Temperature-induced production of recombinant human insulin in high-cell density cultures of recombinant Escherichia coli

被引:51
作者
Schmidt, M
Babu, KR
Khanna, N
Marten, S
Rinas, U
机构
[1] GBF Natl Res Ctr Biotechnol, Div Biochem Engn, D-38124 Braunschweig, Germany
[2] Aruna Asaf Ali Marg, Int Ctr Genet Engn & Biotechnol, New Delhi 110067, India
关键词
human insulin; high-cell density cultivation; recombinant Escherichia coli; temperature-inducible expression;
D O I
10.1016/S0168-1656(98)00189-8
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
The construction of expression vectors encoding either the human insulin A- or B-chains fused to a synthetic peptide and the temperature-induced expression of the recombinant genes in Escherichia coli are reported. Using this two-chain approach we also describe the separate isolation of the insulin A- and B-chains from inclusion bodies and their subsequent assembly into native human insulin. The production of the insulin fusion proteins were carried out in high-cell density fed-batch cultures using a synthetic medium with glucose as sole carbon and energy source. The expression of the recombinant genes by temperature-shift in high-cell density cultures of recombinant E. coli resulted in product yields of grams per litre of culture broth, e.g. 4.5 g of insulin B-chain fusion protein per litre of culture broth. This translates into an expression yield of about 800 mg of the insulin B-chain per litre of culture. Under similar cultivation conditions the expression yield of the insulin A-chain corresponds to approximately 600 mg per litre of culture. The metabolic burden imposed on the recombinant cells during temperature-induced production of insulin fusion proteins in high-cell density cultures is reflected in an increased respiratory activity and a reduction of the biomass yield coefficient with respect to glucose. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:71 / 83
页数:13
相关论文
共 23 条
[1]   Method for increasing the yield of properly folded recombinant human gamma interferon from inclusion bodies [J].
Arora, D ;
Khanna, N .
JOURNAL OF BIOTECHNOLOGY, 1996, 52 (02) :127-133
[2]   Expression and folding of an interleukin-2-proinsulin fusion protein and its conversion into insulin by a single step enzymatic removal of the C-peptide and the N-terminal fused sequence [J].
CastellanosSerra, LR ;
Hardy, E ;
Ubieta, R ;
Vispo, NS ;
Fernandez, C ;
Besada, V ;
Falcon, V ;
Gonzalez, M ;
Santos, A ;
Perez, G ;
Silva, A ;
Herrera, L .
FEBS LETTERS, 1996, 378 (02) :171-176
[3]  
Chance R. E., 1981, PEPTIDES SYNTHESIS S, P721
[4]   PREPARATIVE ISOLATION BY HIGH-PERFORMANCE LIQUID-CHROMATOGRAPHY OF HUMAN INSULIN-B CHAIN PRODUCED IN ESCHERICHIA-COLI [J].
CRUZ, N ;
ANTONIO, S ;
DEANDA, R ;
GOSSET, G ;
BOLIVAR, F .
JOURNAL OF LIQUID CHROMATOGRAPHY, 1990, 13 (08) :1517-1528
[5]   PREPARATIVE ISOLATION OF RECOMBINANT HUMAN INSULIN-A CHAIN BY ION-EXCHANGE CHROMATOGRAPHY [J].
CRUZ, N ;
LOPEZ, M ;
ESTRADA, G ;
ALVARADO, X ;
DEANDA, R ;
BALBAS, P ;
GOSSET, G ;
BOLIVAR, F .
JOURNAL OF LIQUID CHROMATOGRAPHY, 1992, 15 (13) :2311-2324
[6]   GRATUITOUS OVEREXPRESSION OF GENES IN ESCHERICHIA-COLI LEADS TO GROWTH-INHIBITION AND RIBOSOME DESTRUCTION [J].
DONG, HJ ;
NILSSON, L ;
KURLAND, CG .
JOURNAL OF BACTERIOLOGY, 1995, 177 (06) :1497-1504
[7]   SYNTHESIS OF HUMAN INSULIN GENE .8. CONSTRUCTION OF EXPRESSION VECTORS FOR FUSED PROINSULIN PRODUCTION IN ESCHERICHIA-COLI [J].
GUO, LH ;
STEPIEN, PP ;
TSO, JY ;
BROUSSEAU, R ;
NARANG, S ;
THOMAS, DY ;
WU, R .
GENE, 1984, 29 (1-2) :251-254
[8]   HUMAN INSULIN FROM RECOMBINANT DNA TECHNOLOGY [J].
JOHNSON, IS .
SCIENCE, 1983, 219 (4585) :632-637
[9]   Single-step trypsin cleavage of a fusion protein to obtain human insulin and its C peptide [J].
Jonasson, P ;
Nilsson, J ;
Samuelsson, E ;
Moks, T ;
Stahl, S ;
Uhlen, M .
EUROPEAN JOURNAL OF BIOCHEMISTRY, 1996, 236 (02) :656-661
[10]   SIMPLE FED-BATCH TECHNIQUE FOR HIGH CELL-DENSITY CULTIVATION OF ESCHERICHIA-COLI [J].
KORZ, DJ ;
RINAS, U ;
HELLMUTH, K ;
SANDERS, EA ;
DECKWER, WD .
JOURNAL OF BIOTECHNOLOGY, 1995, 39 (01) :59-65