Metabolic characteristics of GS-NS0 Myeloma cells producing anti-cd25 monoclonal antibody in serum-free culture

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生物工程学报 Chin J Biotech 2009, July 25; 25(7): 1069-1076 journals.im.ac.cn Chinese Journal of Biotechnology ISSN 1000-3061 cjb@im.ac.cn 2009 Institute of Microbiology, CAS & CSM, All rights reserved 组织工程与细胞培养 -CD25 GS-NS0 赵亮, 范里, 张旭, 谭文松, 200237 : 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 10 6 cells/ml 和 300 mg/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 : GS-NS0 细胞, 无血清培养基, 抗 CD25 单克隆抗体, 代谢特性 Metabolic characteristics of GS-NS0 Myeloma cells producing anti-cd25 monoclonal antibody in serum-free culture Liang Zhao, Li Fan, Xu Zhang, and Wensong Tan State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China Abstract: As an immunodepressant, anti-cd25 monoclonal antibody has a huge market with wide prospect and economic value. We developed a low protein serum-free medium for large-scale GS-NS0 myeloma cell culture and anti-cd25 monoclonal antibody production. Further study focused on the characteristics of GS-NS0 cell growth, glucose and amino acid metabolism, and antibody production. In the serum-free medium, the maximal viable cell density and antibody concentration reached above 3 10 6 cells/ml and 300 mg/l in batch culture. Compared with the commercial serum-free medium (Excell 620 + 0.2% Primatone), the maximal viable cell density doubled and the maximal antibody concentration increased 46%. Results also showed the specific growth rate decreased when the glucose concentration was lower than 6 mmol/l. And the production of lactate increased when glucose concentration was excessively high (>30 mmol/l). These results were important to provide technique and theory basis for developing optimized GS-NS0 cell culture and anti-cd25 monoclonal antibody production processes. Keywords: GS-NS0 cell, serum-free medium, anti-cd25 monoclonal antibody, metabolic characteristics Anti-CD25(IL-2Rα) T 1992 Hiesse Anti-CD25 ( LO-TACT-1) Received: March 12, 2009; Accepted: May 11, 2009 Supported by: National Natural Science Foundation of China (No. 20706016). Corresponding author: Wensong Tan. Tel: +86-21-64250948; Fax: +86-21-64252250; E-mail: wstan@ecust.edu.cn 国家自然科学基金项目 (No. 20706016) 资助

1070 ISSN1000-3061 CN11-1998/Q Chin J Biotech July 25, 2009 Vol.25 No.7 [1] LO-Tact-1, [2,3],, LO-Tact-1 2,,,, GS-NS0 NS0 [4] [5,6] [7,8],,, Anti-CD25 GS-NS0, Technopharm Anti-CD25 ( LO-TACT-1) GS-NS0, GS-NS0, GS-NS0 CD25, GS, 1 材料与方法 1.1 细胞株 GS-NS0, CD25 LO-Tact-1 [9], 1.2 培养基 DMEM/F12(1:1), HEPES Pluronic F68,, Millipore 0.1 μm Sigma-Aldrich 1.3 细胞培养系统和培养方法 1.3.1 GS-NS0, 2 10 5 ~ 3 10 5 cells/ml, 36.8 o C 5% CO 2, 50 r/min, 1.3.2 GS-NS0, 1200 r/min 5 min,, 4 10 5 ~ 5 10 5 cells/ml, 60 ml, 36.8 o C 5% CO 2, 50 r/min 12 h,, 3000 r/min 10 min, 1.3.3 GS-NS0, 1200 r/min 5 min,, 4 10 5 ~ 5 10 5 cells/ml (2 L BIOSTAT B, B.Braun, MFCS/win1.1), 2 L : ph (7.0 ± 0.1), DO 50%, 36.8 o C, 50 r/min 12 h,, 3000 r/min 10 min, 1.4 测定和分析方法 1.4.1 1.5 ml 24, 0.4%,, 3, 1.4.2 GOD-POD ( ) :,, 4-, 505 nm (

: Anti-CD25 GS-NS0 1071 ) : NAD +, LDH, NAD + NADH, (PMS) (NBT), 530 nm Berthelot ( ),, 5 mmol/l NH 4 Cl :,, 550 nm 1.4.3 Waters AccQ Tag, (1525 Binary HPLC pump, 717plus Autosampler, 2487 Dual λ absorbance detector, Nova-Pak C18 4 μm 3.9 mm 150 mm column, Waters), 1.4.4 ELISA [10] 1:200 IgG1, 100 μl/ 96, 37 o C 2 h 4 o C (16~18 h) 3,, 200 μl/, 37 o C 2 h 3, 5 min/ 100 μl/, 37 o C 1 h 3, 5 min/ 1:500 HRP- Kappa, 100 μl/, 37 o C 1 h 10, 5 min/ 100 μl/ TMB, 5 min, 50 μl/, 450 nm, 655 nm Zymed 2 结果与讨论 2.1 混合脂添加剂对 GS-NS0 细胞生长的影响 NS0 [11], [11 13], NS0, NS0, NS0-I3 ( E ) 1 CLC(Gibco) NS0-I3 GS-NS0 图 1 混合脂添加剂对 GS-NS0 细胞生长的影响 Fig. 1 Effect of complex lipids on GS-NS0 cell growth.,,, CLC NS0-I3, NS0-I3,, CLC, 0.5 d 1 2.2 无血清低蛋白培养基开发 DMEM/F12 (1:1), (Insulin) (Transferrin) NS0-I3, GS-NS0, LP3.6,, 10 mg/l, 2b LP3.6 GS-NS0,,,,,,, (Excell 620 + 0.2% Primatone) ( 2a) LP3.6 GS-NS0, 0.75 d 1 3.47 10 6 cells/ml 307 mg/l, (Excell 620 + 0.2%

1072 ISSN1000-3061 CN11-1998/Q Chin J Biotech July 25, 2009 Vol.25 No.7 Primatone) 114% 103% 46%, 30%, ( 1) ;, 2.3.2 (15~58 h),, 4 Y Lac/Gluc 1.23 mmol/mmol, 60% 图 2 GS-NS0 细胞在 Excell 620 和 LP3.6 培养基中的形态 Fig. 2 Morphology of GS-NS0 cells cultivated in Excell 620 and LP3.6 (40 ). 表 1 Excell620 和 LP3.6 培养基中细胞生长和产物表达 Table 1 Cell growth and antibody production in Excell 620 and LP3.6 media Excell 620 LP3.6 X v max (10 6 cells/ml) 1.62 3.47 μ (1/d) 0.37 0.75 Duration (h) 168 117 IVC (10 9 cells d/l) 8.17 9.98 Max antibody concentration. (mg/l) 210 307 IVC was calculated until the viability decreased to approximately 50%. 图 3 Fig. 3 GS-NS0 细胞批培养的生长曲线 Growth curve of GS-NS0 cells in batch culture. 2.3 GS-NS0 细胞的生长 代谢及抗体表达 2.3.1 3 GS-NS0 2 L 0.51 10 6 cells/ml LP3.6, 91.7%,, 91 h, 3.68 10 6 cells/ml, 3.89 10 6 cells/ml, 0.85 d 1, 0.73 d 1, 图 4 GS-NS0 细胞批培养中的葡萄糖与乳酸代谢 Fig. 4 Metabolism of glucose and lactate in batch culture of GS-NS0 cells., 69 h, 5 mmol/l,,,,

: Anti-CD25 GS-NS0 1073, 2.3.3 GS, ;, α-, ( ) α- ( ), α- GS-NS0,, 5,,, 2 mmol/l,,, 1.90 mmol/l, 1.5, 3 mmol/l,,,, GS-NS0,,, (Tyr) (Cys) (His) (Met) (Phe) (Lys) (Trp) (Val) (Thr) (Arg) (Leu) (Ile),, (Ala) (Gly) (Asp) (Asn) (Pro) (Ser) 6,,,, 图 6 Fig. 6 批培养过程中的其他氨基酸浓度变化 Concentrations of amino acids in batch culture. 图 5 批培养过程中谷氨酸 谷氨酰胺 氨和丙氨酸的浓度变化 Fig. 5 Concentrations of glutamate, glutamine, ammonia, and alanine in batch culture. 0.91 mmol/(10 9 cells d), 0.58 mmol/(10 9 cells d) 2,, 0.15 mmol/(10 9 cells d),,, 0.23 mmol/(10 9 cells d) 2.3.4, 69 h,,,, 301 mg/l

1074 ISSN1000-3061 CN11-1998/Q Chin J Biotech July 25, 2009 Vol.25 No.7, IVC ( 7),, (R 2 = 0.9826),, 24.4 mg/(10 9 cells d) GS-NS0 CD25,, (IVC), 表 2 批培养过程中氨基酸的比消耗速率 Table 2 Specific rates of amino acids in batch culture Amino acids Sp. rate Amino acids Sp. rate Asp 0.131 Arg 0.189 Glut 0.913 Ala 0.225 Gly 0.142 Pro 0.084 Gln 0.575 Tyr 0.088 Met 0.059 Lys 0.207 Ile 0.051 Phe 0.072 Lue 0.167 Trp 0.022 His 0.053 Cys2 0.100 Thr 0.193 Val 0.188 Unit: mmol/(10 9 cells d). (Batch-1) 24 mmol/l(batch-2) 66 mmol/l (Batch-3),,, NaCl KCl, 3 Batch-1,, 1.72 10 6 cells/ml; Batch-2,, ; Batch-3,,, 4.26 10 6 cells/ml,, 表 3 各批批培养的细胞生长 代谢和产物表达 Table 3 Growth, metabolism, and antibody production of GS-NS0 cells in batches Batch-1 Batch-2 Batch-3 X vmax (10 6 cells/ml) 1.72 3.68 4.26 μ (1/d) 0.66 0.73 0.81 IVC (10 9 cells d/l) 3.80 11.28 9.00 Max antibody conc. (mg/l) 102.5 301.1 253.9 q Gluc (mmol/(10 9 cells d)) 7.63 7.18 5.47 q Lac (mmol/(10 9 cells d)) 11.13 9.32 14.42 Y Lac/Gluc (mmol/mmol) 1.46 1.30 2.83 q Antibody (mg/(10 9 cells d)) 24.1 24.4 24.1 图 7 批培养过程中的抗体累积生成量与 IVC 的关系 Fig. 7 Relationship of cumulative antibody production and IVC in batch culture. 2.3.5 GS-NS0 2 L,, GS-NS0 15 mmol/l, 8 GS-NS0, 6 mmol/l, GS-NS0, 0.66 ~ 0.81 d 1 6 mmol/l,,, ( 9),

: Anti-CD25 GS-NS0 1075,, Batch-3 Batch-2, IVC Batch-2,, 24 mg/(10 9 cells d), IVC, IVC Batch-2,, 301 mg/l, 3 结论 图 8 葡萄糖浓度对 GS-NS0 细胞比生长速率的影响 Fig. 8 Effect of glucose concentration on specific growth rate of GS-NS0 cells. 图 9 葡萄糖浓度对葡萄糖比消耗速率的影响 Fig. 9 Effect of glucose concentration on specific glucose consumption rate. 5.47~7.63 mmol/(10 9 cells d), GS-NS0, (Batch-3),, 14.42 mmol/(10 9 cells d) Batch-1 Batch-2 24 mmol/l,, 1.30~1.46 mmol/mmol ; Batch-3, 30 mmol/l, 2, Batch-1 Batch-2 2,,, Batch-3 47.7 mmol/l, GS-NS0, LP3.6,,, 10 mg/l, GS-NS0 GS-NS0 CHO,, GS-NS0 6 mmol/l,,, 6 mmol/l,, 24 mmol/l,, (>30 mmol/l), CD25,, 24 mg/ (10 9 cells d), IVC,, REFERENCES [1] Hiesse C, Lantz O, Kriaa F, et al. Treatment with Lo-Tact-1, a monoclonal antibody to the interleukin-2 receptor, in kidney transplantation. Presse Med, 1991, 20(40): 2036 2038.

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