Application of Continuous Culture Methods to Recombinant Protein Production in Microorganisms
暂无分享,去创建一个
[1] Brigitte Gasser,et al. The vitamin‐sensitive promoter PTHI11 enables pre‐defined autonomous induction of recombinant protein production in Pichia pastoris , 2016, Biotechnology and bioengineering.
[2] Y. P. Khasa,et al. Kinetic studies of constitutive human granulocyte-macrophage colony stimulating factor (hGM-CSF) expression in continuous culture of Pichia pastoris , 2007, Biotechnology Letters.
[3] Ian W. Marison,et al. Quantitative characterization of the regulation of the synthesis of alcohol oxidase and of the expression of recombinant avidin in a Pichia pastoris Mut+ strain , 2006 .
[4] Alois Jungbauer,et al. Continuous downstream processing of biopharmaceuticals. , 2013, Trends in biotechnology.
[5] T. Hwa,et al. Interdependence of Cell Growth and Gene Expression: Origins and Consequences , 2010, Science.
[6] R. Takors,et al. Human Chymotrypsinogen B Production with Pichiapastoris by Integrated Development of Fermentation and Downstream Processing. Part 1. Fermentation , 2001, Biotechnology progress.
[7] Massimo Morbidelli,et al. Continuous integrated manufacturing of therapeutic proteins. , 2018, Current opinion in biotechnology.
[8] G. Robson,et al. Effect of pH on hen egg white lysozyme production and evolution of a recombinant strain of Aspergillus niger. , 1999, Journal of biotechnology.
[9] Kaspar Valgepea,et al. Advanced continuous cultivation methods for systems microbiology. , 2015, Microbiology.
[10] J. Pronk,et al. Effect of Specific Growth Rate on Fermentative Capacity of Baker’s Yeast , 1998, Applied and Environmental Microbiology.
[11] R. Vilu,et al. Use of Mother-Daughter Multi-Bioreactor Systems for Studies of Steady State Microbial Growth Space. Ema-tütre multireaktorite süsteemide kasutamine mikroorganismide püsiseisundis kasvuruumi uurimisel , 2017 .
[12] C. Wittmann,et al. Effect of different carbon sources on central metabolic fluxes and the recombinant production of a hydrolase from Thermobifida fusca in Bacillus megaterium. , 2007, Journal of biotechnology.
[13] Matthias G Steiger,et al. In Pichia pastoris, growth rate regulates protein synthesis and secretion, mating and stress response , 2013, Biotechnology journal.
[14] K. Valgepea,et al. Escherichia coli achieves faster growth by increasing catalytic and translation rates of proteins. , 2013, Molecular bioSystems.
[15] A. Daugulis,et al. A rational approach to improving productivity in recombinant Pichia pastoris fermentation. , 2001, Biotechnology and bioengineering.
[16] H. Bremer. Modulation of Chemical Composition and Other Parameters of the Cell by Growth Rate , 1999 .
[17] A. Novick,et al. Description of the chemostat. , 1950, Science.
[18] P. Hyka,et al. Use of a mixture of glucose and methanol as substrates for the production of recombinant trypsinogen in continuous cultures with Pichia pastoris Mut+. , 2012, Journal of biotechnology.
[19] Brigitte Gasser,et al. Versatile modeling and optimization of fed batch processes for the production of secreted heterologous proteins with Pichia pastoris , 2006, Microbial cell factories.
[20] K. Mukherjee,et al. Kinetic studies of recombinant human interferon-alpha (rhIFN-α) expression in transient state continuous cultures , 2005 .
[21] Henry C. Lim,et al. Relieving effects of glycine and methionine from acetic acid inhibition in Escherichia coli fermentation , 1993, Biotechnology and bioengineering.
[22] Martin Dragosits,et al. Recombinant Fab expression and secretion in Escherichia coli continuous culture at medium cell densities: Influence of temperature , 2012 .
[23] Anne Kahru,et al. The computer-controlled continuous culture of Escherichia coli with smooth change of dilution rate (A-stat) , 1995 .
[24] J. Boonstra,et al. Specific production rate of VHH antibody fragments by Saccharomyces cerevisiae is correlated with growth rate, independent of nutrient limitation. , 2005, Journal of biotechnology.
[25] H. Bremer,et al. Effect of the bacterial growth rate on replication control of plasmid pBR322 in Escherichia coli , 1986, Molecular and General Genetics MGG.
[26] P. Galzy,et al. Physiological approach to heterologous human serum albumin production by Kluyveromyces lactis in chemostat culture , 1994, Yeast.
[27] Dirk Weuster-Botz,et al. A novel milliliter-scale chemostat system for parallel cultivation of microorganisms in stirred-tank bioreactors. , 2015, Journal of biotechnology.
[28] Diethard Mattanovich,et al. Modeling and measuring intracellular fluxes of secreted recombinant protein in Pichia pastoris with a novel 34S labeling procedure , 2011, Microbial cell factories.
[29] J. Nielsen,et al. Flux distributions in anaerobic, glucose-limited continuous cultures of Saccharomyces cerevisiae. , 1997, Microbiology.
[30] L. A. Palomares,et al. Production of recombinant proteins: challenges and solutions. , 2004, Methods in molecular biology.
[31] Martin Dragosits,et al. Reverse engineering of protein secretion by uncoupling of cell cycle phases from growth , 2011, Biotechnology and bioengineering.
[32] P. Ferrer,et al. A step forward to improve recombinant protein production in Pichia pastoris : from specific growth rate effect on protein secretion to carbon-starving conditions as advanced strategy. , 2016 .
[33] Christoph Herwig,et al. Tunable recombinant protein expression in E. coli: enabler for continuous processing? , 2016, Applied Microbiology and Biotechnology.
[34] C. Cooney,et al. White Paper on Continuous Bioprocessing May 20-21 2014 Continuous Manufacturing Symposium. , 2015 .
[35] V. Fromion,et al. Translation elicits a growth rate‐dependent, genome‐wide, differential protein production in Bacillus subtilis , 2016, Molecular systems biology.
[36] W. Verstraete,et al. Microbial protein: future sustainable food supply route with low environmental footprint , 2016, Microbial biotechnology.
[37] P. Fickers,et al. A quantitative study of methanol/sorbitol co-feeding process of a Pichia pastoris Mut+/pAOX1-lacZ strain , 2013, Microbial Cell Factories.
[38] Philip Lijnzaad,et al. Cell cycle population effects in perturbation studies , 2014, Molecular systems biology.
[39] Duboc,et al. From gene to product in yeast: production of fungal cutinase. , 2000, Enzyme and microbial technology.
[40] Paul A Hoskisson,et al. Continuous culture--making a comeback? , 2005, Microbiology.
[41] A. Wolfe. The Acetate Switch , 2005, Microbiology and Molecular Biology Reviews.
[42] Gerhard Schembecker,et al. Developing the biofacility of the future based on continuous processing and single-use technology. , 2015, Journal of biotechnology.
[43] David W. Kicklighter,et al. Modelling carbon responses of tundra ecosystems to historical and projected climate: sensitivity of pan‐Arctic carbon storage to temporal and spatial variation in climate , 2000, Global change biology.
[44] Konstantin B Konstantinov,et al. The future of industrial bioprocessing: batch or continuous? , 2015, Biotechnology and bioengineering.
[45] K. Jensen,et al. The RNA chain elongation rate in Escherichia coli depends on the growth rate , 1994, Journal of bacteriology.
[46] Anurag S Rathore,et al. Integrated continuous processing of proteins expressed as inclusion bodies: GCSF as a case study , 2017, Biotechnology progress.
[47] Lucília Domingues,et al. Aspergillus niger β-galactosidase production by yeast in a continuous high cell density reactor , 2005 .
[48] D. Hoyle,et al. Growth control of the eukaryote cell: a systems biology study in yeast , 2007, Journal of biology.
[49] Dirk Weuster-Botz,et al. Parallel steady state studies on a milliliter scale accelerate fed‐batch bioprocess design for recombinant protein production with Escherichia coli , 2016, Biotechnology progress.
[50] Pei Yee Ho,et al. Multiple High-Throughput Analyses Monitor the Response of E. coli to Perturbations , 2007, Science.
[51] I V Diers,et al. Yeast fermentation processes for insulin production. , 1991, Bioprocess technology.
[52] Peter Neubauer,et al. Detection of growth rate‐dependent product formation in miniaturized parallel fed‐batch cultivations , 2017, Engineering in life sciences.
[53] D. Fotiadis,et al. Cultivation strategies to enhance productivity of Pichia pastoris: A review. , 2015, Biotechnology advances.
[54] Dirk Weuster-Botz,et al. High-performance recombinant protein production with Escherichia coli in continuously operated cascades of stirred-tank reactors , 2017, Journal of Industrial Microbiology & Biotechnology.
[55] C. Curless,et al. Chemostat study of kinetics of human lymphokine synthesis in recombinant Escherichia coli. , 1989, Biotechnology and bioengineering.
[56] J. Bailey,et al. Continuous cultivation of recombinant Escherichia coli: Existence of an optimum dilution rate for maximum plasmid and gene product concentration , 1986, Biotechnology and bioengineering.
[57] Jacques Monod,et al. LA TECHNIQUE DE CULTURE CONTINUE THÉORIE ET APPLICATIONS , 1978 .
[58] F. Segal,et al. A CHARACTERIZATION OF FIBRANT SEGAL CATEGORIES , 2006, math/0603400.
[59] G. Robson,et al. Optimization and stability of glucoamylase production by recombinant strains of Aspergillus niger in chemostat culture. , 1998, Biotechnology and bioengineering.
[60] Tamás Fehér,et al. Low-mutation-rate, reduced-genome Escherichia coli: an improved host for faithful maintenance of engineered genetic constructs , 2012, Microbial Cell Factories.
[61] J. Nielsen,et al. Correlation of cell growth and heterologous protein production by Saccharomyces cerevisiae , 2013, Applied Microbiology and Biotechnology.
[62] E. Baker,et al. Production of recombinant proteins in Mycobacterium smegmatis for structural and functional studies , 2015, Protein science : a publication of the Protein Society.
[63] O. Maaløe,et al. Dependency on medium and temperature of cell size and chemical composition during balanced grown of Salmonella typhimurium. , 1958, Journal of general microbiology.
[64] Alois Jungbauer,et al. Integrated Continuous Manufacturing of Biopharmaceuticals , 2017 .
[65] P. Brigidi,et al. Study of stability of recombinant plasmids during the continuous culture of Bacillus stearothermophilus NUB3621 in nonselective medium. , 1997, Biotechnology and bioengineering.
[66] Karl Friehs,et al. Extracellular recombinant protein production under continuous culture conditions with Escherichia coli using an alternative plasmid selection mechanism , 2014, Bioprocess and Biosystems Engineering.
[67] J. Nielsen,et al. Glucoamylase production in batch, chemostat and fed-batch cultivations by an industrial strain of Aspergillus niger , 2000, Applied Microbiology and Biotechnology.
[68] Anurag S. Rathore,et al. Application of process analytical technology for downstream purification of biotherapeutics , 2015 .
[69] A. Villaverde,et al. Fine regulation of cI857-controlled gene expression in continuous culture of recombinant Escherichia coli by temperature , 1993, Applied and environmental microbiology.
[70] Eun Kyu Lee,et al. Production of single-chain variable fragment antibody (scFv) in fed-batch and continuous culture of Pichia pastoris by two different methanol feeding methods. , 2007, Journal of bioscience and bioengineering.
[71] K. San,et al. Persistence and expression of the plasmid pBR322 inEscherichia coli K12 cultured in complex medium , 1987, Biotechnology Letters.
[72] Annik Nanchen,et al. Nonlinear Dependency of Intracellular Fluxes on Growth Rate in Miniaturized Continuous Cultures of Escherichia coli , 2006, Applied and Environmental Microbiology.
[73] K. J. Mukherjee,et al. Kinetic studies of recombinant human interferon-gamma expression in continuous cultures of E. coli , 2009, Journal of Industrial Microbiology & Biotechnology.
[74] Verena Siewers,et al. Characterization of chromosomal integration sites for heterologous gene expression in Saccharomyces cerevisiae , 2009, Yeast.
[75] Elmar Heinzle,et al. A system of miniaturized stirred bioreactors for parallel continuous cultivation of yeast with online measurement of dissolved oxygen and off‐gas , 2013, Biotechnology and bioengineering.
[76] Diethard Mattanovich,et al. Macromolecular and elemental composition analysis and extracellular metabolite balances of Pichia pastoris growing at different oxygen levels , 2009, Microbial cell factories.
[77] N. T. Eriksen,et al. Acid phosphatase production by Aspergillus niger N402A in continuous flow culture. , 2006, FEMS microbiology letters.
[78] J. Büchs,et al. In situ product recovery of single‐chain antibodies in a membrane bioreactor , 2014, Biotechnology and bioengineering.
[79] Jason Walther,et al. The business impact of an integrated continuous biomanufacturing platform for recombinant protein production. , 2015, Journal of biotechnology.
[80] K. Valgepea,et al. Proteome reallocation in Escherichia coli with increasing specific growth rate. , 2015, Molecular bioSystems.
[81] J. Pronk,et al. Chemostat-based micro-array analysis in baker's yeast. , 2009, Advances in microbial physiology.
[82] Charles E Wyman,et al. Review: Continuous hydrolysis and fermentation for cellulosic ethanol production. , 2010, Bioresource technology.
[83] Wim Soetaert,et al. Minimizing acetate formation in E. coli fermentations , 2007, Journal of Industrial Microbiology & Biotechnology.
[84] H. Bremer,et al. Polypeptide-chain-elongation rate in Escherichia coli B/r as a function of growth rate. , 1976, The Biochemical journal.
[85] M. Flickinger,et al. Sustaining Protein Synthesis in the Absence of Rapid Cell Division: An Investigation of Plasmid‐Encoded Protein Expression in Escherichia coli during Very Slow Growth , 1993, Biotechnology progress.
[86] G. Robson,et al. Recombinant glucoamylase production by Aspergillus niger B1 in chemostat and pH auxostat cultures. , 1998, Fungal genetics and biology : FG & B.