Membrane potential independent transport of NH3 in the absence of ammonium permeases in Saccharomyces cerevisiae
- Hugo F. Cueto-Rojas†1View ORCID ID profile,
- Nicholas Milne†1, 2,
- Ward van Helmond1, 3,
- Mervin M. Pieterse1,
- Antonius J. A. van Maris1, 4,
- Jean-Marc Daran1Email author and
- S. Aljoscha Wahl1Email author
© The Author(s). 2017
Received: 19 May 2016
Accepted: 20 December 2016
Published: 17 April 2017
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.
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.
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.
KeywordsIntracellular ammonium Metabolomics Ammonium transport Central nitrogen metabolism Ammonia passive diffusion Thermodynamics
A significant number of fuels and commodity chemicals have the potential to be produced in bio-refineries using microbial fermentation, which represents a more sustainable alternative to current oil-based production . The increasing interest in microbial-based production is best exemplified by the intensive research efforts to improve the productivity and yield of a vast range of different compounds produced by Saccharomyces cerevisiae [2, 3] and other industrial workhorses. Nevertheless, while the number of compounds produced at industrial scale by S. cerevisiae is increasing, the production of nitrogen-containing compounds using S. cerevisiae is significantly under-represented, with heterologous protein production being the only known example .
Nitrogen-containing compounds represent an economically relevant class of commodity chemicals that includes amino acids such as L-lysine and L-glutamate, diamines such as 1,5-diaminopentane (cadaverine) and 1,4-diaminobutane (putrescine), and relevant synthesis precursors such as caprolactam. Their microbial production is currently performed under aerobic conditions using bacteria, most commonly Corynebacterium glutamicum and Escherichia coli [4–6].
Along with bacteria, S. cerevisiae is seen as an attractive host organism for industrial fermentation due to its fast anaerobic conversion of sugar to product, its resistance to phage attack, and its robustness under common industrial conditions . When using S. cerevisiae for the production of nitrogen-containing compounds, the process should preferably occur under anaerobic conditions  if this is permitted by the thermodynamics and biochemistry of the product pathway. Anaerobic conditions are favorable not only in terms of the resulting fermentation costs, but also in terms of the product yield . Under such conditions, however, the energy supply relies solely on substrate-level phosphorylation, limiting the amount of ATP available for growth and maintenance. Consequently, the anaerobic production of nitrogen-containing compounds should result in net ATP formation and it is essential that the N-source be transported and assimilated using ATP-independent mechanisms.
Urea and ammonium are the most common N-sources used industrially in S. cerevisiae fermentations. Previously, we presented a novel strategy for achieving ATP-independent urea assimilation in S. cerevisiae . While urea is an attractive nitrogen source, ammonium is more commonly used in industrial fermentation and is also present in plant hydrolysates used for second-generation chemical production [11, 12]. Mechanisms for ATP-neutral ammonium transport and assimilation would have significant relevance for the anaerobic production of nitrogen-containing compounds. Ammonia (NH3) protonates in aqueous solutions to produce the ammonium ion (NH4 +), the sum of these two species, NH3 and NH4 +, will be described henceforth as NHX. With a pKa of 9.25, under biologically relevant conditions (between pH 3 and 7), the ratio NH3/NH4 + equals 10pH-9.25, meaning that the vast majority of the NHX is present as the charged ammonium species (NH4 +).
In S. cerevisiae, NH4 + is taken up by the ammonium permeases Mep1, Mep2, and Mep3, which belong to the Amt class of proteins that use the negative membrane potential as their thermodynamic driving force . The evolutionary advantage of this transport mechanism, compared with passive diffusion, is a higher transport rate. And, due to the negative cytosolic membrane potential, accumulation of intracellular NHX is favored. However, one H+ must be exported from the cytosol by the plasma-membrane-bound H+-ATPase Pma1  to recover the proton motive force (pmf) and charge homeostasis after NH4 + import, and subsequent assimilation of NH3 . The deletion of the ammonium permease genes Mep1, Mep2, and Mep3 results in a viable strain able to grow on ammonium concentrations above 5 mM. Previously, it has been assumed that there are additional ammonium transporters  or that there is non-specific transport through potassium channels . However, we here present an alternative hypothesis: that the uncharged NH3 species can diffuse into the cell. If this were correct, it would result in ATP-independent NHX uptake and consequently reduce the demand for ATP demand. Previous experimental observations in synthetic bilayer lipid membranes suggest that the NH3 apparent permeability coefficient is P 1a = 1.728 m/h (48 × 10−3 cm/s) , which indicates that cell membranes are indeed permeable to NH3.
Here, we study the NHX-uptake mechanism in a ∆mep S. cerevisiae strain, and assess the impact of the deletion of Mep1, Mep2, and Mep3 on the physiology of S. cerevisiae. Proteomic and metabolomic measurements are used to investigate the global impact of the changed NHX-uptake mechanism on cellular physiology.
Strains and maintenance
Strains used in this study
MATalpha ura3-52 his3-D1 LEU2 TRP1 MAL2-8c SUC2
MATalpha ura3-52 his3-D1 LEU2 TRP1 MAL2-8c SUC2 mep1::loxP-KanMX4-loxP
CEN.PK113-3B-Δmep1, Δmep 2
MATalpha ura3-52 his3-D1 LEU2 TRP1 MAL2-8c SUC2 mep1::loxP-KanMX4-loxP mep2::loxP-NatNT2-loxP
CEN.PK113-3B-Δmep1, Δmep 2, Δmep 3
MATalpha ura3-52 his3-D1 LEU2 TRP1 MAL2-8c SUC2 mep1::loxP-KanMX4-loxP mep2::loxP-NatNT2-loxP mep3::loxP-Ura3-loxP
CEN.PK113-3B-Δmep1, Δmep 2, Δmep 3-Cure
MATalpha ura3-52 his3-D1 LEU2 TRP1 MAL2-8c SUC2 mep1::loxP-loxP mep2::loxP-loxP mep3::loxP-loxP
MATalpha ura3-52 his3-D1 LEU2 TRP1 MAL2-8c SUC2 mep1::loxP-loxP mep2::loxP-loxP mep3::loxP-loxP pUDE199 (HIS3 URA3)
MATalpha ura3-52 his3-Δ1 LEU2 TRP1 MAL2-8c SUC2 pUDE199 (HIS3 URA3)
Shake flask cultivation
S. cerevisiae strains were grown in synthetic medium . Cultures were grown in either 500 mL or 250 mL shake flasks containing 100 mL or 50 mL of medium, respectively, and incubated at 30 °C in an Innova incubator shaker (New Brunswick Scientific, Edison, NJ) at 200 rpm.
Aerobic nitrogen-limited chemostat cultivation
Controlled aerobic, nitrogen limited chemostat cultivations were carried out at 30 °C in 7 L bioreactors (Applikon Biotechnology B.V., Delft, the Netherlands) with a working volume of 4 L. Chemostat cultivations were preceded by a batch phase using the same synthetic medium as used for the feed. Continuous cultivation was initiated at a dilution rate of 0.05 h−1; synthetic nitrogen-limited medium was used modified from , which contained: 130 g/L glucose, 25 g/L ethanol, 3.48 g/L NH4H2PO4, 1.14 g/L MgSO4 · 7H2O, 6.9 g/L KH2PO4, 0.3 g/L Antifoam C, with the appropriate growth factors added accordingly  (vitamin solution 2 mL/L and trace element solution 2 mL/L), ethanol was added to the medium to avoid potential oscillations. The medium was designed to sustain a biomass concentration of up to 8 g/L in nitrogen-limited anaerobic conditions for the wild type (CEN.PK113-7D) strain. The temperature and stirring speed were kept constant at 30 °C and 500 rpm, respectively. The reactor had an overpressure of 0.3 bar, and an aeration rate of 0.5 vvm was used to keep the dissolved oxygen level above 80%. Dissolved oxygen tension (DOT) was monitored online using an oxygen probe (Mettler-Toledo, Tiel, The Netherlands), and a combined paramagnetic/infrared analyser (NGA 2000, Fisher-Rosemount, Hasselroth, Germany) was used to measure CO2 and O2 fractions in the off-gas. During the batch phase and the first steady state the pH was kept constant at a value of 5 with automatic additions of 4 M KOH or 2 M H2SO4; after reaching steady state and sampling, the pH control was changed to maintain a constant value of 6, while keeping the dilution rate constant; the same operation was performed for the switch from pH = 6 to pH = 7. All samples were taken at steady state between three and seven volume changes after switching on the medium addition or pH changes.
Sampling and sample preparation
For aerobic nitrogen limited chemostats, samples of approx. 2 mL were quenched using cold steel beads , and filtered using 0.45 μm disc filters (Milipore). Samples for residual ammonium determination were prepared by mixing 80 μL of sample with 20 μL of internal standard (500 μmol/L 15N-NH4Cl) and quantified according to . All samples were stored at -80 °C until further analysis.
Samples containing approximately 1.2 g broth were obtained using a dedicated setup, as described by , quenched in 6 mL of -40 °C methanol 100%, and after weighing to accurately determining the mass of each sample, these were centrifuged for 5 min at 10,000 g and -19 °C. The pellet was recovered and resuspended in 6 mL -40 °C methanol 100%; then centrifuged again for 5 min at 10,000 g and -19 °C .
Intracellular ammonium extraction
The biomass pellet obtained from Intracellular sampling was recovered, 3.5 mL of Methanol-acetate buffer 10 mM (pH = 5) 50%(v/v) pre-chilled at -40 °C was added, and then 120 μL of U-13C- cell extract with labeled urea (intracellular metabolites samples) or 120 μL of 15N- NH4Cl 500 μmol/L (intracellular ammonium samples) were added as internal standard. Afterwards, 3.5 mL of Chloroform 100% pre-chilled at -40 °C was added in order to extract intracellular metabolites according to . Samples for quantification of intracellular ammonium were extracted using exclusively this method.
Intracellular metabolite extraction
The biomass pellet (Intracellular sampling) was recovered by addition of 3.5 mL Methanol-MilliQ water 50% (v/v) pre-chilled at -40 °C and 120 μL of U-13C- cell extract. 3.5 mL of chloroform 100% pre-chilled at -40 °C was added in order to extract intracellular metabolites as described by .
Micro-titer plate assays
Ninety-six well plate assays were prepared by adding 100 μL of synthetic medium with 20 g/L glucose, Tween-80 (420 mg/L) and ergosterol (10 mg/L). The initial pH of the medium was adjusted using 2 M HCl and 2 M KOH. (NH4)2SO4 was used as the nitrogen source and the SO4 2− concentration was kept constant at 38 mM by addition of K2SO4 to compensate for the decrease in SO4 2− from (NH4)2SO4. Cells were inoculated in each well to a starting OD660 of 0.1. Plates were covered with Nunc™ sealing tape (Thermo Scientific) and incubated at 30 °C with constant shaking at 200 rpm. OD660 was measured regularly in a GENios pro plate reader (Tecan Benelux, Giessen, The Netherlands).
Quantification of intracellular trehalose, glycolytic, TCA cycle and PPP intermediates was performed as described by ; amino acids were quantified according to , nucleotides as described in  and coenzymes were measured using LC-MS/MS as reported by . Intra- and extracellular ammonium was quantified using ultra-high performance liquid chromatography with isotope dilution mass spectrometry (UHPLC-IDMS) as described by . Quantification of extracellular metabolites was performed using HPLC as described in . Cellular concentrations were estimated using the metabolite content per gCDW (μmol/gCDW) and the average cell volume including dry matter (mLWC/gCDW), which was determined using a Z2 Coulter counter (50 μm aperture, Beckman, Fullerton, CA) .
U-13C-labelled S. cerevisiae biomass was prepared as described by  and used as internal standard for relative protein quantification. Cell suspensions of the sample biomass and internal standard were mixed 1:1 based on the OD600, washed with milli-Q and freeze-dried. Proteins were extracted by grinding the freeze-dried biomass with pestle and mortar, which were precooled with liquid nitrogen. After grinding, 2 mL of 50 mM phosphate buffer (PBS) with 200 mM NaOH was added to extract proteins. The soluble protein fraction was separated from the cell debris by centrifugation at 13,300 rpm for 15 min. Proteins were precipitated overnight in cold acetone at -20 °C by adding 4 parts of cold acetone to 1 part of protein solution. After washing and drying the protein pellet was dissolved in 400 μL of 100 mM ammonium bicarbonate (ABC) with 6 M urea. Of this solution, 20 μL was further processed; proteins were reduced by addition of tris(2-carboxyethil)phosphine (TCEP) to a final concentration of 10 mM and incubating for 60 min at room temperature. Proteins were alkylated by addition of Iodoacetamide (IAM) to a final concentration of 10 mM and incubating for 60 min at room temperature. Prior to digestion the protein solution was 6 times diluted by addition of 100 μL of 100 mM ABC to dilute the urea concentration to 1 M. Proteins were digested by addition of trypsin (trypsin singles, proteomics grade, Sigma-Aldrich) in a 1:100 ratio and incubating at 37 °C for 16 h. The digested protein mixture was purified and concentrated using an in-house made SPE pipette tip using 5 μm particles of Reprosil-Pur C18-Aq reversed phase material (Dr. Maisch GmbH, Ammerbuch-Entringen, Germany).
Digested peptides were separated using nanoflow chromatography performed using a vented column system essentially as described by  and a 2-dimensional precolumn (RP-SCX-RP). Analytical columns of 50 μm id were prepared with a 1 mm Kasil frit and packed with 5 μm particles of Reprosil-Pur C18-Aq reversed phase material to a length of 40 cm. The capillary RP-SCX-RP precolumn of 150 μm id was prepared with a 1 mm Kasil frit and packed with 5 μm particles of Reprosil-Pur C18-Aq reversed phase material to a length of 17 mm, 5 μm particles of PolySulfoethyl a strong cation exchange material for 60 mm and again 5 μm particles of Reprosil-Pur C18-Aq reversed phase material for 17 mm (total length 94 mm). The different column materials were kept separated from each other by insertion of a piece of glass wool. The used LC equipment and solvents were similar to . Each sample analysis consisted of six fractionations. In the first fraction the peptides are injected and trapped on the precolumn by applying 100% solvent A for 10 min. Then a first linear gradient was applied from 4 to 35% B in 75 min. After this, a linear gradient to 80% B was followed for 6 min and then 3 min of 80% B. Finally the column was reconditioned for 26 min with 100% A. In the following 5 fractionations, peptides were eluted by 10 μL injections of respectively 5, 10, 50, 250 or 1000 mM ammonium formate pH 2.6 from the autosampler (followed by 100% A for 10 min). Again a first linear gradient was applied from 4 to 35% B in 75 min, followed by a second linear gradient to 80% B for 6 min and then 3 min of 80% B. After each fraction the column was reconditioned for 26 min with 100% A. This results in six fractionations per sample with a total run-time of 12 h per sample. For each analysis ~10 μg of protein was injected.
Mass spectrometry was performed using a protocol derived from  and similar to . Briefly explained, full scan MS spectra (from m/z 400–1500, charge states 2 and higher) were acquired at a resolution of 30,000 at m/z 400 after accumulation to a target value of 106 ions (automatic gain control). Nine data-dependent MS/MS scans (HCD spectra, resolution 7,500 at m/z 400) were acquired using the 9 most intense ions with a charge state of 2+ or higher and an ion count of 10,000 or higher. The maximum injection time was set to 500 ms for the MS scans and 200 ms for the MS/MS scan (accumulation for MS/MS was set to target value of 5 × 104). Dynamic exclusion was applied using a maximum exclusion list of 50, one repeat count, repeat duration of 10 s and exclusion duration of 45 s. The exclusion window was set from −10 to + 10 ppm relative to the selected precursor mass.
Data processing and analysis was performed similarly to . Briefly, MS/MS spectra were converted to Mascot Generic Files (MGF) using Proteome Discoverer 1.4 (ThermoFisher Scientific) and DTASuperCharge version 2.0b1 . MGF’s from the 6 SCX fractions of the same sample were combined using MGFcombiner version 1.10 . The samples were analyzed with Mascot v2.2.02 search engine (Matrix Science, Boston, MA, USA). As reference proteome the Uniprot  proteome of Saccharomyces cerevisiae strain ATCC 204508/288c (ID: UP000002311; 6634 sequences) was used.
Carbamidomethyl cysteine was set as a fixed modification and oxidized methionine as a variable modification. Trypsin was specified as the proteolytic enzyme, and up to three missed cleavages were accepted. Mass tolerance for fragment ions was set at 0.05 Da and for precursor peptide ions at 10 ppm. Peptides with Mascot score <10 were removed and only the highest scoring peptide matches for each query listed under the highest scoring protein (bold red) were selected. Proteins were quantified using MSQuant version 2.0b7  by importing the Mascot results html file with the corresponding raw mass spectrometric data files. MSQuant automatically calculated peptide and protein ratios by using a 13C quantitation method (in quantitationmodes.xml), containing 7 modifications based on the amount of carbon atoms each amino acid contains. The difference in mass between 12C and 13C is 1.00335 Da. Resulting in mass shifts of 2 (glycine), 3 (ASC), 4 (NDT), 5 (EQMPV), 6 (RHILK), 9 (FY) or 11 (W) carbon atoms. Quantification was restricted to peptides with Mascot score ≥25, it is considered that a protein is up regulated when the concentration of protein is at least 50% higher in one strain compared to the other, growing at the same environmental condition. On the other hand, proteins identified with 2 or more confidence peptides with Mascot score ≥25 in one strain but not in the other are considered “unique proteins”.
Effect of extracellular NH3 concentration on growth rate
The growth rate of IME169 reached a maximum at approximately 20 mM NHX. The growth rate was negatively affected by increasing pH values (Fig. 1a), an expected effect caused by the deviation from the optimum pH =5. On the other hand, it was observed that the strain IMZ351 increased its growth rate with increasing pH values (Fig. 1b). Consequently, plotting the specific growth rate as a function of the NH3 concentration revealed a clear correlation between the two variables (Fig. 1c), indicating that the growth of IMZ351 was dependent on NH3 concentration whereas IME169 growth was dependent on NH4 + concentrations. This supports the hypothesis that deletion of Mep proteins leads to a change in the main uptake mechanism, from NH4 + uniport to NH3 diffusion. Clearly, diffusion is also present in the wild type. But, because of the electrochemical-based driving force, the concentration gradient for diffusion is actually in the direction of export rather than import. Thus, NHX uptake can only take place in the Mep-dependent transport mechanism.
If the Δmep strain (IMZ351) indeed relied on diffusion of NH3 to supply nitrogen to the cell, then the specific rate of N-uptake (-q N , in mol N/gCDW/h) is dependent on the NH3 concentration gradient between extracellular space and cytosol ([NH 3 ] EC -[NH 3 ] cyt , in mmol/L). The rate of NH3 uptake can be described by the apparent permeability coefficient (P 1a , in m/h) of the membrane, the biomass specific mass transfer area (a m , in this study 3.22 m2/gCDW), and the concentration gradient: − q N = P 1a a m ([NH 3] EC − [NH 3] cyt ). Under nitrogen-limited conditions, the growth rate will be dependent on the extracellular NH3 concentration, i.e., µ = χ N − 1 − q N , with χ N representing the biomass N-content (usually 0.148 mol N/C-mol biomass or 5.60 × 10−3 mol N/gCDW ).
Based on this dependency, the NH3 permeability coefficient for batch conditions can be estimated. Assuming that the NH3 extracellular concentration is much higher than the cytosolic concentration, the previous dependency can be approximated by − q N = P 1a a m [NH 3] EC . With the array of measured μMTP as a function of the initial NH3 concentration (Fig. 1c), the NH3 permeability coefficient is estimated as P 1a = 0.01 m/h. This value is two orders of magnitude below values reported in literature. This large deviation from the permeability measured in vitro could be due to different membrane compositions, but above all it is the assumption of negligible intracellular NHX concentration, which has an impact on the value obtained. The estimated value therefore represents the lower limit of permeability rather than a precise measure.
Intracellular and extracellular NHX ratios under N-limiting conditions
The micro-titer assay described above showed a clear link between the extracellular NH3 concentration and the growth rate of IMZ351, but these results cannot provide insights into the intracellular metabolism. Moreover, the absence of pH control and monitoring of dissolved oxygen concentration could potentially bias these results. In order to perform a detailed analysis of the resulting strain physiology in response to different mechanisms of NHX assimilation, aerobic N-limited chemostat cultures were carried out at varying pH values (pH = 5, pH = 6, pH = 7). Extracellular and intracellular metabolite measurements were performed at each steady-state condition. The aerobic N-limited conditions were selected to observe the energetic effect of NH3-diffusion based on differences in specific oxygen consumption rates (-q O2 ) between strains. Additionally, the use of N-limited conditions reduced the residual NHX and so increased the accuracy of the intracellular NHX measurements.
Intracellular and extracellular NHX concentrations of IME169 (reference strain) and IMZ351 (Δmep) measured at steady state at varying pH values from aerobic N-limited chemostats in synthetic medium with glucose at a dilution rate of 0.05 h−1 and the corresponding NHX IC/EC ratios. For calculation of predicted intracellular/extracellular ratios with compartmentalization three compartments were considered: cytosol, mitochondria and vacuole. The ratios were calculated as the maxima and minima of a sensitivity analysis where the following critical variables were considered: vacuolar volumes (between 25 and 14% intracellular volume), cytosolic pH (between 6 and 7) and vacuolar pH (between 4 and 5.5). The data represent average and mean deviation of triplicates
Average cell volume (mLIC/gCDW)
Biomass concentration (gCDW/Lbroth)
Intracellular NHX (mmol/LIC)
Extracellular NHX (mmol/LEC)
Measured IC/EC ratio
Predicted IC/EC equilibrium ratio range
IME169 Uniport NH4 +
2.59 ± 0.04
7.00 ± 0.02
1.74 ± 0.14
0.008 ± 0.001
219 ± 39
5.44 × 103
2.43 ± 0.04
7.45 ± 0.01
3.16 ± 0.16
302 ± 40
5.44 × 104
1.09 × 103
2.62 ± 0.02
7.73 ± 0.03
3.33 ± 0.09
0.013 ± 0.001
254 ± 10
5.44 × 105
1.09 × 104
IMZ351 Diffusion NH3
2.01 ± 0.08
6.44 ± 0.01
10.5 ± 0.7
6.99 ± 0.28
1.5 ± 0.1
2.00 ± 0.04
7.37 ± 0.04
10.9 ± 0.6
2.61 ± 0.09
4.2 ± 0.3
2.31 ± 0.09
7.73 ± 0.01
7.48 ± 0.7
0.57 ± 0.02
13.2 ± 1.3
However, the cytosolic NHX concentration cannot be measured directly. Current metabolomic approaches allow only for whole-cell quantifications, which from now on will be called intracellular (IC) measurement. In the case of NHX, previous works [41, 42] suggest significant accumulation and storage of NHX in the vacuole, which means that the whole-cell measurement and the cytosolic concentration could differ significantly. To account for vacuolar storage, the measured NHX ratios were compared with expected maximum and minimum ratios (IC/EC) based on assumptions for vacuolar diffusion (Additional file 1). Interestingly, the expected difference in ratios still allows for a clear separation of mechanisms in the presence of vacuolar storage.
In line with our hypothesis, the experimental data showed ratios with a difference of at least one order of magnitude between IME169 (Mep1, Mep2, Mep3) and IMZ351 (∆mep) (Table 2). For IMZ351, the IC/EC ratios measured experimentally corresponded well with the predicted ratios. However, while the IC/EC ratio for IME169 was predicted to increase with extracellular pH, it actually varied between 210 and 300 under the experimental conditions (Table 2) - which might indicate that, under these conditions, the ratio is determined by the affinity of the ammonium permeases and not by the thermodynamic driving force. Besides differences in IC/EC ratios, a substantially higher intracellular NHX concentration was observed for IMZ351.
Estimation of the NH3 permeability coefficient at steady state under N-limiting conditions
Under N-limiting conditions, it can be assumed that transport of the N-source is the limiting factor for growth in both strains. In IMZ351, the diffusion rate is determined, as explained earlier, by the NH3 permeability and the concentration gradient across the plasma membrane (([NH 3 ] EC -[NH 3 ] cyt ). While the concentration in the extracellular space ([NH 3 ] EC ) is measured directly, the cytosolic concentration ([NH 3 ] cyt ) needs to be estimated from the whole-cell measurement (IC), the specific nitrogen uptake rate (-q N ), and assumptions regarding the intracellular NHX distribution (Additional file 1). Here, it is assumed that the cytosol volume represents 70% of the cell volume, the vacuolar volume is 14% and the mitochondrial volume is about 1% of the total cell volume .
Additionally, NH3 transport processes between different compartments are assumed to operate close to thermodynamic equilibrium -and since no transport proteins that could translocate NHX between compartments are described in literature, passive diffusion of NH3 between vacuole and cytosol, as well as between cytosol and mitochondria, are assumed.
Estimation of the apparent permeability coefficient of ammonium for IMZ351 (Δmep) into the plasma membrane
Cytosolic NH3 (μmol/LCyt)
Extracellular NH3 (μmol/LEC)
Estimated Cyt/EC ratio
Apparent permeability coefficient (m/h)
Impact of NH3-diffusion on the physiology and metabolic fluxes of S. cerevisiae under aerobic N-limiting conditions
Effect of diffusion on the specific consumption and production rates
Overview of measured extracellular fluxes and N-content of IME169 (reference strain) and IMZ351 (Δmep) during N-limited aerobic chemostats in synthetic medium with glucose at a dilution rate of 0.05 h−1 at different extracellular pH
mol ATP/mol N
0.053 ± 0.001
3.862 ± 0.050
1.643 ± 0.006
7.028 ± 0.015
4.601 ± 0.223
0.251 ± 0.001
4.70 ± 0.01
0.077 ± 0.001
92.3 ± 1.3
7.72 ± 0.22
30.8 ± 0.9
0.052 ± 0.001
3.398 ± 0.013
1.468 ± 0.004
6.157 ± 0.010
4.438 ± 0.055
0.223 ± 0.004
4.30 ± 0.08
0.085 ± 0.001
91.4 ± 1.7
7.23 ± 0.05
32.4 ± 0.6
0.051 ± 0.001
2.953 ± 0.013
1.273 ± 0.007
5.218 ± 0.020
3.608 ± 0.038
0.208 ± 0.004
4.06 ± 0.08
0.096 ± 0.001
104.1 ± 2.3
6.03 ± 0.04
28.9 ± 0.6
0.047 ± 0.001
3.485 ± 0.025
1.390 ± 0.005
6.620 ± 0.014
4.735 ± 0.039
0.190 ± 0.008
4.00 ± 0.17
0.081 ± 0.001
110.1 ± 4.7
7.38 ± 0.04
38.9 ± 1.6
0.047 ± 0.001
3.074 ± 0.017
1.223 ± 0.006
5.825 ± 0.028
4.404 ± 0.046
0.183 ± 0.003
3.91 ± 0.06
0.085 ± 0.001
100.8 ± 1.7
6.73 ± 0.05
36.7 ± 0.6
0.048 ± 0.001
2.826 ± 0.031
1.239 ± 0.004
5.081 ± 0.009
3.639 ± 0.053
0.187 ± 0.003
3.88 ± 0.06
0.095 ± 0.001
90.7 ± 1.8
5.99 ± 0.05
32.0 ± 0.5
Intracellular metabolite concentrations
IMZ351 showed decreased biomass N-content when compared to IME169, suggesting that deletion of Mep genes resulted in an altered cellular response in nitrogen-limited chemostat cultures. To investigate physiological effects caused by the decreased specific NHX uptake rates, the concentrations of intracellular metabolites involved in carbon and nitrogen metabolism were measured (Additional file 1). While, surprisingly, the intracellular NHX concentration was actually significantly higher in IMZ351, the intracellular concentration of the product of the most prominent entry route for NHX assimilation, L-glutamate (Glu), was comparable in both strains at each pH. The L-glutamine concentration, which is the end product of the alternative route of NHX assimilation via the GS-GOGAT system, was lower for IMZ351 compared to the reference strain, but increased with pH. Downstream, the concentration of amino acids synthesized in the mitochondria -L-alanine, L-valine and L-lysine- were significantly lower in IMZ351. Furthermore, the intracellular trehalose concentration -which is an indicator of cellular stress and/or nitrogen limitation - was significantly higher in IMZ351 at all pH conditions.
Effects of NH3 diffusion on the protein levels
Alteration of the NHX transport mechanism resulted in changes in cellular metabolism, which were also related to changes in the protein levels [47, 48]. The measurement of relative protein levels showed changes in more than 300 different proteins, but in amounts that varied between strains in the different pH conditions. The concentration of certain proteins were low and could only be observed in one of the strains. Those proteins are called from “unique proteins”, although in this case the word “unique” does not imply that they are totally absent from the other strains/conditions, but only that their levels are in some cases below the detection tershold. While our analytical method cannot provide an answer on whether proteins are present or absent in the protein levels, then, these ‘unique’ proteins can be considered a especial subset of up/down regulated proteins. Nineteen proteins were consistently found as unique in IMZ351, but not in the reference strain (IME169) at all pH conditions; i.e., they were expressed at measurable levels in IMZ351 while not in IME169 (Additional file 1). Of these, of particular interest were Rav1 (regulator of the activity of vacuolar ATPase acitivty), Hog1 (global regulator of stress responses), and Mck1 (threonine/serine protein kinase that regulates DNA replication , C-metabolism, and protein kinase A activity ).
GO-term cluster analysis revealed that among the proteins with at least 50% increased levels in IMZ351 were related to stress-response terms, i.e., DNA replication stress and inefficient DNA replication , as well as autophagy and decreased protein production . In that group, Rtp6 and Cps1 were found at higher levels and described to correlate with severe N-limitation state. While a significant up-regulation of proteins involved in various stress responses was observed, no significant differences in proteins involved in nitrogen catabolite repression (NCR) and central nitrogen metabolism were observed.
Based on the experimental and modeling results, it was shown that NH3 diffusion is the main NHX transport mechanism in Mep-deficient strain IMZ351. Alternative mechanisms, like transport through K+-channels, can be excluded. In particular, the aerobic micro-titer experiments showed that the growth rate was dependent on extracellular NH3 concentration rather than the electrochemical gradient. Furthermore, the cytosolic/extracellular ratio of NHX for IMZ351 under aerobic N-limiting conditions was consistent with the ratio predicted for NH3 diffusion, but not with any transport mechanism dependent on the cell membrane potential or pmf.
By contrast with IMZ351, the observed IC/EC ratio for IME169 remained relatively constant and at least one order of magnitude higher than the ratios observed in IMZ351 across all pH values. Nevertheless, the experimental ratios did not match the predicted ratios at pH 6 and pH 7, which could be explained by a limitation in affinity (K M ) of the Mep proteins rather than the thermodynamic driving force. Notwithstanding this, our results for IME169 at different pH values clearly show that NH4 + is the transported species, opposing previous studies suggesting that Mep proteins and other Amt-class transporters carry uncharged NH3 across the membrane [42, 53].
The metabolic profile in both strains presented clear differences, like a significantly higher concentration of intracellular NHX and trehalose in the strain IMZ351. While the cause of this remains unanswered, the observation raises questions about the signaling pathways for N-limitation. Our experimental results suggest that intracellular NHX is not involved in signaling.
This (stressed) phenotype of IMZ351 revealed the system’s nature –while the cost for the transport could be reduced, secondary responses lead to ATP consumption and the aim of improved energy efficiency cannot be achieved without additional steps. This increased energy consumption interferes with the ability to apply anaerobic production conditions without decreasing the negative physiological effects from deletion of Mep proteins.
The underlying goal of this study was to engineer membrane potential-decoupled NHX assimilation for use in bulk N-containing chemical production. Although diffusion of NH3 metabolically conserves ATP in the N-assimilation process, the observed metabolic rates did not show this energy conservation improvement. The different degrees of N-limitation in both strains led to an uncoupling between of metabolic ATP saving from biomass production, as observed from the experimental N-biomass content, trehalose concentration and q ATP /q N ratio.
To enable future industrial (anaerobic) applications, elucidation and subsequent engineering of this stress response will be required.
- NH3 :
- NH4 + :
- NHX :
Sum of NH3 + NH4 + (total ammonium)
- P1a :
Protein kinase A
Proton motive force
Stress response element
Ultra-high performance liquid chromatography with isotope dilution mass spectrometry
The authors wish to thank Martijn Pinkse, Sebastiaan de Bruin, Erik de Hulster, Reza Maleki Seifar, Angela ten Pierick, Marijke Luttik, Tim Vos and Pascale Daran-Lapujade for their valuable contribution to this work. Special thanks to Prof. Dr. Ir. Sef Heijnen and Prof. Dr. Jack Pronk for their valuable feedback and critical revision of this manuscript. The authors especially thank colleagues helping with rapid sampling experiments: Camilo Suárez-Méndez, Cristina Bernal, Angel Sevilla, Francisca Lameiras, Leonor Guedes da Silva, Mariana Velasco-Alvarez and Mihir Shah.
This work was performed within the BE-Basic R&D program (http://www.be-basic.org), which was granted a FES subsidy from the Dutch Ministry of Economic Affairs, Agriculture and Innovation (EL&I). The author HFCR received a scholarship from CONACyT (Scholarship number: 212059).
Availability of data and materials
The datasets supporting the conclusions of this article are included within the article and attached supplementary materials.
HFCR: drafted and edited the manuscript, performed chemostat experiments, metabolomics analysis, data collection and analysis. NM performed strain constructions and micro-titer plate experiments, wrote the respective manuscript section and reviewed the manuscript. WH performed proteomics measurements and data analysis, and contributed to the respective manuscript section. MP supervised the proteomics measurements and contributed to the interpretation of measurement data. AJAM contributed to the design of the experiments and reviewed the manuscript. JMD contributed to the design of the experiments and reviewed the manuscript. SAW contributed to the design of the experiments and reviewed the manuscript. All authors contributed equally reviewing this manuscript. All authors read and approved the final manuscript.
The funders had no role in study design, data collection and interpretation, or the decision to submit the work for publication. The authors declare that they have no competing interests.
Consent for publication
Ethics approval and consent to participate
Not applicable. This article does not contain any studies with human participants or animals performed by any of the authors.
Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/) applies to the data made available in this article, unless otherwise stated.
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