Metabolic response of Pseudomonas putida during redox biocatalysis in the presence of a second octanol phase.
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A Comparison of the Microbial Production and Combustion Characteristics of Three Alcohol Biofuels: Ethanol, 1-Butanol, and 1-OctanolMetabolic Engineering of Pseudomonas putida KT2440 to Produce Anthranilate from GlucoseMetabolic engineering of Pseudomonas sp. strain VLB120 as platform biocatalyst for the production of isobutyric acid and other secondary metabolitesRapid Prediction of Bacterial Heterotrophic Fluxomics Using Machine Learning and Constraint ProgrammingRobustness and plasticity of metabolic pathway flux among uropathogenic isolates of Pseudomonas aeruginosa.The Entner-Doudoroff pathway empowers Pseudomonas putida KT2440 with a high tolerance to oxidative stress.Engineering of Pseudomonas taiwanensis VLB120 for constitutive solvent tolerance and increased specific styrene epoxidation activity.Reconciling in vivo and in silico key biological parameters of Pseudomonas putida KT2440 during growth on glucose under carbon-limited conditionIsolation and characterization of a thermotolerant ene reductase from Geobacillus sp. 30 and its heterologous expression in Rhodococcus opacus.Efflux systems in bacteria and their metabolic engineering applicationsAnoxic metabolism and biochemical production in Pseudomonas putida F1 driven by a bioelectrochemical system.Bypasses in intracellular glucose metabolism in iron-limited Pseudomonas putidaWhy are chlorinated pollutants so difficult to degrade aerobically? Redox stress limits 1,3-dichloroprop-1-ene metabolism by Pseudomonas pavonaceaeIndustrial biotechnology of Pseudomonas putida and related species.Biotechnological domestication of pseudomonads using synthetic biology.Response of Pseudomonas putida KT2440 to increased NADH and ATP demand.Experimental validation of in silico estimated biomass yields of Pseudomonas putida KT2440.Engineering microbial hosts for production of bacterial natural productsEngineering mediator-based electroactivity in the obligate aerobic bacterium Pseudomonas putida KT2440.Growth independent rhamnolipid production from glucose using the non-pathogenic Pseudomonas putida KT2440.Variability in subpopulation formation propagates into biocatalytic variability of engineered Pseudomonas putida strains.Subpopulation-proteomics reveal growth rate, but not cell cycling, as a major impact on protein composition in Pseudomonas putida KT2440.The glycerophospholipid inventory of Pseudomonas putida is conserved between strains and enables growth condition-related alterations.Pseudomonas putida KT2440 Strain Metabolizes Glucose through a Cycle Formed by Enzymes of the Entner-Doudoroff, Embden-Meyerhof-Parnas, and Pentose Phosphate PathwaysLet's talk about flux or the importance of (intracellular) reaction rates.Accumulation of inorganic polyphosphate enables stress endurance and catalytic vigour in Pseudomonas putida KT2440.Metabolic Engineering of Pseudomonas putida KT2440 for the Production of para-Hydroxy Benzoic Acid.The functional structure of central carbon metabolism in Pseudomonas putida KT2440.Selected Pseudomonas putida strains able to grow in the presence of high butanol concentrations.The metabolic cost of flagellar motion in Pseudomonas putida KT2440.Creating metabolic demand as an engineering strategy in Pseudomonas putida - Rhamnolipid synthesis as an example.When Do Two-Stage Processes Outperform One-Stage Processes?Dynamics of benzoate metabolism in Pseudomonas putida KT2440.The application of constitutively solvent-tolerant P. taiwanensis VLB120ΔCΔttgV for stereospecific epoxidation of toxic styrene alleviates carrier solvent use.D-Xylose assimilation via the Weimberg pathway by solvent-tolerant Pseudomonas taiwanensis VLB120.Synthesis of chiral 2-alkanols from n-alkanes by a P. putida whole-cell biocatalyst.Pyridine nucleotide transhydrogenases enable redox balance of Pseudomonas putida during biodegradation of aromatic compounds.H2-driven biotransformation of n-octane to 1-octanol by a recombinant Pseudomonas putida strain co-synthesizing an O2-tolerant hydrogenase and a P450 monooxygenase.Making variability less variable: matching expression system and host for oxygenase-based biotransformations.Production host selection for asymmetric styrene epoxidation: Escherichia coli vs. solvent-tolerant Pseudomonas.
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Metabolic response of Pseudomonas putida during redox biocatalysis in the presence of a second octanol phase.
description
2008 nî lūn-bûn
@nan
2008年の論文
@ja
2008年学术文章
@wuu
2008年学术文章
@zh-cn
2008年学术文章
@zh-hans
2008年学术文章
@zh-my
2008年学术文章
@zh-sg
2008年學術文章
@yue
2008年學術文章
@zh
2008年學術文章
@zh-hant
name
Metabolic response of Pseudomo ...... nce of a second octanol phase.
@en
Metabolic response of Pseudomo ...... nce of a second octanol phase.
@nl
type
label
Metabolic response of Pseudomo ...... nce of a second octanol phase.
@en
Metabolic response of Pseudomo ...... nce of a second octanol phase.
@nl
prefLabel
Metabolic response of Pseudomo ...... nce of a second octanol phase.
@en
Metabolic response of Pseudomo ...... nce of a second octanol phase.
@nl
P2860
P50
P1433
P1476
Metabolic response of Pseudomo ...... ence of a second octanol phase
@en
P2093
Georgios Ionidis
Lars M Blank
P2860
P304
P356
10.1111/J.1742-4658.2008.06648.X
P407
P577
2008-09-18T00:00:00Z