flask to 1.0-L bubble column reactor and concentric-tube airlift reactor. High-density bioreactor batch cultivation was carried out using a modified MS medium. The maximum cell density in batch cultures reached 20.1, 21.0 and 24.1 g/L in the shake flask, bubble column and airlift reactors, respectively, and their corresponding biomass productivity was 950, 1140 and 1350 mg/(L x d) for each. The productivity of ginseng saponin was 70, 96 and 99 mg/(L x d) in the flask, bubble column and airlift reactors, respectively; and the polysaccharide productivity reached 104, 119 and 151 mg/(L x d) for each. Furthermore, a fed-batch cultivation strategy was developed on the basis of specific oxygen uptake rate (SOUR), i.e., sucrose feeding before a sharp decrease of SOUR, and the highest cell density of 29.7 g/L was successfully achieved in the airlift bioreactor on day 17 with a very high biomass productivity of 1520 mg/(L x d). The concentrations of ginseng saponin and polysaccharide reached about 2.1 and 3.0 g/L, respectively, and their productivity was 106 (saponin) and 158 mg/(L x d) (polysaccharide). This work successfully demonstrated the high-density bioreactor cultivation of P. notoginseng cells in pneumatically agitated bioreactors and the reproduction of the shake flask culture results in bioreactors. The cell density, biomass productivity, production titer and productivity of both ginseng saponin and polysaccharide obtained here were the highest that have been reported on a reactor scale for all the ginseng species.     

Shear rate and microturbulence effects on the synthesis of proteases by Jacaratia mexicana cells cultured in a bubble column, airlift, and stirred tank bioreactors

Cysteine proteases from Jacaratia mexicana, an endemic Mexican plant, could compete in industrial applications with papain. Currently the only way to obtain these proteases is by extracting them from the wild plant. An alternative source of these enzymes is by J. mexicana suspension culture. In this work, this culture was carried out in airlift, bubble column and stirred tank bioreactors, and the effects of shear rate and microturbulence on cell growth, protein accumulation and proteolytic activity were determined. The shear rates in the stirred tank, bubble column and airlift bioreactors were 274 1/s, 13 1/s and 36 1/s respectively, and microturbulences (symbolized by λ, in units of μm) were 46, 79, and 77 μm, respectively. Protein levels and proteolytic activity were linearly correlated with both shear rate and microturbulence. A higher shear rate and a more intensive microturbulence occurred in the stirred tank, producing higher protein accumulation and higher proteolytic activity compared with those of the other two bioreactor systems. Higher shear rate and microturbulence had an elicitor effect on protease synthesis, because microturbulence in stirred tank bioreactors was lower than the average length of J. mexicana cells. Furthermore, cells in the stirred tank were smaller and thinner than those grown in shake flask, bubble column and airlift bioreactors. In summary, proteases were produced by J. mexicana cell cultures in a stirred tank under conditions of high shear rate and intensive microturbulence, which are similar to those which occur in industrial stirred tanks. These results encourage continuation of the process development for large scale production of these proteases by this technology.     

The effect of nickel on the growth, photosynthesis, and nitrogenase activity of Anabaena inaequalis.

Anabaena inaequalis was sensitive to nickel ion in the order of decreasing sensitivity of growth, photosynthesis, and acetylene reduction. At a culture density of 9 x 10(4) cells per millilitre, growth after 12 days was completely inhibited by 0.125 ppm (microgram/mL) Ni2+. Nickel caused the increase of both the lag phase of growth and the culture doubling time, and caused the retardation phase to be sooner. Photosynthesis and acetylene reduction were completely inhibited by 10 and 20 ppm Ni2+, respectively, at a cell concentration of 1.3 x 10(6) cells per millilitre. Preincubation for 24 h in the presence of nickel ion significantly increased the sensitivity of photosynthesis and acetylene reduction. Under these conditions acetylene reduction was more sensitive than photosynthesis. Nickel ion reduced culture growth by 35% at a level of 0.05 ppm and inhibited that culture's acetylene-reducing ability by 29% while leaving photosynthesis unaffected. Nickel caused some damage to filament apical cells and induced pigment bleaching in aged cultures. Nickel toxicity was proposed to be due to poisoning of intracellular enzyme systems by nickel ions.     

Improved medium for clonal growth of human diploid fibroblasts at low concentrations of serum protein

Summary A new medium (MCDB 104) has been developed which will support clonal growth of WI-38 cells at concentrations of serum protein as low as 25 μg per ml (equivalent to 0.05% serum). The principal factors responsible for reduction of the protein requirement are: (a) adjustment of all nutrient concentrations in medium F12 to experimentally determined optimum values for WI-38 cells; (b) supplementation with trace elements; (c) replacement of hypoxanthine and folic acid with adenine and folinic acid; and (d) coating of the culture surface with polylysine. Individually, many of these modifications exert only a small effect on cellular growth at reduced protein concentrations, but collectively their effect has been very substantial. Other strains of fibroblast-like human diploid cells from amniotic fluid, fetal lung and newborn foreskin also will grow at reduced concentrations of serum protein in the new medium. This work was supported by Grant No. AG00310 from the National Institute on Aging, and by Contract No. 223-74-1156 from the Bureau of Biologics, U.S. Food and Drug Administration.     

Development of improved media and culture conditions for clonal growth of normal diploid cells

Multiplication of normal diploid cells in culture is controlled by a complex set of interacting extracellular variables. The amount of serum protein needed for colony formation by such cells is affected directly by many of the other variables, including the nature of the culture surface, the type of trypsinization procedure used, and the qualitative and quantitative composition of the culture medium. By a sequential process of adjusting all of these variables to optimum values for cellular multiplication with minimal amounts of serum protein, we have been able to obtain clonal growth of normal human and chicken cells with less than 500 microgram per ml dialyzed serum protein. Precise quantitative adjustment of nutrient concentrations is particularly important. The multiplication-promoting functions of serum can be classified operationally as "replaceable" (those that can be replaced by modifying the medium or the culture conditions) and "nonreplaceable" (those that we have not yet been able to replace). Elimination of the requirement for replaceable functions of serum has improved greatly the specificity and sensitivity of the bioassay for the nonreplaceable functions. The nonreplaceable multiplication-promoting activity from fetal bovine serum for human diploid fibroblasts has been separated from fetuin and serum albumin and purified approximately 15-fold.     

Selective desorption of carbon dioxide from sewage sludge for in situ methane enrichment--part I: pilot-plant experiments

In situ methane enrichment in anaerobic digestion of sewage sludge has been investigated by experiments and by modeling. In this first part, the experimental work on the desorption of carbon dioxide and methane from sewage sludge is reported. The bubble column, had a diameter of 0.3 m and a variable height up to 1.8 m. At operation the dispersion height in the column was between 1 and 1.3 m. Outdoor air was used. The column was placed close to a full-scale sewage sludge digester, at a municipal wastewater treatment plant. The digester was operated at mesophilic conditions with a hydraulic retention time of about 20 days. The bubble column was operated to steady-state, at which carbon dioxide concentration and alkalinity were determined on the liquid side, and the concentration of carbon dioxide and methane on the gas side. Thirty-eight experiments were performed at various liquid and gas flow rates. The experimental results show that the desorption rates achieved for carbon dioxide ranges from 0.07 to 0.25 m(3) CO(2)/m(3) sludge per day, which is comparable to the rate of generation by the anaerobic digestion. With increasing liquid flow rate and decreasing gas flow rate the amount of methane desorbed per amount of carbon dioxide desorbed increases. The lowest methane loss achieved is approximately 2% of the estimated methane production in the digestion process.     

Use of Geotrichum candidum for olive mill wastewater treatment in submerged and static culture

The production of lignin peroxidase (LiP), manganese peroxidase (MnP) and lipases by Geotrichum candidum were performed in order to control the decolourisation and biodegradation of olive mill wastewater (OMW). Optimisation of different factors showed that dilution, carbon and ammonium concentrations significantly affected decolourisation and activities of ligniolytic peroxidases (LiP and MnP) on OMW. Moreover, addition of olive oil and agitation improved the lipase production. Batch and continuous OMW treatments in settler or bubble column bioreactors showed high COD and colour removal efficiencies of 60% and 50%, respectively. Lipolytic activity was greater in the batch bubble column whereas, LiP and MnP productions were improved in the settler. The performance of the continuous processes decreased with the decrease of hydraulic retention time (HRT). It has been shown that decolourisation and biodegradation decreased with an average of 40% and 45%, respectively, by decreasing the HRT from 4 d to 1.7 d.     

Development of a novel bioreactor system for treatment of gaseous benzene

A novel, continuous bioreactor system combining a bubble column (absorption section) and a two-phase bioreactor (degradation section) has been designed to treat a gas stream containing benzene. The bubble column contained hexadecane as an absorbent for benzene, and was systemically chosen considering physical, biological, environmental, operational, and economic factors. This solvent has infinite solubility for benzene and very low volatility. After absorbing benzene in the bubble column, the hexadecane served as the organic phase of the two-phase partitioning bioreactor, transferring benzene into the aqueous phase where it was degraded by Alcaligenes xylosoxidans Y234. The hexadecane was then continuously recirculated back to the absorber section for the removal of additional benzene. All mass transfer and biodegradation characteristics in this system were investigated prior to operation of the integrated unit, and these included: the mass transfer rate of benzene in the absorption column; the mass transfer rate of benzene from the organic phase into the aqueous phase in the two-phase bioreactor; the stripping rate of benzene out of the two-phase bioreactor, etc. All of these parameters were incorporated into model equations, which were used to investigate the effects of operating conditions on the performance of the system. Finally, two experiments were conducted to show the feasibility of this system. Based on an aqueous bioreactor volume of 1 L, when the inlet gas flow and gaseous benzene concentration were 120 L/h and 4.2 mg/L, respectively, the benzene removal efficiency was 75% at steady state. This process is believed to be very practical for the treatment of high concentrations of gaseous pollutants, and represents an alternative to the use of biofilters.     

Degradation of n-valeric acid by alginate-entrapped Alcaligenes denitrificans

Summary Alcaligenes denitrificans was isolated from sewage sludge and showed a strong degradative ability towards volatile fatty acids. The organism was tested both as free cells and immobilised in calcium alginate, for the ability to degrade the sodium salt of a typical volatile fatty acid, valeric acid.In shake flask culture the immobilised cells could be used to fully degrade 18 mM valerate over ten 48 h runs before bead break up occurred. The use of beads in conventional stirred tank fermenters, and a bubble column reactor was also investigated, with a 50 ml bubble column containing 5 ml of beads giving the highest overall degradation rate of 1.8 mmol/h, for 40 h in a fed batch mode of operation.     

Comparison of the Baker's yeast process performance in laboratory and production scale

A 215 m³ industrial bubble column reactor for fedbatch production of Baker's yeast was sampled for sugar, to investigate the extent of concentration gradients. The results verify that such gradients exist: the concentration is higher closer to the feeding point. Effects of sugar heterogeneities at different scales were studied by 1)?performing a volumetric scale-down of the industrial process in a laboratory stirred tank reactor (STR); 2) performing the same scaled down process in a Scale-Down Reactor (SDR) with repeated short term exposure of the cells to high sugar concentrations. In this reactor about 10% of the Baker's yeast culture was intermittently exposed to high (0.45–1.9?g?l^?1) concentrations of sugar, for periods of 60 seconds. It was found that physiological parameters of glycolysis and respiration were affected by environmental heterogeneities: 1) A biomass yield reduction of about 6–7% was found, with both the production reactor and the SDR, as compared to the homogeneous reactor. The loss of yield is interpreted in terms of a metabolic by-pass via ethanol, where cells are consuming and producing ethanol with different yields. 2) The maximum respiration rate was higher in cells produced in the production unit and in the SDR. 3) The product quality, expressed as gassing power of the yeast in a dough, was increased for sweet and non-sugar doughs in the SDR, and for sweet doughs in the production reactor. Thus, the SDR, when run with defined glucose gradients, in some aspects resembles the large reactor. It could be regarded as a tool for scale-down and scale-up studies and may be useful in investigations on the scale-up sensitivity of a process.     

Quantitative investigations of cell-bubble interactions using a foam fractionation technique

Previous work by the authors and others has shown that suspended animal cell damage in bioreactors is caused by cell-bubble interactions, regardless whether the bubbles are from bubble entrainment or direct gas sparging. As approach to measure the adsorptivity of animal cells to bubbles, a modified batch foam fractionation technique has been developed in this work and proven to be applicable. By using this technique, the number of cells adsorbed per unit bubble surface area and the adsorption coefficients have been measured to quantify hybridoma cell-bubble interactions, and the prevetive effects of serum and Pluronic F68 on these interactions. It was demonstrated quantitatively that the hybridoma cells adhere to bubbles spontaneously and significant numbers exist in the foam, and that both the serum and Pluronic F68 provide strong prevention to these cell-bubble interactions. The results obtained provide criteria for bioreactor operation and medium formulation to prevent cell-bubble interactions and cell damage in the culture processes.Abbreviations NBCS new born calf serum - SFM serum-free medium