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.     

乳杆菌微胶囊化培养的研究

采用MaCSPDMDAAC微胶囊对两种乳杆菌进行了固定化发酵研究。结果表明,两种乳杆菌能够在微胶囊内很好地生长和繁殖,菌浓度可分别达到18×1011/mL 胶囊和269×1011/mL胶囊,比游离培养高出十倍以上,并且能与游离发酵一样产生乳酸,糖耗时间可缩短1/3～2/3。进行的多批次发酵显示了巨大的产酸能力。     

Growth of baculovirus-infected insect cells in microcapsules to a high cell and virus density

Summary Insect cells (Spodoptera Frugiperda), infected with a temperature-sensitive mutant (TS10) of theAutographa Californica nuclear polyhedrosis virus (AcNPV), were cultured in multiple membrane alginate-polylysine (PLL) microcapsules. It was possible to obtain intracapsular cell densities of 8× 10⁷ cells/mL of capsules and virus concentrations of up to 10⁹ IFU/mL of capsules. This was higher by a factor of 10 than that which could be achieved by conventional cell suspension culture.     

Substantial overproduction of antibodies by applying osmotic pressure and sodium butyrate

Much of the current cell technology has enabled increased antibody production levels due to judicious nutrient feeding to raise cell densities and design better bioreactors. This study demonstrates that hybridomas can be hyperstimulated to produce higher immunoglobulin (lg) levels by suppressing cell growth and increasing culture longevity through adaptation to higher osmolarity media and addition of sodium butyrate. Prior to adaptation, cells placed in higher osmotic pressures (350 and 400 mOsm) were severely suppressed in growth down to 25% of the control (300 mOsm), although total lg titers achieved were similar to the control, approximately 140 mg/L. After a week of adaptation to 350 and 400 mOsm media, cell growth was not as dramatically suppressed, but considerably higher lg levels were attained at these elevated osmolarities. The highest yield of 265 mg/L was obtained at 350 mOsm compared to 140 mg/L at 300 mOsm, while maximum viable cell numbers dropped from 35 x 10(5) cells/mL to 31 x 10(5) cells/mL and culture longevity was extended by 20 h more than the control. Sodium butyrate, known to enhance protein production in other cell types, was then supplemented at a range of concentrations between 0.01 and 0.4 mM to the 350 mOsm culture to further enhance the lg levels. Butyrate at a concentration of 0.1 mM, in combination with osmotic pressure at 350 mOsm, further elevated the lg levels to 350 mg/L. Concomitantly, maximum viable cell numbers were reduced to 22 x 10(5) cells/mL, but culture longevity was extended by 40 h in the 0.1 mM butyrate supplemented culture compared to the control condition. Specific antibody productivity, q(Mab), continued to stay high during the stationary phase and was further elevated during the decline phase: thus, overall lg levels can be increased by 2.3 times by combining osmotic pressure and butyrate treatment. (c) 1993 John Wiley & Sons, Inc.     

Alginate concentration: a key factor in growth of temperature-sensitive baculovirus-infected insect cells in microcapsules

The desire to increase cell density and product concentration has been the primary driving force for the development of better animal cell culture processes. In the technique used in our laboratory-microencapsulation-insect cells (Spodoptera frugiperda), infected with a temperature-sensitive mutant of the Autographa californica nuclear polyhedrosis virus (AcNPV), were cultured in multiple membrane alginate-polylysine (PLL) microcapsules which had a controlled membrane molecular-weight cutoff and an intracapsular alginate concentration which was ca. 16% lower than that obtained in the commercially available single-membrane system. Cell culture experiments indicated that the intracapsular alginate concentration appears to be a key factor in achieving good cell growth. It was possible to obtain intracapsular cell densities of 8 x 10(7) cells/mL capsules and virus concentrations to 10(9) IFU/mL capsules. The virus litre in the supernatant was ca. 300 times lower, indicating that virtually all of the virus was retained within the capsules.     

Continuous hybridoma growth and monoclonal antibody production in hollow fiber reactors-separators

Growth of a hybridoma culture, along with production of monoclonal antibody, was demonstrated over extended periods in polysulfone hollow fiber membrane modules. The molecular weight cutoffs of the membranes were 70,000, 50,000, and 100,000 daltons. The hybridoma cell line, designated 65/26, produced IgG (2b/kappa) directed at mouse thymus cell surface antigen, TL.1. Cell growth occurred in the shell space of the reactor, using supplemented RPMI 1640 (20% fetal bovine serum) supplied from a separate reservoir vessel through the hollow fiber lumen. The reservoir contained 125 mL media, which was changed every 4 days. Concentrations of immunoglobulin were determined by an enzyme immunoassay (using protein A and alkaline phosphatase-labeled antibody conjugate). For the 10K, 50K, and 100K hollow fiber membrane modules, the maximum IgG concentrations detected in the 2.5-mL shell space were 47.5-80, 510, and 740 mug/mL, respectively. In the 125-mL reservoir for the 100K hollow fiber membrane module, the IgG concentration was measured at 260 mug/mL These values compare with an IgG concentration of 1 mug/mL when grown in a standard tissue culture flask and 3.2-7.6 mug/mL when grown in 100 ml media in a spinner flask. In addition, 10K and 50K hollow fiber membrane modules were run in a mode that decreased the fetal bovine serum supplement with time. Differences between these systems suggest that it is possible to obtain high IgG accumulation rates, both during and after the exponential growth phase of the hybridoma population.     

连续灌流培养杂交瘤细胞生产单克隆抗体

自 2 0世纪 70年代以来 ,工程抗体在基础医学研究、临床诊断和治疗 ,以及免疫预防等领域中的广泛应用 ,大大促进了其产业化的进程。目前工业化生产单克隆抗体的主要方法是通过发酵罐、中空纤维和固定床等生物反应器培养系统 ,以微载体、微包囊法在体外大规模高密度培养杂交瘤细胞 ,再通过相关的纯化手段浓缩纯化制备抗体[1 ,2 ] 。就操作方式而言 ,一般采用两个基本策略 :①大容量高密度的悬浮培养 ,最多采用的是搅拌式气升式生物反应器 ,通过微载体依托细胞相对固定化 ,降低了搅拌培养时对细胞的剪切力 ,提高细胞的密度和稳定性及生产率。…     

High-Density culture of mouse-human hybridoma in serum-free defined medium

Mouse-human hybridoma 4H11 cells producing anti-Pseudomonas sp. monoclonal antibody (IgA) grew in a serum-free medium supplemented with insulin, transferrin, ethanolamine, and selenite (ITES). The hybridoma could be applied to high-density culture in a serum-free medium supplemented with ITES, 0.5% BSA, egg yolk VLDL, and artificial blood FC-43 in a culture vessel equipped with hollow-fiber modules for medium exchange. Total cell density reached 1.1 x 10(7) cells/mL (viable cell density was 7.6 x 10(6) cells/mL), and the IgA productivity was around 20 mug/10(6) cells/day in the serum-free medium, which corresponded to the levels in serum-supplemented medium.     

Regulation of antibody response in different immunoglobulin classes. II. Induction of in vitro IgE antibody response in murine spleen cells and demonstration of a possible involvement of distinct T-helper cells in IgE and IgG antibody responses.

In vitro induction of anti-DNP IgE as well as IgG1, IgG2a antibody responses was shown in murine spleen cell culture. Spleen cells primed three times with 1 mug of DNP-OA or DNP-Asc produced significant amounts of anti-DNP IgE as well as IgG antibodies by the in vitro stimulation with DNP-OA or DNP-Asc, respectively. Collaboration between DNP-primed B cells and carrier-primed T cells was required for the induction of both IgE and IgG antibodies with DNP-coupled T-dependent antigen. Carrier-specific T cells induced with a low dose of Asc (0.01 mug) showed helper function only on IgE antibody response, whereas T cells primed with a higher dose of Asc (10 mug) cooperated only with IgG-B cells. T cells primed with Asc in CFA showed helper function mainly on IgG antibody response but not on IgE antibody response. The result indicated the presence of a distinct population of T helper cells for IgE and IgG antibody responses. T-independent antigen (DNP-Ficoll) induced both anti-DNP IgE and IgG antibody responses in DNP-primed spleen cell population without the requirement of the collaboration of helper T cells.     

Preparation and application of poly(vinylamine)/alginate microcapsules to culturing of a mouse erythroleukemia cell line

Poly(vinylamine) was synthesized and used to replace poly-L-lysine in forming microcapsule with alginate. Test results indicated that capsules with good mechanical strength and permeability could be obtained under the controlled treatment conditions of poly(vinylamine) and alginate. Application of the current microcapsular system to cell culture was demonstrated by the usage of erythropoietin- (EPO-) producing IW32 mouse erythroleukemia cells. The encapsulated IW32 cells grew to a density of 8 x 10(7) cells/mL, two times that found in the corresponding poly-L-lysine/alginate capsules. The EPO accumulation inside the microcapsule with the current encapsulation system was also higher. A concentration of 7.3 U/mL was attained as compared to 4.3 U/mL in the poly-L-lysine/alginate microcapsule. (c) 1992 John Wiley & Sons, Inc.     

Large-scale, high-density freezing of hybridomas and its application to high-density culture

Large-scale, high-density freezing of hybridomas was studied to apply frozen cells to start high-density culture. We showed here that hybridomas can be frozen at 1.5 x 10(8) cells/mL, without decrement in viability and proliferating activity. Blood transporting bags were used for large-scale freezing to store 25 mL of cell suspension with a cell density, 1.5 x 10(8)/mL. The number of cells stored in a bag (3.0 x 10(9) cells) was enough to start a high-density culture at a 10 times higher cell density (6.0 x 10(6) cells/mL) than normal inoculation, and the cells proliferated to 10(7) cells/mL within 2 days. These results indicate that the large-scale freezing method is useful for large-scale culture of mammalian cells.     

A modified matrix perfusion-microcarrier bead cell culture system. II. Production of human (beta) interferon in a matrix perfusion system

Addition of microcarrier beads to a matrix perfusion cell culture system allowed growth of anchorage dependent human foreskin fibroblasts which would not grow in the culture units alone. The utility of the system for collection of cellular products was demonstrated by the induction and harvesting of human (beta) interferon. Interferon production was highest in perfusion cultures when medium was circulated throughout the induction and when inducer containing 100 mug/mL polyriboinosinic: polyribocytidylic acid was placed directly in contact with cells in the extracapillary space. These conditions provided 4-to-10-fold greater interferon yields per cell, and approximately 12-fold increases per vessel, than monolayer cultures. Perfusion grown cells produced interferon at a maximal level for 20 h postinduction compared to approximately 2 h for monolayer grown cells, thus giving a higher total yield of interferon. Other procedures increasing the efficiency of the system included priming with 50 U/mL interferon standard, reinduction of cells, use of antibiotic free medium, reduced serum concentrations, and in vitro aging of the cells.     

Production of Bacillus thuringiensis spores in total cell retention culture and two-stage continuous culture using an internal ceramic filter system

The production of Bacillus thuringiensis spores was investigated in a bioreactor incorporating a ceramic membrane filter to improve spore concentration and volumetric productivity. Two cultivation methods were used in this study: a total cell retention culture (TCRC), and a two-stage continuous culture with partial cell bleeding. In the TCRC, fed by 50 g/L of glucose, a spore concentration of 1.6 x 10(10) CFU/mL was obtained with a spore percentage of greater than 95% and a maximum cell mass of 82.2 g/L. The volumetric productivity was four times higher than that obtained from batch cultivation. In the two-stage continuous culture with partial cell bleeding spore concentration was strongly dependent on the bleed ratio. The spore concentration of 1.8 x 10(9) CFU/mL and the spore percentage of 70% were obtained at the second stage when a bleed ratio of 0.33 and a dilution rate of 0.23 h(-1) were used. (c) 1993 John Wiley & Sons, Inc.     

Encapsulated animal cell culture for the production of monoclonal antibody (MAb)

Biopolymer membrane was prepared using two oppositely charged natural biopolymer. The biopolymer membrane was used for the encapsulation of two hybridoma cell (ATCC CRL-1606, ATCC BH-8852) to produce monoclonal antibodies. In order to reduce the down stream steps, the pore size of the membrane was controlled to retain the monoclonal antibodies in the capsules based on the diffusion experiments with standard proteins. T-flask culture showed cell densities of 8×10⁷ cells/mL and 3×10⁷ cells/mL, and MAb concentrations of 506 μg/mL and 109 μg/mL for encapsulated ATCC CRL-1606 and HB-8852, respectively. Two liter perfusion culture with encapsulated ATCC HB-8852 was performed to enhance the MAb production. The MAb production of the encapsulated hybridoma increased considerably comparing to the culture using silicone tubing for oxygen transfer.     

Ethanol production from nonsterilized carob pod extract by free and immobilized Saccharomyces cerevisiae cells using fed-batch culture

The production of ethanol from carob pod extract by free and immobilized Saccharomyces cerevisiae cells in batch and fed-batch culture was investigated. Fed-batch culture proved to be a better fermentation system for the production of ethanol than batch culture. In fed-batch culture, both free and immobilized S. cerevisiae cells gave the same maximum concentration (62 g/L) of final ethanol at an initial sugar concentration of 300 g/L and F = 167 mL/h. The maximum ethanol productivity (4.4 g/L h) was obtained with both free and immobilized cells at a substrate concentration of 300 g/L and F = 334 mL/h. In repeated fed-batch culture, immobilized S. cerevisiae cells gave a higher overall ethanol concentration compared with the free cells. The immobilized S. cerevisiae cells in Ca-alginate beads retained their ability to produce ethanol for 10 days. (c) 1994 John Wiley & Sons, Inc.     

Evaluation of a novel pneumatic bioreactor system for culture of recombinant Chinese hamster ovary cells

Single use culture systems are a tool in research and biotechnology manufacturing processes and are employed in mammalian cell-based manufacturing processes. Recently, we characterized a novel bioreactor system developed by PBS Biotech. The Pneumatic Bioreactor System? (PBS) employs the Air-wheel?, which is a mixing device similar in structure to a water wheel but is driven by the buoyant force of gas bubbles. In this study, we investigated the physical properties of the PBS system, with which we performed biological tests. In 2 L PBS, the mixing times ranged from 6 (30 rpm, 0.175 vvm) to 15 sec (10 rpm, 0.025 vvm). The k_La value reached upto 7.66/h at 0.5 vvm, even without a microsparger, though this condition is not applicable for cell cultures. Also, when a 10 L PBS equipped with a microsparger was evaluated, a k_La value of upto approximately 20/h was obtained particularly in mild cell culture conditions. We performed cultivation of Chinese hamster ovary (CHO) cells in 2 and 10 L PBS prototypes. Results from the PBS were compared with those from an Erlenmeyer flask and conventional stirred tank type bioreactor (STR). The maximum cell density of 10.6 × 106 cells/mL obtained fromthe 2 L PBSwas about 2 times higher than that from the Erlenmeyer flask (5.6 × 10⁶ cells/mL) andwas similar to the STR (9.7 × 10⁶ cells/mL) when the CHO-S cells were cultured. These results support the general suitability of the PBS system using pneumatic mixing for suspension cell cultivation as a novel single-use bioreactor system.     

Cell permeability: a factor in the biotin-oleate relationship in Lactobacillus arabinosus. II. Effect of oleic acid and other surfactants on free biotin uptake

Bound biotin-saturated cells were incubated in the presence of biotin and glucose (37 C, pH 7.5) with or without oleic acid, Tween 20, 40, 60, and 80, Aerosol OT, sodium dodecyl sulfate (SDS), cetyltrimethylammonium bromide, Triton X-100, Non-Ion-Ox, and Haemo-Sol. With low concentrations (up to 5 mug/ml) and short reaction times (up to 10 min), oleic acid stimulated free biotin accumulation. Increased concentrations (10 to 50 mug/ml) or reaction times (10 to 30 min) caused progressive reductions in uptake or increased release of previously accumulated vitamin. Combination of Tween 40 (1 mg/ml) with oleic acid (up to 50 mug/ml) detoxified oleic acid and stimulated free biotin uptake. Oleic acid (5 mug/ml or more) reduced cell viability, an effect which was overcome by Tween 40. All other surfactants tested stimulated free biotin accumulation at sublethal concentrations. Aerosol OT and SDS exhibited the same degree of stimulatory activity as detoxified oleic acid; however, at concentrations higher than 200 mum, a rapid decrease in vitamin accumulation was observed which paralleled that caused by increased oleic acid concentrations. The results suggest that oleic acid and other surfactants affect the permeability of cells of Lactobacillus plantarum (formerly called L. arabinosus) in a similar manner.     

胀果甘草悬浮培养细胞合成甘草总黄酮

比较了胀果甘草(Glycyrrhiza inflata)悬浮细胞在逐级放大摇瓶中的生长、黄酮产量以及营养消耗过程,以便了解其放大规律。结果表明,在250和500mL摇瓶中,细胞的最大生物量、黄酮产量以及最大比生长速率没有显著性差异,但是在1L的摇瓶中,这三种参数都显著地降低,分别比250mL摇瓶中降低了27%,30%和27%。在逐级放大的摇瓶中,氮、磷、铵浓度都随着培养时间延长而逐渐降低,尽管在1L的摇瓶中磷消耗得最慢,但三种摇瓶中磷在细胞生长对数期基本都被消耗尽了。此外,硝态氮在第18天时基本被消耗完,而铵态氮在细胞收获时仍能维持在100mg/L。因此在反应器中培养时,主要的培养条件还需进一步优化。     

High-titer adenovirus vector production in 293S cell perfusion culture

Human 293S cells culture for recombinant adenovirus production is traditionally carried out in batch at a maximum of 6 x 10(5) cells/mL. A previous report demonstrated that fed-batch, applied to the adenovirus/293S cells system, improves the volumetric production of viral proteins by increasing the cell density at which cells can be infected, up to 2 x 10(6) cells/mL, without reducing the per-cell yield of product. To increase this cell density limit, the adenovirus production was performed in a perfusion system where the cells were separated by means of a tangential flow filtration device. 293S cell growth to 14 x 10(6) cells/mL was achieved in 10 days, at a medium renewal rate of 1 volume of medium per reactor volume and day (VVD). For adenovirus production, three 293S cell cultures were perfused at 1 VVD in parallel and infected at an average density of 8 x 10(6) cells/mL. One of the cultures was set at 37 degrees C and the two others at 35 degrees C. After a rapid initial cell loss, the average cell density stabilized at 5.75 x 10(6) cells/mL, 12 h postinfection, which was 8 times higher than the cell density in the batch control. This allowed the production of 3.2 x 10(9) infectious viral particles/mL (IVP/mL) at 37 degrees C and 7.8 x 10(9) IVP/mL at 35 degrees C, this last result being 5.5 times higher than the control. To our knowledge, this nonconcentrated titer is the highest value that has ever been published for adenovirus vector production. These observations lead to the conclusion that perfusion is an efficient tool to maintain, at high cell density, a specific production rate level sufficient to increase significantly the adenovirus volumetric production. Furthermore, it shows that perfusion at 35 degrees C can improve viral titer by 2.4-fold compared to 37 degrees C, in accordance with a previous study on adenovirus batch production.