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1.
BMC Syst Biol ; 11(1): 49, 2017 04 17.
Article in English | MEDLINE | ID: mdl-28412970

ABSTRACT

BACKGROUND: Microbial production of nitrogen containing compounds requires a high uptake flux and assimilation of the N-source (commonly ammonium), which is generally coupled with ATP consumption and negatively influences the product yield. In the industrial workhorse Saccharomyces cerevisiae, ammonium (NH4+) uptake is facilitated by ammonium permeases (Mep1, Mep2 and Mep3), which transport the NH4+ ion, resulting in ATP expenditure to maintain the intracellular charge balance and pH by proton export using the plasma membrane-bound H+-ATPase. RESULTS: To decrease the ATP costs for nitrogen assimilation, the Mep genes were removed, resulting in a strain unable to uptake the NH4+ ion. Subsequent analysis revealed that growth of this ∆mep strain was dependent on the extracellular NH3 concentrations. Metabolomic analysis revealed a significantly higher intracellular NHX concentration (3.3-fold) in the ∆mep strain than in the reference strain. Further proteomic analysis revealed significant up-regulation of vacuolar proteases and genes involved in various stress responses. CONCLUSIONS: Our results suggest that the uncharged species, NH3, is able to diffuse into the cell. The measured intracellular/extracellular NHX ratios under aerobic nitrogen-limiting conditions were consistent with this hypothesis when NHx compartmentalization was considered. On the other hand, proteomic analysis indicated a more pronounced N-starvation stress response in the ∆mep strain than in the reference strain, which suggests that the lower biomass yield of the ∆mep strain was related to higher turnover rates of biomass components.


Subject(s)
Ammonium Compounds/metabolism , Cation Transport Proteins/genetics , Gene Deletion , Membrane Potentials , Saccharomyces cerevisiae Proteins/genetics , Saccharomyces cerevisiae/cytology , Saccharomyces cerevisiae/metabolism , Adenosine Triphosphate/metabolism , Aerobiosis , Biological Transport , Cation Transport Proteins/deficiency , Cation Transport Proteins/metabolism , Diffusion , Extracellular Space/metabolism , Hydrogen-Ion Concentration , Intracellular Space/metabolism , Metabolomics , Nitrogen/metabolism , Permeability , Proteomics , Saccharomyces cerevisiae/genetics , Saccharomyces cerevisiae Proteins/metabolism
2.
Metabolites ; 6(2)2016 Apr 23.
Article in English | MEDLINE | ID: mdl-27120628

ABSTRACT

Ammonium (NH4⁺) is the most common N-source for yeast fermentations, and N-limitation is frequently applied to reduce growth and increase product yields. While there is significant molecular knowledge on NH4⁺ transport and assimilation, there have been few attempts to measure the in vivo concentration of this metabolite. In this article, we present a sensitive and accurate analytical method to quantify the in vivo intracellular ammonium concentration in Saccharomyces cerevisiae based on standard rapid sampling and metabolomics techniques. The method validation experiments required the development of a proper sample processing protocol to minimize ammonium production/consumption during biomass extraction by assessing the impact of amino acid degradation-an element that is often overlooked. The resulting cold chloroform metabolite extraction method, together with quantification using ultra high performance liquid chromatography-isotope dilution mass spectrometry (UHPLC-IDMS), was not only more sensitive than most of the existing methods but also more accurate than methods that use electrodes, enzymatic reactions, or boiling water or boiling ethanol biomass extraction because it minimized ammonium consumption/production during sampling processing and interference from other metabolites in the quantification of intracellular ammonium. Finally, our validation experiments showed that other metabolites such as pyruvate or 2-oxoglutarate (αKG) need to be extracted with cold chloroform to avoid measurements being biased by the degradation of other metabolites (e.g., amino acids).

3.
Prep Biochem Biotechnol ; 46(8): 815-821, 2016 Nov 16.
Article in English | MEDLINE | ID: mdl-26829467

ABSTRACT

This work describes a strategy to optimize a downstream processing of a recombinant human growth hormone (rhGH) by incorporating a quality by design approach toward meeting higher quality specifications. The optimized process minimized the presence of impurities and degradation by-products during manufacturing by the establishment of in-process controls. Capillary zone electrophoresis, reverse phase, and size-exclusion chromatographies were used as analytical techniques to establish new critical process parameters for the solubilization, capture, and intermediate purification steps aiming to maintain rhGH quality by complying with pharmacopeial specifications. The results indicated that the implemented improvements in the process allowed the optimization of the specific recovery and purification of rhGH without compromising its quality. In addition, this optimization facilitated the stringent removal of the remaining impurities in further polishing stages, as demonstrated by the analysis of the obtained active pharmaceutical ingredient.


Subject(s)
Growth Hormone/isolation & purification , Chromatography, Gel/methods , Chromatography, Reverse-Phase/methods , Electrophoresis, Capillary/methods , Humans , Recombinant Proteins/isolation & purification , Solubility
4.
Trends Biotechnol ; 33(9): 534-46, 2015 Sep.
Article in English | MEDLINE | ID: mdl-26232033

ABSTRACT

The field of metabolic engineering has delivered new microbial cell factories and processes for the production of different compounds including biofuels, (di)carboxylic acids, alcohols, and amino acids. Most of these processes are aerobic, with few exceptions (e.g., alcoholic fermentation), and attention is focused on assembling a high-flux product pathway with a production limit usually set by the oxygen transfer rate. By contrast, anaerobic product synthesis offers significant benefits compared to aerobic systems: higher yields, less heat generation, reduced biomass production, and lower mechanical energy input, which can significantly reduce production costs. Using simple thermodynamic calculations, we demonstrate that many products can theoretically be produced under anaerobic conditions using several conventional and non-conventional substrates.


Subject(s)
Biomass , Biotechnology/methods , Fermentation , Metabolic Engineering/methods , Anaerobiosis , Thermodynamics
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