IN PURSUIT OF THE OPTIMAL FED-BATCH PROCESS FOR MONOCLONAL-ANTIBODY PRODUCTION

被引:181
作者
BIBILA, TA [1 ]
ROBINSON, DK [1 ]
机构
[1] MERCK RES LABS,DEPT CELLULAR & MOLEC BIOL,RAHWAY,NJ 07065
关键词
D O I
10.1021/bp00031a001
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Fed-batch culture currently represents the most attractive choice for large scale production of monoclonal antibodies (MAbs), due to its operational simplicity, reliability, and flexibility for implementation in multipurpose facilities. Development of highly productive cell lines, maximization of cell culture longevity, and maintenance of high specific antibody secretion rates through genetic engineering techniques, nutrient supplementation, waste product minimization, and control Of environmental conditions are important for the design of high-yield fed-batch processes. Initially simple supplementation protocols have evolved into sophisticated serum-free multinutrient feeds that result in MAb titers on the order of 1-2 g/L. Limited research has been published to date on the effects of various culture parameters on potentially important quality issues, such as MAb glycosylation and stability. Although most fed-batch protocols to date have relied on relatively simple control schemes, increasingly sophisiticated algorithms must be applied in order to take full advantage of the potentially additive effects of manipulating nutrient and environmental parameters to maximize fed-batch process productivity.
引用
收藏
页码:1 / 13
页数:13
相关论文
共 156 条
[1]  
ANUINS JG, 1993, BIOPROCESSING, V3, P223
[2]  
AUBERSON LCM, 1991, 1991 AM I CHEM ENG A, P502
[3]   HUMAN MONOCLONAL-ANTIBODIES NEUTRALIZING CYTOMEGALOVIRUS (CMV) FOR PROPHYLAXIS OF CMV DISEASE - REPORT OF A PHASE-I TRIAL IN BONE-MARROW TRANSPLANT RECIPIENTS [J].
AULITZKY, WE ;
SCHULZ, TF ;
TILG, H ;
NIEDERWIESER, D ;
LARCHER, K ;
OSTBERG, L ;
SCRIBA, M ;
MARTINDALE, J ;
STERN, AC ;
GRASS, P ;
MACH, M ;
DIERICH, P ;
HUBER, C .
JOURNAL OF INFECTIOUS DISEASES, 1991, 163 (06) :1344-1347
[4]   SIMULATION OF ANIMAL-CELL METABOLISM [J].
BARFORD, JP ;
PHILLIPS, PJ ;
HARBOUR, C .
CYTOTECHNOLOGY, 1992, 10 (01) :63-74
[5]  
BARFORD JP, 1992, ANIMAL CELL TECHNOLOGY : BASIC & APPLIED ASPECTS, VOL 4, P397
[6]  
BARTLEY A, 1992, ANIMAL CELL TECHNOLOGY : DEVELOPMENTS, PROCESSES AND PRODUCTS, P376
[7]   A STRUCTURED KINETIC MODELING FRAMEWORK FOR THE DYNAMICS OF HYBRIDOMA GROWTH AND MONOCLONAL-ANTIBODY PRODUCTION IN CONTINUOUS SUSPENSION-CULTURES [J].
BATT, BC ;
KOMPALA, DS .
BIOTECHNOLOGY AND BIOENGINEERING, 1989, 34 (04) :515-531
[8]   INCLINED SEDIMENTATION FOR SELECTIVE RETENTION OF VIABLE HYBRIDOMAS IN A CONTINUOUS SUSPENSION BIOREACTOR [J].
BATT, BC ;
DAVIS, RH ;
KOMPALA, DS .
BIOTECHNOLOGY PROGRESS, 1990, 6 (06) :458-464
[9]  
BATT BC, 1991, THESIS U COLORADO
[10]  
BEBBINGTON CR, 1990, BIOTECHNOLOGY, V10, P169