- Original article
- Open Access
Subpopulation-proteomics reveal growth rate, but not cell cycling, as a major impact on protein composition in Pseudomonas putida KT2440
© Lieder et al.; licensee Springer 2014
- Received: 18 August 2014
- Accepted: 18 August 2014
- Published: 29 August 2014
Population heterogeneity occurring in industrial microbial bioprocesses is regarded as a putative effector causing performance loss in large scale. While the existence of subpopulations is a commonly accepted fact, their appearance and impact on process performance still remains rather unclear. During cell cycling, distinct subpopulations differing in cell division state and DNA content appear which contribute individually to the efficiency of the bioprocess. To identify stressed or impaired subpopulations, we analyzed the interplay of growth rate, cell cycle and phenotypic profile of subpopulations by using flow cytometry and cell sorting in conjunction with mass spectrometry based global proteomics. Adjusting distinct growth rates in chemostats with the model strain Pseudomonas putida KT2440, cells were differentiated by DNA content reflecting different cell cycle stages. The proteome of separated subpopulations at given growth rates was found to be highly similar, while different growth rates caused major changes of the protein inventory with respect to e.g. carbon storage, motility, lipid metabolism and the translational machinery.
In conclusion, cells in various cell cycle stages at the same growth rate were found to have similar to identical proteome profiles showing no significant population heterogeneity on the proteome level. In contrast, the growth rate clearly determines the protein composition and therefore the metabolic strategy of the cells.
- Pseudomonas putida
- Flow cytometry
- Cell cycle
Commonly applied assumptions consider microbial populations in bioreactors as uniform, thus leveling individual properties of subpopulations to averages. However, it is increasingly accepted that clonal microbial cultures comprise individuals that are not identical, differing in terms of DNA content and cell physiology (Brehm-Stecher and Johnson ; Delvigne and Goffin ). Heterogeneity of clonal microbial cultures may result from several distinct sources, either from internal biological origins, such as mutations, cell cycle decisions and age distribution, or from ‘external’ technical factors (Avery ; Müller et al. ). Notably, external factors interact with biological properties, yielding the superimposition of both impacts in the population. Here, we shed light on the impact of two key players in the origin of population heterogeneity, the growth rate and the cell cycle.
It is suspected, that biosynthesis of biotechnological interesting compounds occurs in dependency of the cell cycle, e.g. only within the stochastic B- and pre-D-phases, when cells are neither replicating nor dividing (Müller et al. ). Ackermann et al. () described for Methylobacterium rhodesianum that products like polyhydroxyalkanoates (PHAs) accumulate only when cells comprise a certain chromosome number. This phenomenon was found to occur at off-cell-cycling stages. In microbial biotechnology, heterogeneity caused by cell cycling may cause inefficiently producing subpopulations and could have significant impact on the overall process performance (Lencastre Fernandes et al. ). Here, we aim to investigate if the protein inventory of a cell, which is related to its metabolic activity, is dependent on cell cycle stages and how growth rates may influence both, protein composition and cell cycling.
Pseudomonas putida KT2440 was used as a model organism owing to its numerous qualities as an expression host, such as safety (Bagdasarian et al. ; Nakazawa and Yokota ), fast growth, a fully sequenced genome (Nelson et al. ) and high stress tolerance (Martins Dos Santos et al. ). Together with simple nutrient demand, the potential to regenerate redox cofactors at a high rate (Blank et al. ) and its amenability to genetic manipulation, P. putida is an ideal host for heterologous gene expression (Meijnen et al. ). With the advance of genome-wide pathway modeling (Puchałka et al. ) and ‘omics techniques, the way for systems-wide engineering strategies was paved to turn P. putida into a flexible cell factory chassis (Yuste et al. ). Consequently, P. putida is more and more explored and already successfully used for numerous industrial applications (Poblete-Castro et al. ; Puchałka et al. ).
In our study, we applied continuous cultivations under controlled growth conditions at defined growth rates. While (fed-) batch approaches are characterized by steadily changing environmental conditions such as media composition, steady-state modes of a chemostat, where cells are cultivated with a pre-installed growth rate, are defined by environmental conditions that remain unchanged (Carlquist et al. ). Notably, (fed-) batch cultures usually represent a mixture of cells growing with different speed as a consequence of changing environmental conditions (Unthan et al. ). Investigating a wide spectrum of growth rates with chemostat cultivation and sampling at steady state conditions gave a specific and unmasked view on the influence of the growth rate on population characteristics. Features like DNA content of the cells, protein composition and adenylate energy charge measurements were included in the study. Additionally, subpopulations with different DNA content were sorted at growth rates 0.1 h−1, 0.2 h−1 and 0.7 h−1 and analyzed for their proteome composition.
Summarizing, we investigated if cell cycling subpopulations at the same growth rate were independent and different from each other on the level of metabolic pathways, e.g. whether slow growing cells with longer cell cycling phases might specialize between proliferation and production phases. In addition, we wanted to clarify if cells invest into different protein species under rising growth rates.
Bacterial strains and cultivation conditions
Chemicals were purchased from Fluka, St. Gallen, Switzerland. Experiments were performed with P. putida KT2440 (ATCC 47054) cells originating from a single colony stored in a working cell bank at −70°C. Cells were cultivated in M12 minimal salt medium containing 2.2 gL−1 (NH4)2SO4, 0.4 gL−1 MgSO4 · 7 H2O, 0.04 gL−1 CaCl2 · 2 H2O, 0.02 gL−1 NaCl, 2 gL−1 KH2PO4 and trace elements (2 mgL−1 ZnSO4 · 7 H2O, 1 mgL−1 MnCl2 · 4 H2O, 15 mgL−1 Na3-citrate · 2 H2O, 1 mgL−1 CuSO4 · 5 H2O, 0.02 mgL−1 NiCl2 · 6 H2O, 0.03 mgL−1 NaMoO4 · 2 H2O, 0.3 mgL−1 H3BO3, 10 mgL−1 FeSO4 · 7 H2O).
A shake flask preculture (150 mL) was started from a minimal medium working cell bank (8.5 mL) with a glucose concentration of 5 gL−1. At mid-exponential growth phase, the preculture was used to inoculate the bioreactor (KLF 3.7 L, Ser. No. 10819, Bioengineering AG, Wald, Switzerland) to reach a final working volume of 1.5 L. Before inoculation, the cultivation conditions were set to 30°C, a stirrer speed of 700 rpm, a pressure of 0.5 bar and an aeration of 2 Lmin−1 sterile filtered ambient air. The pH was set and maintained at pH 7 with 25% (v/v) NH4OH. Exhaust gas composition (Blue Sense CO2 and O2, (DCP-CO2 DCP-02, Blue Sense gas sensor GmbH, Herten, Germany), dissolved oxygen and pH in the liquid phase (Ingold, Mettler Toledo GmbH, Giessen, Germany) were monitored online. After glucose depletion, the batch cultivation was continued as a chemostat. At steady state conditions, the dilution rate equals the specific growth rate μ in a chemostat set-up. Each dilution rate (and therefore growth rate) and environmental condition was kept for 5 residence times. The dilution rate was adjusted by feeding at a defined flow rate. Weight gain of the reactor was monitored and a harvest pump was started at a weight gain of 10 g. Additionally, the dilution rate was checked manually by measuring the mass of the harvest outflow within a timespan of one hour before sampling. Steady state was evaluated online via exhaust air analysis. Chemostat cultivations were performed in three individual biological replicates.
Determination of the adenylate energy charge
The adenylate energy charge (AEC) value mirrors the cellular energy status (Atkinson and Walton ) and can be assessed as follows: Biocatalytic reactions inside the cells were stopped with 35% (w/v) HClO4. 4 mL biosuspension was taken directly into 1 mL of precooled (−20°C) HClO4 solution on ice and mixed immediately (Theobald et al. ). The sample was shaken at 4°C for 15 min in an overhead rotation shaker. Afterwards, the solution was neutralized on ice by fast addition of 1 mL 1 M K2HPO4 and 0.9 mL 5 M KOH (Buchholz et al. ). The neutral solution was centrifuged at 4°C and 4,000×g for 10 min to remove cell debris, precipitated protein and potassium perchlorate. The supernatant was kept at −20°C for batch high pressure liquid chromatography (HPLC) measurements. At each sampling time, the biosuspension sample and a filtrated sample without cells was treated according to the above described procedure.
Nucleotide analysis was performed by reversed phase ion pair HPLC (Theobald et al. ). The HPLC system (Agilent Technologies, Waldbronn, Germany) consisted of an Agilent 1200 series autosampler, an Agilent 1200 series Binary Pump SL, an Agilent 1200 series thermostated column compartment, and an Agilent 1200 series diode array detector set at 260 and 340 nm. The nucleotides were separated and quantified on an RP-C-18 column that was combined with a guard column (Supelcosil LC-18-T; 15 cm × 4.6 mm, 3 μm packing and Supelguard LC-18-T replacement cartridges, 2 cm; Supelco, Bellefonte, USA) at a flow rate of 1 ml/min. A gradient elution method (Cserjan-Puschmann et al. ) was adapted and performed with two mobile phases, buffer A (0.1 M KH2PO4/K2HPO4, with 4 mM tetrabutylammonium sulfate and 0.5% (v/v) methanol, pH 6.0) and (ii) solvent B (70% (v/v) buffer A and 30% (v/v) methanol, pH 7.2). The following gradient programs were implemented: 100% (v/v) buffer A from 0 min to 3.5 min, increased to 100% (v/v) B until 43.5 min, remaining at 100% (v/v) B until 51 min, decreased to 100% (v/v) A until 56 min and remaining at 100% (v/v) A until 66 min.
Sample preparation and staining for flow cytometry
Samples for flow cytometry were washed with PBS, resuspended in cryo-protective solution (15% (v/v) glycerol in PBS according to Jahn et al. ()) and stored at −20°C.
Deep-frozen cell samples were thawed on ice and centrifuged for 2 min at 8,000×g and 4°C to remove the cryo-protective solution. The supernatant was discarded, the cells were resuspended in ice cold PBS and adjusted to an optical density of OD600nm = 0.05 in 2 mL volume. For DNA staining, the cells were centrifuged, taken up in 1 mL permeabilization buffer (0.1 M citric acid, 5 gL−1 Tween 20), incubated for 10 min on ice, centrifuged again and the supernatant was removed. Finally, cells were resuspended in 2 mL ice cold staining buffer (0.68 μM DAPI, 0.1 M Na2HPO4), filtered through a Partec CellTrics mesh (Partec, Germany) with 30 μm pore size and stored on ice until analysis.
Flow cytometry and cell sorting
Flow cytometry was performed using biological duplicates. For each biological replicate two technical replicates were investigated using a MoFlo cell sorter (Beckman-Coulter, USA) as described before (Jahn et al. ; Jehmlich et al. ). Forward scatter (FSC) and side scatter signals (SSC) were acquired using blue laser excitation (488 nm, 400 mW) and a bandpass filter of 488/10 nm together with a neutral density filter of 2.0 for emission. The DAPI fluorescence was recorded using a multi-line UV laser for excitation (333–365 nm, 100 mW) and a bandpass filter of 450 ± 30 nm for emission. The datasets were annotated according to the miFlowCyt standard (Lee et al. ) and are publicly available on the FlowRepository database (Spidlen et al. ). Cells were sorted at the most accurate mode (single cell, one drop) with a sorting speed of 4,000 s−1 and a sample chamber cooled to 4°C. For cell sorting a total number of 5 × 106 cells per replicate were directly sorted on a filter well plate (LoProdyne™ membrane with 0.45 μm pore size, Nunc, Germany) and the residual buffer was constantly drawn off by an exhaust pump. After sorting, the filter membrane was washed three times with 200 μL PBS, air dried and stored at −20°C for further analysis.
Identification of proteins by LC-MS-MS
For quantitative proteomics, the filter membrane was cut into smaller pieces and treated by trypsin for whole cell proteolytic digestion as described in Jahn et al. (). The obtained peptide solution was purified using the ZipTip protocol (Millipore, USA), dried in a vacuum concentrator at 30°C and finally taken up in 20 μL 0.1% (w/v) formic acid. The solution was separated by nano-ultra performance liquid chromatography and measured by an LTQ Orbitrap XL (Thermo Fisher Scientific, Germany) as described in Jahn et al. ().
Mass spectra were analyzed by MaxQuant v220.127.116.11 (Cox and Mann ) for protein identification and label-free quantification with the genome database of P. putida KT2440 and the settings given in Jahn et al. (). The label-free quantification (LFQ) values were used for further data analysis and can be found in the Additional file 1. The mean, standard deviation and relative quantity of replicates in relation to the reference population (RP, μ = 0.2 h−1, mean of two biological replicates) was calculated. The RP was sorted in order to exclude influences of the sorting procedure on the proteomic content. Unsorted cells of the 0.2 h−1 grown population were used as an unaffected control population (CP). Student's t-test was performed for significance testing (p < 0.05) of single proteins. Proteins were annotated using COG (clusters of orthologous groups) (Tatusov et al. ) and clustered in two hierarchical levels of metabolic pathways (‘metabolism’, ‘pathway’). Protein clusters were tested for significant changes using the R Bioconductor (www.bioconductor.org) packages GAGE (Luo et al. ) and GlobalTest (Goeman et al. ), setting p < 0.05 and a relative fold change (FC) of 1.5 (log2 FC > 0.58) as thresholds. Hierarchical groups were visualized using a color-coded circular treemap (Jahn et al. ).
The yield of biomass on glucose increased gradually by 10% from μ = 0.1 h−1 to μ = 0.5 h−1. Further rise of the growth rate resulted in yield reductions, returning to the level at μ = 0.1 h−1 (−10%). The energetic capacity of the cells can be estimated via AEC, taking the relative contribution of all three phosphorylated forms of adenine into account. The AEC was found to be stable with increasing growth rate until μ = 0.4 h−1. Further increasing the growth rate resulted in a reduction of the AEC level by – 18% (p-value < 0.01), which was almost the same at maximum growth, still staying in the range of expected physiological levels. The specific glucose uptake rate qs was increasing linearly with increasing growth rate.
To investigate whether subpopulations with different DNA content show physiological differences as well, we sorted the cell population at three growth rates (0.1 h−1, 0.2 h−1 and 0.7 h−1) into subpopulations containing single (C1), double (C2) or more than double chromosome content (Cx) aiming to analyze their proteome profile as the basis of their phenotype. In total, 677 unique proteins could be detected. 351 proteins were found in at least one replicate of all subpopulations and 245 proteins were found across all replicates. 707 different functions of 647 unique proteins were annotated using the database of clusters of orthologous groups (COG) (Tatusov et al. ) (Additional file 2: Figure S2). 95.2% of the non-sorted control population (CP) proteome could be found in the reference population (RP) proteome without significant changes, indicating only a small influence of cell sorting on protein recovery and confirming the quality of the analysis.
Significant changes in protein quantity were defined by exceeding a threshold of more than 1.5 fold change (FC) in combination with a p-value < 0.05 (Student's t-test). Changes in metabolic pathways were detected using GAGE and GlobalTest gene set analysis (Goeman et al. ; Luo et al. ) applying the same significance filter as for the individual proteins.
In contrast, subpopulations C2 and Cx of fast growing cells (μ = 0.7 h−1) revealed higher presence of proteins grouped in the pathway ‘Translation, ribosomal structure and biogenesis’ (Translation), while proteins of 'Signal transduction mechanisms’ (Signaling) and ‘Lipid transport and metabolism’ (Lipids), were significantly underrepresented. The faster growth was reflected in proteins related to translation and therefore protein production. Here, 11 tRNA synthetases and 25 ribosomal proteins showed significantly higher abundance. In lipid metabolism, mostly enzymes of beta-oxidation were found in lower presence at fast growth (Figure 5). The supposed down regulation of the ‘Cell Cycle’ (C2 versus Cx) was mainly due to the single protein change of the poorly characterized PP_3128.
In summary, the proteome of cells differing in DNA content but of identical growth rate was highly similar, whereas the proteome of cells cultivated at different growth rates was significantly diverging in particular pathways.
Considering the influence of different growth rates on the population, proteome analysis revealed that slow growth triggered starvation response, while fast growing cells displayed accelerated protein synthesis and alleviated stress physiology. In slowly growing cells, proteins connected to PHA synthesis and glycerol hydrolysis were amplified, indicating higher PHA carbon storage activity. Additionally, these cells showed protein patterns anticipating increased motility and chemotaxis response. Notably, low qS values of slowly growing cells (μ = 0.1 h−1) were not reflected on the energetic state of the population. AEC values did not differ significantly between slow and moderate growth rates of 0.1 h−1 and 0.4 h−1, respectively. Chemotaxis and cellular motility as a response to carbon-poor conditions are well-known phenomena in natural environments (Harshey ; Soutourina and Bertin ). Our observations in slowly growing cells are in agreement with findings of transcriptome studies in ‘average populations’ of other species. For instance, studies in E. coli showed higher expression of genes involved in motility at slower growth rates in direct comparison to faster growth conditions (Nahku et al. ) and studies in Saccharomyces cerevisiae showed significant amplification of carbon storage metabolism at slow growth (François and Parrou ).
Fast growing cells were obviously investing resources in proteins involved or related to the translation machinery. Multiple ribosomal proteins as well as tRNA synthetases were highly abundant fostering protein/biomass production (Figure 5). This finding is also in agreement with observations in eukaryotes like S. cerevisiae (Rebnegger et al. ) and prokaryotes such as Salmonella typhimurium (Schaechter et al. ). Additionally, proteins of typical carbon storage pathways, e.g. PHA synthesis, were less abundant in P. putida KT2440. Proteins of lipid biosynthesis, especially involved in beta oxidation were also lowered in fast growing cells compared to RP. This observation is in agreement with the lower abundance of the PHA synthesis proteins, as the beta oxidation provides precursors for this pathway (Aldor and Keasling ).
To our surprise, the almost 6.5-fold increase of the specific glucose uptake rate with increasing growth rate (Figure 2), was not mirrored by major changes among proteins involved in carbohydrate and energy metabolism.
Notably, relative changes of protein quantity can be elucidated with the method applied here. Absolute changes per cell, dependent on the growth rate were not measured with the applied workflow, as it was first shown for the sum of proteins by Schaechter et al. (). Their pioneering studies described an exponential increase in protein, DNA and RNA contents and therefore, cell size with increasing growth rates (Bremer and Dennis ; Maaløe and Kjeldgaard ; Schaechter et al. ). In our study, the relative cell size estimation was acquired using FSC. In accordance to various other cell cycle analyses, the FSC increased with increasing growth rates (Donachie ; Hewitt et al. ; Neumeyer et al. ; Skarstad et al. ) (Figure 3). Following the rational of Schaechter et al. (), this phenomenon reflects increasing protein contents per cell. We presume that the increased amount of cellular glucose uptake is proportional to the elevated production of proteins, thus increasing absolute protein quantity but leaving relative quantity unchanged.
Studying the putative impact of growth rate and cell cycle stage on the functional diversity of a population, the growth rate is obviously a major determinant for cellular protein composition, as found in our chemostat studies. Growth and cell cycle were clearly linked, but subpopulations showing different DNA content showed only small differences in cellular physiology at the same growth rate. The detection of FtsZ in a significant higher abundance in the C2 subpopulation, which is preparing for division after finishing replication, is in agreement with its assigned function as a proposed diffusible factor (Teather et al. ) initiating cell division (Chien et al. ). Despite this cell cycle related finding, subpopulations showed almost identical protein patterns irrespective of cell sizes, anticipated protein mass (Lindmo ; Rønning et al. ) and DNA content.
Surprisingly, no signs for a specialization of cells in different cell stages for e.g. carbon storage or protein production/growth could be observed that could support the hypothesis of shared tasks of subpopulations in B- and pre-D/D-phases during the cell cycle. This result is remarkable: subpopulations distinguished by DNA content appear to be physiologically highly similar provided that the growth rate is the same.
Although we are aware that subpopulations do not mirror single cell proteome compositions, the high resemblance of the subpopulations proteome patterns at the various growth rates point to their nearly identical physiological state.
One may argue whether this finding was influenced by the operation mode ‘chemostat’. We identified the high similarity among subpopulations by installing distinct growth rates, because superimposing impacts in classical (fed-) batch fermentations would have prevented the unequivocal growth-to-subpopulation analysis. However, the chemostat approach might have excluded the detection of subpopulations with different protein contents because this ‘growth rate filter’ was installed. Assuming that cells aim to grow with the least energetic burden as possible, cellular protein compositions should be optimized at a given growth rate. Therefore, it could not be excluded, that subpopulations showing different protein patterns may have existed, but were washed-out because they could not achieve the required growth rate. While the latter demands for further in-depth analysis, the determining impact of growth on cell cycle and subpopulations is clearly visible. It gives rise to the assumption that the cell cycle itself has a minor impact on population heterogeneity under the conditions tested.
This work was supported within the ERA-IB / ERA-NET scheme of the 6th EU Framework Programme (0315932B).
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