Polysaccharide production by immobilized Aureobasidium pullulans cells in batch bioreactors.

Cells of the fungus Aureobasidium pullulans ATCC 201253 were entrapped within 4% agar cubes or 5% calcium alginate beads and were examined for their production of the polysaccharide pullulan in batch bioreactors. The batch bioreactors were utilized twice for 168 hours of polysaccharide production in medium containing corn syrup as a carbon source. The agar-entrapped cells produced nearly equivalent pullulan concentrations during both production cycles. The alginate-entrapped cells produced higher polysaccharide levels during the second cycle compared to the levels observed during the initial cycle. The agar-entrapped cells elaborated a polysaccharide with a higher pullulan content than did the alginate-entrapped cells during both production cycles.     

Polysaccharide production by immobilized Aureobasidium pullulans cells in batch bioreactors

Cells of the fungus Aureobasidium pullulans ATCC 201253 were entrapped within 4% agar cubes or 5% calcium alginate beads and were examined for their production of the polysaccharide pullulan in batch bioreactors. The batch bioreactors were utilized twice for 168 hours of polysaccharide production in medium containing corn syrup as a carbon source. The agar-entrapped cells produced nearly equivalent pullulan concentrations during both production cycles. The alginate-entrapped cells produced higher polysaccharide levels during the second cycle compared to the levels observed during the initial cycle. The agar-entrapped cells elaborated a polysaccharide with a higher pullulan content than did the alginate-entrapped cells during both production cycles.     

Cell Culture conditions determine the enhancement of specific monoclonal antibody productivity of calcium alginate-entrapped S3H5/gamma2bA2 hybridoma cells

Immobilization offers several intrinsic advantages over free suspension cultures for the production of monoclonal antibodies. An important advantage of immobilization is the improved specific monoclonal antibody (MAb) productivity (q(MAb)) that can be obtained. However, there are conflicting reports in the literature on the enhancement of the q(MAb) with immobilization. The discrepancies between these reports can be attributed to the different to either the cultivation methods used for immobilized cell or to difference between the cell lines used in the various studies. We show that these differences may be attributed to the different cultivation methods used for one model hybridoma cell line. S3H5/Upsilon2bA2 hybridoma cells entrapped in different sizes of calcium alginate beads were cultivated in both T- and spinner flasks in order to determine whether cultivation methods (T- and spinner flasks) and bead size influence the q(MAb) Free-suspended cell cultures inoculated with cells recovered from alginate beads were also carried out in order to determine whether changes in the q(Mab) of the entrapped cells are reversible.The cultivation methods was found to influence significantly the q(MAb) of the entrapped cells. When the entrapped cells in 1-mn diameter beads were cultivated in T-flasks, the q(MAb) was not increased by 200% as previously observed in an entrapped cell culture using 1-mm-diameter alginate beads in spinner flasks. The q(MAb) of the entrapped cell was approximately 58% higher than that of the free-suspended cells in a control experiment. Unlike the cultivation method, the bead size in the range of 1- to 3-mm diameter did not significantly influence the q(MAb), regardless of cultivations methods. The changes in q(MAb) of an entrapped cells were reversible. When the free-suspended cells recovered from the T- and spinner flasks were sub-cultured in T- and spinner flasks enhanced q(MAb) of the entrapped cells in both cases decreased to the level of the free-suspended cell in a control experiments. Taken together, these results shows that the method of cultivation of hybridoma cells immobilized in alginate beads determines the extent of enhancement of the q(MAb). (c) 1993 John Wiley & Sons, Inc.     

Enhanced specific antibody productivity of calcium alginate-entrapped hybridoma is cell line-specific

In order to determine whether the enhanced specific antibody productivity (q _MAb ) of calcium alginate-entrapped hybridoma is cell line-specific, calcium alginate-entrapped hybridomas (4A2 and DB9G8) were cultivated under the condition where we had previously observed significantly enhancedq _MAb of calcium alginate-entrapped S3H5/2bA2 hybridoma. Unlike S3H5/2bA2 hybridoma, neither 4A2 nor DB9G8 hybridomas showed persistently enhancedq _MAb when they were entrapped in calcium alginate beads. The enhancedq _MAb of entrapped 4A2 and DB9G8 hybridomas, which was 2–3 times higher than theq _MAb of free-suspended cells in a control experiment, was observed only during the early stage of the culture. During the early stage of the culture, the viable cell concentration decreased probably due to cell damage during the entrapment process. As cell growth resumed, theq _MAb decreased to the similar level ofq _MAb of free-suspended cells within 5–7 days. Thus, we conclude that the enhancedq _MAb of calcium alginate-entrapped hybridomas is cell line-specific.     

Stability of antibody productivity is improved when hybridoma cells are entrapped in calcium alginate beads

Loss of monoclonal antibody (MAb) productivity in long-term, free-suspended cell culture is often attributed to the appearance of a nonproducing population of hybridoma cell (NP) in the culture which has a growth advantage over the producing population (P). However, when an NP appears in long-term culture of entrapped cells, it may not be able to take over the whole culture in a short period of time due to the limited growth of the entrapped cells. In order to examine the hypothesis that entrapped cells can have improved stability of MAb productivity due to limited cell growth, free-suspended cell culture and calcium alginate-entrapped cell culture with inocula consisting of a P and an NP were compared with regard to stability of MAb productivity in a repeated fed-batch culture. In free-suspended cell culture, the NP appeared to take over the whole culture within three batches, and thereby MAb production completely disappeared. In entrapped cell culture, an NP appeared to outgrow the P rapidly only during an exponential growth phase, resulting in a significant decrease in specific MAb productivity, q(MAb), from 11.58 mug/10(6) cell/day to 2.76 mug/10(6) cell/day. However, when the cell growth was limited in entrapped cell culture, the NP no longer outgrew the P rapidly, as indicated by the stable value of q(MAb). In addition, when the cells recovered from the alginate beads by citrate buffer treatment were subcultured in free-suspended cell culture, MAb production rapidly deteriorated and completely disappeared within two batches. Thus, the P present at a small fraction of viable cell concentration in the beginning of the free-suspended cell culture, which were previously entrapped in alginate beads, seemed to be outgrown rapidly by the NP. Taken together, the results obtained from these experiments support the hypothesis that the limited cell growth in entrapped cell culture, which keeps an NP from taking over the whole culture, is responsible, in part, for the improved stability of MAb productivity. (c) 1993 John Wiley & Sons, Inc.     

Hybridoma perfusion systems: a comparison study

The efficiency of lgM production by hybridoma cells (1) cultured in suspension; (2) entrapped in alginate beads; or (3) packed in hollowfiber cartridge bioreactors, were compared in long-term perfusion cultures. The results showed that steady-state cell concentration and antibody production, per liter of perfused medium per day, were similar when cells were either entrapped in alginate beads of maintained in suspension. These values were also similar whether cells were maintained at high density in a hollowfiber cartridge bioreactro, or at low density in suspension. This work points out that cell behavior and antibody yield are comparable overall in the various perfusion systems currently used. However, a significant reduction of antibody production appeared whenever a part of the viable cells was lost in the filtrate. The reduction was due both to a decrease of viable cell yield and a decline of lgM productivity on a percell basis. This result is well in agreement with the previously presented model of "grow or die" cell cycle system of hybridoma, which proposes that the ratio of arrested to proliferating cells in perfusion cultures, should be increased in proportion to cell retention in the bioreactor, with a concomitant increase of lgM productivity.     

Survival of Bifidobacterium longum immobilized in calcium alginate beads in simulated gastric juices and bile salt solution

Bifidobacterium longum KCTC 3128 and HLC 3742 were independently immobilized (entrapped) in calcium alginate beads containing 2, 3, and 4% sodium alginate. When the bifidobacteria entrapped in calcium alginate beads were exposed to simulated gastric juices and a bile salt solution, the death rate of the cells in the beads decreased proportionally with an increase in both the alginate gel concentration and bead size. The initial cell numbers in the beads affected the numbers of survivors after exposure to these solutions; however, the death rates of the viable cells were not affected. Accordingly, a mathematical model was formulated which expressed the influences of several parameters (gel concentration, bead size, and initial cell numbers) on the survival of entrapped bifidobacteria after sequential exposure to simulated gastric juices followed by a bile salt solution. The model proposed in this paper may be useful for estimating the survival of bifidobacteria in beads and establishing optimal entrapment conditions.     

Calcium alginate beads as a slow-release system for delivering angiogenic molecules in vivo and in vitro.

A method previously used in this laboratory for entrapment of tumor cells in alginate beads has been extended to provide a slow release delivery system for growth factors with known in vivo angiogenic activity. Protein growth factors were entrapped in alginate beads in amounts sufficient to cause incorporation of 3H-thymidine by COMMA-D cells in vitro, and in vivo neovascularization when injected subcutaneously into Balb/c mice. Entrapment of 125I-labelled growth factors showed that the amount of molecule entrapped in alginate beads may vary with the charge of the molecule. In vitro cell proliferation studies showed that entrapment in alginate beads may provide a slow-release system or a stabilizing environment for the protein. In some cases biological activity of the growth factor in solution was increased by the presence of control alginate beads. When alginate-entrapped growth factors were injected into Balb/c mice, induction of new blood vessels could be monitored qualitatively by macroscopic photography and assessed quantitatively by measuring the pooling of radiolabelled red blood cells at the experimental site. Subcutaneous injection of purified angiogenic factors not entrapped in alginate beads did not cause neovascularization. Diffusion of 125I-labelled growth factors from alginate beads in the animal showed that release in vivo may depend on the charge of the protein molecule. These results indicate that injection of purified molecules entrapped in alginate beads provides an effective localized and slow-release delivery of biologically active molecules. This delivery system may extend the time of effectiveness of biologically active molecules in vivo compared to direct injection without alginate entrapment. The method of entrapment and injection has potential for identifying active factors in tumor-induced angiogenesis and testing new compounds as modulators of neovascularization.     

Oxygen uptake by entrapped hybridoma cells

Oxygen consumption by hybridoma cells immobilized in 1- and 3.9-mm-diameter calcium alginate beads was measured. The entrapped cells consumed oxygen at about 10 mumol/min per 10(9) cells, regardless of the bead size and cell loading. In contrast, the same cells in suspension culture respire at specific rates of 3-8 mumol/min per 10(9) cells (depending on the cell density). The growth rate of the immobilized cells was significantly reduced, while specific antibody production was comparable to that of free cells.     

Survival of Bifidobacterium longum Immobilized in Calcium Alginate Beads in Simulated Gastric Juices and Bile Salt Solution

Bifidobacterium longum KCTC 3128 and HLC 3742 were independently immobilized (entrapped) in calcium alginate beads containing 2, 3, and 4% sodium alginate. When the bifidobacteria entrapped in calcium alginate beads were exposed to simulated gastric juices and a bile salt solution, the death rate of the cells in the beads decreased proportionally with an increase in both the alginate gel concentration and bead size. The initial cell numbers in the beads affected the numbers of survivors after exposure to these solutions; however, the death rates of the viable cells were not affected. Accordingly, a mathematical model was formulated which expressed the influences of several parameters (gel concentration, bead size, and initial cell numbers) on the survival of entrapped bifidobacteria after sequential exposure to simulated gastric juices followed by a bile salt solution. The model proposed in this paper may be useful for estimating the survival of bifidobacteria in beads and establishing optimal entrapment conditions.     

Cell immobilization technique for the enhanced production of alpha-galactosidase by Streptomyces griseoloalbus

Streptomyces griseoloalbus was immobilized in calcium alginate gel and the optimal immobilization parameters (concentrations of sodium alginate and calcium chloride, initial biomass and curing time) for the enhanced production of alpha-galactosidase were determined. The immobilization was most effective with 3% sodium alginate and 0.1M calcium chloride. The optimal initial biomass for immobilization was approximately 2.2g (wet wt.). The alginate-entrapped cells were advantageous because there was a twofold increase in the enzyme yield (55 U/ml) compared to the highest yield obtained with free cells (23.6 U/ml). Moreover, with immobilized cells the maximum yield was reached after 72 h of incubation in batch fermentation under optimal conditions, whereas in the case of free cells the maximum enzyme yield was obtained only after 96 h of incubation. The alginate beads had good stability and also retained 75% ability of enzyme production even after eight cycles of repeated batch fermentation. It is significant that this is the first report on whole-cell immobilization for alpha-galactosidase production.     

Ethanol production from whey with immobilized living yeast

Summary Living Kluyveromyces fragilis yeast cells were succesfully entrapped in calcium alginate gel beads at cell loadings of 4 to 16 g yeast (0.8 to 3.2 g d.m.) per 1 g of sodium alginate. In batch systems, about 90 % conversion in 48 h was obtained both with free and immobilized yeast using demineralized whey of 5 to 10 % lactose content as substrate. In continuous packed-bed column operation nearly a constant 2 % product ethanol concentration could be maintained at 5 % substrate lactose level for at least one month.     

Performance of an external loop air-lift bioreactor for the production of monoclonal antibodies by immobilized hybridoma cells

Summary The performance of an external loop air-lift bioreactor was investigated by assessing the inter-relationships between various hydrodynamic properties and mass transfer. The feasibility of using this bioreactor for the production of monoclonal antibodies by mouse hybridoma cells immobilized in calcium alginate gel beads and alginate/poly-l-lysine microcapsules was also examined. When the superficial gas velocity, V _g , in the 300 ml reactor was varied from 2 to 36 cm/min, the average liquid velocity increased from 3 to 14 cm/sec, the gas hold-up rose from 0.2 to 3.0%, and the oxygen mass transfer coefficient, k _L a, increased from 2.5 to 18.1 h^-1. A minimum liquid velocity of 4 cm/s was required to maintain alginate gel beads (1000 m diameter, occupying 3% of reactor volume) in suspension. Batch culture of hybridoma cells immobilized in alginate beads followed logarithmic growth, reaching a concentration of 4×10⁷ cells/ml beads after 11 days. Significant antibody production did not occur until day 9 into the culture, reaching a value of 100 g/ml of medium at day 11. On the other hand, bioreactor studies with encapsulated hybridoma cells gave monoclonal antibody concentrations of up to 800 g/ml capsules (the antibody being retained within the semipermeable capsule) and maximum cell densities of 2×10⁸ cells/ml capsule at day 11. The volumetric productivities of the alginate gel immobilized cell system and the encapsulated cell system were 9 and 3 g antibody per ml of reactor volume per day, respectively. The main advantage of the bioreactor system is its simple design, since no mechanical input is required to vary the hydrodynamic properties.     

固定化乳酸乳球菌连续生产Nisin的研究

以海藻酸钙为材料 ,固定乳酸乳球菌 (Lactococcuslactissubsp .lactis)SM5 2 6 ,研究不同条件对Nisin合成的影响。结果表明 ,利用 2 %海藻酸钠在 1 0mmol LCaCl2 条件下 ,得到的固定化细胞颗粒稳定性较好 ,可维持 90h无破裂 ;在发酵过程中SYS3培养基中的无机盐成分尤其磷酸盐对固定化颗粒有破坏作用 ;用mSYS3培养基代替SYS3 ,通过 72h三批次循环的半连续培养 ,Nisin活性为 85 0IU mL ,无明显的细胞渗漏现象。连续化生产 70h ,Nisin活性达 1 1 5 0IU mL ,相当于游离细胞的发酵水平。     

Effect of trisodium citrate treatment on hybridoma cell viability

Trisodium citrate has been widely used to dissolve calcium alginate beads in order to estimate cell concentration in the beads. To obtain an accurate measurement of viable cell concentration in calcium alginate beads, the effect of trisodium citrate solutions on hybridoma cell viability was studied with regard to stage of growth and trisodium citrate concentration. The cells in the decline phase of growth were more sensitive to 30 minutes of trisodium citrate treatment than the cells in the exponential phase of growth. The cell viability did not decrease rapidly during citrate treatment regardless of cell growth phase and trisodium citrate concentration in the range of 1–1.5%. By using the commercially available sodium alginate, Keltone LV, dissolution time can be kept short enough (below 5 minutes) to keep the effect of trisodium citrate negligible to cell viability.     

Continuous production of l-serine by immobilized growing Corynebacterium glycinophilum cells

Summary Auxotrophic mutant cells of Corynebacterium glycinophilum with high l-serine production activity were immobilized by entrapment with various gel materials, such as synthetic prepolymers and natural polysaccharides. The entrapped cells were used for estimation of l-serine productivity in a medium supplemented with glycine as a precursor. Based on the above criteria, including cell growth in gels and cell leakage from gels, calcium alginate was the most suitable gel material. Continuous l-serine fermentation with calcium alginate-entrapped growing cells was successfully achieved in an air-bubbled reactor for at least 13 days.     

Anti-Hepatitis B surface Antigen monoclonal antibody IgM production in suspension and immobilized cell bioreactors

Summary We have cultivated a hybridoma cell-line H505AC in suspension and alginate immobilized cell bioreactors to produce anti-Hepatitis B surface Antigen (anti-HBsAg) monoclonal antibody IgM. The specific IgM production rates correlate linearly with the specific glucose consumption rate in suspension culture with a maximum production rate of 300 g/10⁶ cells/day. In alginate-cell immobilized airlift bioreactor, a total of 1143 milligrams IgM was produced in 9 days operation with a volumetric productivity 44.1 mg/day.L     

Characterization of an encapsulation device for the production of monodisperse alginate beads for cell immobilization

An encapsulation device, designed on the basis of the laminar jet break-up technique, is characterized for cell immobilization with different types of alginate. The principle of operation of the completely sterilizable encapsulator, together with techniques for the continuous production of beads from 250 microm to 1 mm in diameter, with a size distribution below 5%, at a flow rate of 1-15 mL/min, is described. A modification of the device, to incorporate an electrostatic potential between the alginate droplets and an internal electrode, results in enhanced monodispersity with no adverse effects on cell viability. The maximum cell loading capacity of the beads strongly depends on the nozzle diameter as well as the cells used. For the yeast Phaffia rhodozyma, it is possible to generate 700 microm alginate beads with an initial cell concentration of 1 x 10(8) cells/mL of alginate whereas only 1 x 10(6) cells/ml could be entrapped within 400 microm beads. The alginate beads have been characterized with respect to mechanical resistance and size distribution immediately after production and as a function of storage conditions. The beads remain stable in the presence of acetic acid, hydrochloric acid, water, basic water, and sodium ions. The latter stability applies when the ratio of sodium: calcium ions is less than 1/5. Complexing agents such as sodium citrate result in the rapid solubilization of the beads due to calcium removal. The presence of cells does not affect the mechanical resistance of the beads. Finally, the mechanical resistance of alginate beads can be doubled by treatment with 5-10 kDa chitosan, resulting in reduced leaching of cells.     

Effect of skim milk-alginate beads on survival rate of bifidobacteria

In this study, an attempt was made to increase the survival rate of bifidobacteria entrapped in alginate in the gastrointestinal tract, and to investigate the potential industrial applications, for example lyophilized capsules and yogurt. First, the protective effect of various food additives on bifidobacterial survivability was determined after exposure to simulated gastric juices and bile salts. The additives used in this study were skim milk (SM), poly dextrose (PD), soy fiber (SF), yeast extract (YE), chitosan (CS), κ-carageenan (κ-C) and whey, which were added at 0.6% concentration (w/v) to 3% alginate-bifidobacterial solution. In the simulated gastric juices and bile salts, the protective effect of 0.6% skim milk-3% alginate (SM-A) beads on the survival rate of bifidobacteria proved to be higher than the other additives. Second, the hydrogen ion permeation was detected through SM-A vessel without bifidobacterial cells at different SM concentrations (0.2%, 0.4%, 0.6%, 0.8%, and 1.0%). There were no differences in terms of the pH decrease in SM-A vessels at 0.6%, 0.8%, and 1.0% (w/v) SM concentrations. The survival rate of bifidobacteria in SM-A beads would appear to be related to the SM buffering capacity against hydrogen ions and its tendency to reduce the pore size of bead. In this experiment, the survival rate of bifidobacteria entrapped in beads containing 0.6% SM showed the highest viability after exposure to simulated gastric juices for 3 h, thereby indicating that 0.6% SM is the optimum concentration for 3% alginate bead preparation. Third, the effect of SM-A beads on the freeze-drying and yogurt storage for 10 days was investigated. SM-A beads were found to be more efficient for freeze drying and yogurt storage than untrapped cells and the alginate bead. Consequently, the survival rate of bifidobacteria entrapped in SM-A beads was increased in simulated gastric juices, bile salts and probiotic products such as lyophilized capsules and yogurt, SM-A beads can be expected to produce high value probiotic products.     

Effect of calcium chloride treatment on hybridoma cell viability and growth

In order to minimize hybridoma cell damage during calcium alginate entrapment, the effect of calcium chloride treatment on hybridoma cell viability and growth was studied in terms of calcium chloride concentration and treatment time. The cell viability as measured by trypan blue exclusion did not decrease rapidly during the first hour of calcium chloride treatment regardless of calcium chloride concentrations used (1.3 and 1.5%). However, 1.3% calcium chloride solution appeared to be more detrimental to the cells than 1.5% calcium chloride solution. The cells in 1.3% calcium chloride solution lost their viability faster than the cells in 1.5% calcium chloride solution. In addition, when the cells treated with calcium chloride were inoculated into spinner flasks containing IMDM with 10% fetal calf serum, the cells treated with 1.3% calcium chloride solution showed a longer lag phase than the cells treated with 1.5% calcium chloride solution.