Two-stage depth filter perfusion culture for recombinant antibody production by recombinant Chinese hamster ovary cell

A rCHO cell line of DUKX origin 26*-320, producing recombinant antibody against the human platelet, was cultivated in a two-stage depth filter perfusion system (DFPS) for 20 days in order to attain high recombinant antibody concentration. The productivity of the first stage DFPS bioreactor reached 53 times that of the batch culture in a controlled stirred tank reactor and was showed 12.1 mg/L antibody concentration at a perfusion rate of 6.0 d⁻¹. Glucose concentration in the first DFPS was maintained at 1.5 g/L to avoid cell damage in the perfusion culture. A second stage DFPS system was attached to the first DFPS, which resulted in a low glucose concentration of 0.02 g/L and a high antibody concentration of 23.9 mg/L. The two-stage depth filter perfusion culture yielded 60% higher product concentration than the batch and 49-fold higher productivity of 69.3 mg/L/d in comparison with that (1.4 mg/L/d) in a batch system. Furthermore, antibody concentration of the second stage was 97% higher than that of the first stage, and the antibody productivities were comparable to that of the first stage. This two-stage DFPS system also showed potential for higher titer production of recombinant antibody and high volumetric productivity for long-term culture of bio-pharmaceutical substances.     

Recombinant antibody production by perfusion cultures of rCHO cells in a depth filter perfusion system

Recombinant Chinese hamster ovary cells, producing recombinant antibody against the human platelet, were cultivated in a depth filter perfusion system (DFPS). When perfusion cultures with working volume of 1 L were operated at perfusion rates of 5/d and 6/d, volumetric antibody productivities reached values 28 and 34 times higher than that of batch suspension culture in Erlenmeyer flasks and 43 and 53 times higher than that of batch culture in a controlled stirred tank reactor, respectively. Perfusion cultures in the DFPS showed stable antibody production over the whole culture period of up to 20 days. In the DFPS, inoculated cells in suspension were entrapped in a few hours within the depth filter matrix by medium circulation and retained there until the void space of the filter matrix was saturated by the cultured cells. After cells in the depth filter matrix reached saturation, overgrown viable cells at a perfusion rate of 5/d or 6/d were continuously collected into waste medium at a density of 2-4 x 10(5) cells/mL, which resulted in stable operation at high perfusion rates, maintaining values of process parameters such as glucose/lactate concentration, pH, and dissolved oxygen concentration. Because the DFPS overcomes most drawbacks observed with conventional perfusion systems, it is preferable to be used as a key culture system to produce monoclonal antibody stably for a long culture period.     

High-density continuous cultures of hybridoma cells in a depth filter perfusion system

A depth filter perfusion system (DFPS) for animal cell culture was developed and its use in continuous highdensity cultures of hybridoma cells was investigated. In the DFPS, based on cell immobilization in a cylindrical depth filter matrix, cells were easily immobilized and cultivated by simple medium recirculation. The cell density in the 20-mum pore size filter matrix reached up to 3 x 10(7) cells/mLin less than 10 days. This resulted in a high monoclonal antibody productivity of 744 mg/L/day, which was 25-35 times higher than that of continuous-suspension cultures using the same cell line. The 20-mum pore filter retained more cells than the 30-mum filterin a shorter period. The DFPS provides advantages of low-cost set-up, easy operation, and scale-up in the cultures of anchorage-independent cells. It also has a high potential for anchorage-dependent cell cultures because of its unusually high surface-to-volume ratio of 450-600 cm(2)/cm(3). (c) 1994 John Wiley & Sons, Inc.     

Continuous production of tissue plasminogen activator from recombinant CHO cells in a depth filter perfusion system

Summary A depth filter perfusion system (DFPS), equipped with a 40-m polypropylene depth filter for cell immobilization, was used for the continuous production of tissue plasminogen activator (t-PA) from recombinant Chinese hamster ovary cells. Final cell density in the DFPS with oxygen control was 1.8×10⁷ cells/mL of the total working volume and maximum t-PA productivity was 2.63 mg/L/day. Dissolved oxygen concentration in the filter matrix was successfully controlled by air sparging and stable operation was possible for more than 20 days.     

High cell density perfusion cultures of anchorage-dependent Vero cells in a depth filter perfusion system

A depth filter perfusion system (DFPS) with polypropylene fibers had been demonstrated to support high density cultures of anchorage-independent hybridoma cells. The DFPS provides advantages of high surface-to-volume ratio of 450–600 cm²/cm³, low cost set-up, easy operation and scale-up. To test the feasibility of using DFPS for high density cultures of anchorage-dependent cells, Vero cells were cultivated in the DFPS. Gelatin coating on polypropylene fibers in the DFPS was necessary to promote cell attachment and growth. Dissolved oxygen (DO) concentrations could be controlled by sparging air into the reservoir vessel through a filter sparger. When DO concentration was controlled above 40% of air saturation in the DFPS with 40 m pore size, the maximum cell concentration as estimated on specific lactate production rate, was 3.81×10⁷ cells/ml of the total reactor volume. This viable cell concentration is approximately 18 times higher than that obtained in a T-flask batch culture. Taken together, the results obtained here showed the potential of DFPS for high-density cultures of anchorage-dependent cells.     

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 hybridoma cells in a dual hollow fiber bioreactor

Summary Hybridoma cells were cultured for two months in the dual hollow fiber bioreactor (DHFBR) which had been successfully used for high cell density cultures of various microbial cells. In batch suspension culture the concentration of monoclonal antibody (Mab) against human Chorionic Gonadotropin (hCG) and the cell density of Alps 25-3 hybridoma cells were obtained in 30 μg/mL and 2.35×10⁶ cells/mL, respectively. The continuous culture with DHFBR produced Mab of 100–130 μg/mL for 30 days and the estimated cell density in the extracapillary space of DHFBR was 1.87×10⁸ cells/mL based on the antibody production rate. The productivity of Mab was 205 mg/day per litre of the total reactor volume while that of the batch suspension culture was only 10 mg/L day.     

Control of culture environment for improved polyethylenimine-mediated transient production of recombinant monoclonal antibodies by CHO cells

In this study we describe optimization of polyethylenimine (PEI)-mediated transient production of recombinant protein by CHO cells by facile manipulation of a chemically defined culture environment to limit accumulation of nonproductive cell biomass, increase the duration of recombinant protein production from transfected plasmid DNA, and increase cell-specific production. The optimal conditions for transient transfection of suspension-adapted CHO cells using branched, 25 kDa PEI as a gene delivery vehicle were experimentally determined by production of secreted alkaline phosphatase reporter in static cultures and recombinant IgG4 monoclonal antibody (Mab) production in agitated shake flask cultures to be a DNA concentration of 1.25 microg 10(6) cells(-1) mL(-1) at a PEI nitrogen:DNA phosphate ratio of 20:1. These conditions represented the optimal compromise between PEI cytotoxicity and product yield with most efficient recombinant DNA utilization. Separately, both addition of recombinant insulin-like growth factor (LR3-IGF) and a reduction in culture temperature to 32 degrees C were found to increase product titer 2- and 3-fold, respectively. However, mild hypothermia and LR3-IGF acted synergistically to increase product titer 11-fold. Although increased product titer in the presence of LR3-IGF alone was solely a consequence of increased culture duration, a reduction in culture temperature post-transfection increased both the integral of viable cell concentration (IVC) and cell-specific Mab production rate. For cultures maintained at 32 degrees C in the presence of LR3-IGF, IVC and qMab were increased 4- and 2.5-fold, respectively. To further increase product yield from transfected DNA, the duration of transgene expression in cell populations maintained at 32 degrees C in the presence of LR3-IGF was doubled by periodic resuspension of transfected cells in fresh media, leading to a 3-fold increase in accumulated Mab titer from approximately 13 to approximately 39 mg L(-1). Under these conditions, Mab glycosylation at Asn297 remained essentially constant and similar to that of the same Mab produced by stably transfected GS-CHO cells. From these data we suggest that the efficiency of transient production processes (protein output per rDNA input) can be significantly improved using a combination of mild hypothermia and growth factor(s) to yield an extended "activated hypothermic synthesis".     

Continuous stable production of von Willebrand Factor monoclonal antibody in spin filter bioreactor with bleeding technology

The characteristics of two different modes of perfusion culture, intermittent and continuous bleedings, were investigated by culturing the hybridoma cells producing von Willebrand Factor (vWF) monoclonal antibody (McAb) in a 15 L bioreactor without clogging the filter. Both culture methods exhibited similar profiles of cell density and metabolite concentrations during the culture period at the cell concentration of around 1×10⁷ cells/mL. When the perfusion rate was increased, the intermittent bleeding culture showed problems of ammonia accumulation and decrease of cell viability. The continuous bleeding culture exhibited higher physiological activity than that of the intermittent bleeding culture in terms of nutrient consumption and metabolite production kinetics. But the analysis of specific oxygen consumption rate showed that the specific oxygen consumption rate of intermittent bleeding culture was similar to that of exponential growth phase. The continuous bleeding culture showed higher specific vWF McAb productivity and cumulative production than those of the intermittent bleeding culture. Finally we proved the possibility of long-term operation of continuous bleeding culture and produced approximately 40 g of vWF McAb in a 15 L bioreactor after one-month operation.     

表达抗-CD25单克隆抗体的GS-NS0骨髓瘤细胞无血清培养及代谢特性

抗-CD25单克隆抗体作为免疫抑制剂拥有广阔的市场前景和巨大的经济价值。本实验以表达抗?CD25单克隆抗体的GS-NS0细胞为研究对象,开发了支持其大规模培养和抗体表达的无血清低蛋白培养基,批培养最大活细胞密度和最大抗体浓度分别达3×106cells/mL和300mg/L以上,比商业无血清培养基(Excell 620+0.2% primatone)分别提高了100%和46%。通过批培养实验,研究了细胞的生长、葡萄糖和氨基酸代谢、以及产物表达特点,并揭示了批培养过程中初始葡萄糖浓度对GS-NS0细胞生长与代谢的影响规律。为优化GS-NS0细胞培养过程和抗CD25单抗成功迈向产业化提供了重要的科学依据。     

扩张柱床吸附层析回收纯化灌流培养生产的单克隆抗体

用扩张柱床吸附层析技术,一步回收纯化连续灌流培养的单克隆抗体。用Streamline SP阳离子交换介质在固定床柱XK16/20上进行条件摸索,扩张床柱Streamline25和50分别用于小规模条件优化和中试规模放大。培养液中的低浓度单抗经此步处理,浓缩10倍以上,纯度提高5～7倍,回收率＞90%,制备周期比固定柱床层析缩短一半以上。 根据培养液中单抗浓度的不同,一次处理量为18～50L,纯化规模由实验室水平（400mg）扩大至中试水平（2g）,生产成本和工艺复杂性大为降低。应用扩张柱床吸附层析技术,建立单克隆抗体回收纯化工艺,具有经济、简便、高效实用和良好的可放大性。     

Cardiopulmonary, hemocytologic and biochemical effects of xylazine in goats

Intramuscular administration of xylazine at the rate of 0.22 mg/kg body weight caused a significant reduction in respiratory rates. Mean arterial blood pressure and rectal temperature were not altered. Preadministration of atropine did not affect the depth and pattern of respiration; however, the heart rate increased. A significant reduction in pH and arterial oxygen tension and an increase in carbon dioxide tension was observed after xylazine and xylazine following atropine treatment. Hemocytologic changes included a decrease in total erythrocytes, leukocytes, hematocrit and hemoglobin concentration and a rise in neutrophils with relative decrease in lymphocytes. Biochemical changes included a slight rise in potassium and a decrease in sodium concentration. Glucose level was significantly increased at maximum depth of sedation. The changes in hemocytologic and biochemical parameters returned to near preadministration level in 24-72 hours. No alteration was observed in the electrocardiogram. Xylazine was well tolerated, and the sedation was rapid in onset and lasted for about 30 minutes. The recovery was uneventful.     

Comparison of different ligand densities for the manufacture of CB Hep-1 immunosorbents

Different ligand densities of monoclonal antibody (Mab) CB.Hep-1 were studied during covalent coupling on Sepharose CL-4B for recombinant hepatitis B surface antigen (rHBsAg) immunoaffinity purification. Ligand densities of 2.2, 3.2, 4.2 and 5.2 mg Mab/ml immunosorbents, respectively, were assayed during five cycles of immunoaffinity chromatography (IAC). Adsorption capacities averaged either 3.2 mg/ml (0.57 mg rHBsAg/ml immunosorbent/5.42 mg of total purified protein) or 5.2 mg/ml (0.56 mg rHBsAg/ml immunosorbent/5.05 mg total purified protein). Immunosorbents showed ligand leakage levels below 3 ng Mab/microg rHBsAg. Antigen purity was higher than 95% in all cases. The results suggest that a ligand density (LD) of 3.2 mg Mab/ml immunosorbent should be used for immunoaffinity chromatography because no significant differences were found in the ligand densities studied (P-value=0.012), which saves 40% of CB.Hep-1 immunosorbent manufacturing cost in comparison with 5 mg Mab/ml immunosorbent, which is currently used in large-scale production.     

Transfer of monoclonal antibodies into mammalian cells by electroporation

A simple rapid and reproducible procedure for transferring monoclonal antibodies into mammalian cells by electroporation is described. Two functionally different monoclonal antibodies (Mab 3F3 and Mab 2B4) specific for asparagine synthetase (EC 6.3.1.1) were used for electroporation into HeLa, HT-5, and L5178Y D10/R (L-asparaginase-resistant) cells. The conditions were optimized so that the viability of the electroporated cells was very high (80-90%), and 90% of the viable cells had antibody incorporated. Electropermeabilized cells were structurally intact, and the high voltage electric pulse had no inhibitory effect on overall cellular DNA and protein synthesis. Incorporated immunoglobulins showed unaltered structural integrity and were functionally active. L5178Y D10/R cells incorporated with an antibody (Mab 3F3) known to be a potent inhibitor of tumor asparagine synthetase showed increased dependence on an exogenous source of asparagine in the culture medium, while the growth of cells incorporated with a control (noninhibitory) antibody (Mab 2B4) remained unaffected. These studies demonstrate that electroporation can be employed successfully for large scale transfer of antibodies into cultured mammalian cells for the study of cellular metabolism.     

Antifungal and antitumor activities of a monoclonal antibody directed against a stress mannoprotein of Candida albicans

Immunization of mice with a stress mannoprotein of >200 kDa from the cell wall of Candida albicans led to the production of monoclonal antibody (Mab) C7. The immunogen is a major target of secretory IgA and its expression is regulated by different environmental conditions including temperature, pH, glucose concentration and ammonium sulphate in the culture medium. Mab C7 reacted with a peptide epitope present in the >200 kDa antigen as well as in a number of antigens from the blastoconidium and germ tube cell wall, including enolase. In addition to its reactivity with C. albicans, Mab C7 also reacted with antigens present in C. krusei, C, tropicalis, C. glabrata, C. dubliniensis and C. lusitaniae, as well as in Cryptococcus neoformans, Scedosporium prolificans and Aspergillus fumigatus. Mab C7 exhibited four important biological activities, namely inhibition of adhesion of C. albicans to a variety of surfaces, inhibition of germination of C. albicans, direct candidacidal activity and direct tumoricidal activity. In tumor cells, Mab C7 reacted with nucleoporin Nup88, a reactivity that can be utilized for diagnostic and prognostic purposes.     

Physiology and morphology of Legionella pneumophila in continuous culture at low oxygen concentration.

Two strains of Legionella pneumophila serogroup 1 monoclonal subgroup Pontiac were grown for the first time in continuous culture using a chemically defined medium. The influence of temperature on physiology and morphology was investigated by fixing the growth rate (equal to the dilution rate, D) at 0.08 h-1 and controlling the pH and dissolved oxygen concentration of the culture. Serine provided the principal source of carbon and energy but growth was limited by tyrosine. The bacterium behaved as a microaerophile in this medium, with maximal growth occurring at 0.31 (mg O2)I-1 (equivalent to a dissolved oxygen tension of 4% (v/v) air saturation at 30 degrees C). The cultures consisted of flagellated, short rods at 24 degrees C, but exhibited an increased level of pleomorphism and the loss of flagella as the temperature was increased to 37 degrees C. The presence of intracellular granules was noted, and their abundance was temperature-dependent. Polyhydroxybutyrate was present in L. pneumophila, and the proportion of the cell dry weight that it accounted for varied with temperature, being maximal at 24 degrees C. The ratio of saturated to unsaturated fatty acids in the cells decreased as the temperature was reduced towards 24 degrees C, so as to maintain membrane fluidity at low growth temperature.     

Tumor oxygenation and acidification are increased in melanoma xenografts after exposure to hyperglycemia and meta-iodo-benzylguanidine

Tumor oxygen tension and extracellular pH (pH(e)) are physiological parameters that can be manipulated to improve current cancer therapies. Many human tumors consist of cells that are chronically exposed to low pH(e). Exposure of tumor cells in culture to glucose decreases oxygen consumption (oxygen sparing or Crabtree effect), and while this effect is absent in low pH-adapted tumor cells, it can be restored by combining the respiratory inhibitor meta-iodo-benzylguanidine (MIBG) with glucose (Burd et al., Cancer Res. 61, 5630-5635, 2001). The effects of hyperglycemia and MIBG on tumor oxygen tension and on pH(e) were investigated in human melanoma xenografts in SCID mice. An oral gavage of 1 M glucose (2 g/kg) increased the average blood glucose concentration from <140 mg/dl to approximately 400 mg/dl. Although tumor pH(e) decreased from pH 6.7 to pH 6.5 (P < 0.01) after about 60 min, no change in tumor oxygen tension was observed. However, when oral glucose and MIBG (15 mg/kg) were administered together, oxygen tension increased from 2.8 mmHg to approximately 17 mmHg, and tumor pH(e) decreased from pH 6.7 to pH 6.3 (P < 0.01) after about 115 min. In conclusion, administration of glucose together with MIBG increases tumor oxygen tension and also increases the magnitude and duration of acidification. Hyperglycemia plus MIBG has the potential to improve response to radiation therapy as well as to hyperthermia and some chemotherapies.     

Rapid protein production using CHO stable transfection pools

During early preclinical development of therapeutic proteins, representative materials are often required for process development, such as for pharmacokinetic/pharmacodynamic studies in animals, formulation design, and analytical assay development. To rapidly generate large amounts of representative materials, transient transfection is commonly used. Because of the typical low yields with transient transfection, especially in CHO cells, here we describe an alternative strategy using stable transfection pool technology. Using stable transfection pools, gram quantities of monoclonal antibody (Mab) can be generated within 2 months post‐transfection. Expression levels for monoclonal antibodies can be achieved ranging from 100 mg/L to over 1000 mg/L. This methodology was successfully scaled up to a 200 L scale using disposable bioreactor technology for ease of rapid implementation. When fluorescence‐activated cell sorting was implemented to enrich the transfection pools for high producers, the productivity could be improved by about three‐fold. We also found that an optimal production time window exists to achieve the highest yield because the transfection pools were not stable and productivity generally decreased over length in culture. The introduction of Universal chromatin‐opening elements elements into the expression vectors led to significant productivity improvement. The glycan distribution of the Mab product generated from the stable transfection pools was comparable to that from the clonal stable cell lines. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Evaluation of startup and operation of four anaerobic processes treating a synthetic meat waste

Two continuous stirred tanks reactors (CSTR) and four anaerobic fluidized bed reactors (AFBR) were used to study the treatment of a synthetic meat waste during single-and two-stage anaerobic treatment. Four configurations were investigated; a single-stage CSTR and AFBR and the two-stage systems CSTR-AFBR and AFBR-AFBR. Startup of the anaerobic reactors was achieved within 50 days by use of a regime that included stepped increases in influent COD, methanol substitution of the substrate, and addition of essential trace metals such as cobalt and nickel. Two-stage reactors removed up to 85% of influent COD concentrations of 5000 mg/L, whereas the single-stage AFBR and CSTR removed 76 and 9%, respectively. The proportion of methane in the effluent gases increased as the influent COD concentration was increased. Volumetric production of methane was greatest for the first stage of the AFBR-AFBR system. Solids retention times calculated for the AFBRs ranged from 7 to 12 days, sufficient to support methanogenesis. The AFBRs and two-stage systems were more resistant to an influent pH shock from the operating value of pH 6.8 down to pH 3 than the CSTRs and single-stage reactors. It was concluded that high-rate anaerobic treatment systems were applicable to meat industry wastewaters and that two-stage digestion produced a better quality effluent.     

Application of a cell-once-through perfusion strategy for production of recombinant antibody from rCHO cells in a Centritech Lab II centrifuge system

Based upon the results of scale-down intermittent perfusion processes, a cell-once-through (COT) perfusion concept was applied to a dual bioreactor system coupled to a Centritech Lab II centrifuge for culture of recombinant Chinese hamster ovary (rCHO) cells for monoclonal antibody production. In this new culture mode, i.e., the COT perfusion process, total spent medium was transferred to the centrifuge and a fixed percentage was removed. Approximately 99% of the viable cells are transferred to another bioreactor filled with fresh medium by single operation of the Centritech Lab II centrifuge system for about 30 min. Accordingly, a significant reduction of the cell-passage frequency to the centrifuge led to minimization of cell damage caused by mechanical shear stress, oxygen limitation, nutrient limitation, and low temperature outside the bioreactor. The effects of culture temperature shift and fortified medium on cell growth and recombinant antibody production in the COT perfusion process were investigated. Although the suppressive effects of low culture temperature on cell growth led to a loss of stability in a long-term COT perfusion culture system, the average antibody concentration at 33 degrees C was 157.8 mg/L, approximately 2.4-fold higher than that at 37 degrees C. By the use of a fortified medium at 37 degrees C, rCHO cells were maintained at high density above 1.2 x 10(7) cells/mL, and antibody was produced continuously in a range of 260-280 mg/L in a stable long-term COT perfusion culture. The proposed new culture mode, the COT perfusion approach, guarantees the recovery of rCHO cells damaged by lowered temperature or high lactate and ammonium concentration. It will be an attractive choice for minimization of cell damage and stable long-term antibody production with high cell density.