Fed-batch production of L-phenylalanine from glycerol and ammonia with recombinant Escherichia coli

被引:43
|
作者
Weiner, Michael [1 ]
Albermann, Christoph [2 ]
Gottlieb, Katrin [2 ]
Sprenger, Georg A. [2 ]
Weuster-Botz, Dirk [1 ]
机构
[1] Tech Univ Munich, Lehrstuhl Bioverfahrenstech, Garching, Germany
[2] Univ Stuttgart, Inst Mikrobiol, Stuttgart, Germany
关键词
L-Phenylalanine; Glycerol; Escherichia coli; Fed-batch; Plasmid stability; BIOMASS CONCENTRATION; CRUDE GLYCEROL; PHOSPHOENOLPYRUVATE; INACTIVATION; FACILITATOR; METABOLISM; GLUCOSE; ENZYMES; GROWTH; GENES;
D O I
10.1016/j.bej.2013.12.001
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
Glycerol was used as carbon source for L-phenylalanine production with recombinant Escherichia coli. In contrast to glucose, no consumption of the precursor phosphoenolpyruvate (PEP) is necessary for glycerol uptake. Additional lactic acid feeding was necessary for growth because the genes encoding the PEP consuming pyruvate kinase isoenzymes have been deleted. Thus a fed-batch process was developed with feeding of lactic acid and glycerol for biomass formation followed by feeding of glycerol and ammonia for L-phenylalanine production. Unfortunately, plasmid instability was observed in the first process. Plasmid stability could be successfully assured by replacing an ampicillin resistance gene by a kanamycin resistance gene cassette. The resulting maximum L-phenylalanine concentration of 13.4 g L-1 was improved by 26% and biomass specific productivity (22 mg(L-phe) g(CDW)(-1)h(-1)) was raised by 69%. The final L-phenylalanine concentration of 13.4g L-1 was thus improved by a factor of 2.4 compared to earlier reports. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:62 / 69
页数:8
相关论文
共 50 条
  • [31] Production of β-carotene by recombinant Escherichia coli with engineered whole mevalonate pathway in batch and fed-batch cultures
    Jung Hun Kim
    Seon-Won Kim
    Do Quynh Anh Nguyen
    He Li
    Sung Bae Kim
    Yang-Gon Seo
    Jae-Kyung Yang
    In-Young Chung
    Dae Hwan Kim
    Chang-Joon Kim
    Biotechnology and Bioprocess Engineering, 2009, 14 : 559 - 564
  • [32] Run-to-run fed-batch optimization for protein production using recombinant Escherichia coli
    Ko, Chih-Lung
    Wang, Feng-Sheng
    BIOCHEMICAL ENGINEERING JOURNAL, 2006, 30 (03) : 279 - 285
  • [33] Constitutive production of human leptin by fed-batch culture of recombinant rpoS- Escherichia coli
    Jeong, KJ
    Choi, JH
    Yoo, WM
    Keum, KC
    Yoo, NC
    Lee, SY
    Sung, MH
    PROTEIN EXPRESSION AND PURIFICATION, 2004, 36 (01) : 150 - 156
  • [34] A simple feedback control of Escherichia coli growth for recombinant aldolase production in fed-batch mode
    Pinsach, J
    de Mas, C
    López-Santín, J
    BIOCHEMICAL ENGINEERING JOURNAL, 2006, 29 (03) : 235 - 242
  • [35] PRODUCTION OF POLY-BETA-HYDROXYBUTYRATE BY FED-BATCH CULTURE OF RECOMBINANT ESCHERICHIA-COLI
    KIM, BS
    LEE, SY
    CHANG, HN
    BIOTECHNOLOGY LETTERS, 1992, 14 (09) : 811 - 816
  • [36] A decreasing feeding profile for the optimization of ethanol production in a recombinant Escherichia coli fed-batch fermentation
    Saucedo, VM
    Karim, MN
    BIOTECHNOLOGY LETTERS, 1996, 18 (09) : 1055 - 1060
  • [37] Metabolic footprinting of Escherichia coli grown in fed-batch fermentation during recombinant protein production
    Carneiro, S.
    Villas-Boas, S.
    Rocha, I.
    Ferreira, E. C.
    NEW BIOTECHNOLOGY, 2009, 25 : S342 - S342
  • [38] Regulation of trp promoter for production of bovine somatotropin in recombinant Escherichia coli fed-batch fermentation
    Yoon, SK
    Kang, WK
    Park, TH
    JOURNAL OF FERMENTATION AND BIOENGINEERING, 1996, 81 (02): : 153 - 157
  • [39] Fed-Batch Process for Pyruvate Production by Recombinant Escherichia coli YYC202 Strain
    Zelic, B.
    Gerharz, T.
    Bott, M.
    Vasic-Racki, D.
    Wandrey, C.
    Takors, R.
    ENGINEERING IN LIFE SCIENCES, 2003, 3 (07): : 299 - 305
  • [40] Modeling of the pyruvate production with Escherichia coli in a fed-batch bioreactor
    B. Zelić
    Đ. Vasić-Rački
    C. Wandrey
    R. Takors
    Bioprocess and Biosystems Engineering, 2004, 26 : 249 - 258