Abstract
Recent advances in the modeling of microbial growth and metabolism have shown that growth rate critically depends upon the optimal allocation of finite proteomic resources among different cellular functions and that modeling growth rates becomes more realistic with the explicit accounting for the costs of macromolecular synthesis, most importantly, protein expression. The “proteomic constraint” is considered together with its application to understanding photosynthetic microbial growth. The central hypothesis is that physical limits of cellular space (and corresponding solvation capacity) in conjunction with cell surface-to-volume ratios represent the underlying constraints on the maximal rate of autotrophic microbial growth. The limitation of cellular space thus constrains the size the total complement of macromolecules, dissolved ions, and metabolites. To a first approximation, the upper limit in the cellular amount of the total proteome is bounded this space limit. This predicts that adaptation to osmotic stress will result in lower maximal growth rates due to decreased cellular concentrations of core metabolic proteins necessary for cell growth owing the accumulation of compatible osmolytes, as surmised previously. The finite capacity of membrane and cytoplasmic space also leads to the hypothesis that the species-specific differences in maximal growth rates likely reflect differences in the allocation of space to niche-specific proteins with the corresponding diminution of space devoted to other functions including proteins of core autotrophic metabolism, which drive cell reproduction. An optimization model for autotrophic microbial growth, the autotrophic replicator model, was developed based upon previous work investigating heterotrophic growth. The present model describes autotrophic growth in terms of the allocation protein resources among core functional groups including the photosynthetic electron transport chain, light-harvesting antennae, and the ribosome groups.
How Fast Can Cyanobacteria Grow?
There is a very wide range of maximal growth rates observed among cyanobacterial strains (Carr and Whitton, ). Fast growing model cyanobacterial strains can be grown with doubling times in the range of 3–6 h under optimal conditions (Binder and Chisholm, ; Nomura et al., ; Kim et al., ; Ludwig and Bryant, ). On the other hand, many cyanobacterial strains have doubling times on the order of once per day (Carr and Whitton, ). Moreover, even the fastest growing cyanobacteria are still much slower growing than many heterotrophic bacteria and yeasts. Furthermore, the factors accounting for the diversity of maximal rates of cyanobacterial growth remain poorly understood and it appears that autotrophic growth tends to be slower than heterotrophic growth, which can be as short as ~10 min doubling times (Labbe and Huang, ). This is important because researchers often include “fast growth” among the criteria in choosing a cyanobacterial strain for engineering. Since the fastest rate of growth in heterotrophs occurs in “rich” media containing abundant amino acids and cofactors and since the main macromolecular investment in cell growth is the synthesis of proteins, then a reasonable hypothesis is that autotrophic metabolism in cyanobacteria results in slower maximal growth because of the necessity for the synthesis of the amino acids and all other cell components from CO2. However, assuming it is the burden of synthesizing amino acids, then the question arises whether this is because of the energetic cost of making amino acids, such as ATP consumed per amino acid and “opportunity costs” of not using ATP for other cell functions that contribute to cell reproduction. A bioinformatics analysis using codon bias as an indicator for expression rates found that less expensive amino acids are preferably utilized for highly expressed protein (Akashi and Gojobori, ). However, energetically more expensive amino acids also tend to require more biosynthetic steps, and consequently a greater number of enzymes. Moreover, a more exhaustive analysis found that amino acid utilization rates for protein were only weakly correlated, if at all, with the bioenergetic costs of their synthesis (Barton et al., ). Or is it something else, such as greater cellular space devoted to the corresponding biosynthetic enzymes? As discussed below, recent theoretical and experimental studies point to the latter and suggest that the ultimate speed limit relates to the physical constraints of packing all necessary molecular machinery, small molecules, and ions into the confined space (cytoplasmic and membrane) of the cell yet have small enough cell dimensions to allow sufficient nutrient exchange (Figure 1). Analysis of the physical state of cytoplasmic water in E. coli under different osmotic conditions indicates that macromolecular crowding limits growth rate, probably through decreasing the “kinetics of some biopolymer diffusion processes” (Cayley and Record, ). Accordingly, intracellular crowding appears to be the main constraint to growth and sets the upper bound on the size of the proteome. Evidence for this includes the analysis of the impact of protein overexpression on maximal growth rates (Scott et al., ; Scott and Hwa, ; You et al., 2013) and the effects of crowding on diffusion within the bacterial cell (Klumpp et al., ; Soh et al., ; Parry et al., ). Crowding also would affect the size to the metabolome, primarily because of the limited amount of free water, as discussed below. Based on these considerations, the total size of the proteome is likely bounded by intracellular crowding constraints and, assuming a relatively fixed amount of dissolved ions and metabolites1, the allocation of proteomic resources becomes a “zero sum game.” This is one of the key points for this discussion since we are trying to understand the physical basis optimal proteomic allocation strategies. As discussed below, the results of modeling studies and the consideration of “overflow” metabolism is best explained by a limitation in the total amount of protein that can be crowed into a cell, yet remain soluble and diffusionally mobile. From that perspective, it could be that the autotrophic lifestyle requires a comparatively large investment into photosynthetic and other anabolic proteins. This would include the large investment into extensive internal membranes for photosynthetic machinery as well as the need for large amounts of the catalytically inefficient carbon-fixing enzyme, Rubisco. Correspondingly, this comparatively greater investment would come at the expense of the macromolecular machinery dedicated to cell duplication including ribosomes, initiation factors, cell division proteins, and all the metabolic precursors required for the duplication. Conversely, it might be expected that very fast growing bacteria (Labbe and Huang, ) have a greater investment in the machinery for cell duplication and a streamlined metabolic capacity that constituted by a minimal set of core enzymes, transporters, and metabolites for the provision of precursors to support the operation of the cell duplication machinery.
Figure 1
Engineering and Modeling Cyanobacteria
Because of their comparative cellular simplicity and ease of genetic manipulation, cyanobacteria are the object of numerous biotechnological efforts for metabolic engineering for the renewable production of biofuels and high-value products. Compared with algae and plants, cyanobacteria are easier to genetically modify and are amenable to organism-wide metabolic modeling, which are attributes that lend themselves to synthetic biology approaches [for current review see Berla et al. (
In parallel with this progress in genetic engineering of desired physiological characteristics into cyanobacteria, systematic modeling approaches for understanding the productivity of genetically modified cyanobacteria have been developed. To gain insight on the physiological characteristics of the strains targeted for engineering studies, researchers have developed large-scale models of metabolic networks based upon annotated gene content that has been deduced from genomic sequences for a number of both heterotrophic and autotrophic bacteria [technical approaches reviewed in Covert et al. (
There are also important experimental applications for reconstructed metabolic networks. This includes metabolic flux analysis (MFA), which uses pulse-labeling of cells with substrate atoms tagged using stable isotopes. This approach has been applied in cyanobacteria to analyze metabolic fluxes under autotrophic conditions (Young et al., 2011). Again, metabolic network models are used, but they are used as input to fit the experimental labeling patterns (Young, 2014). Thus, metabolic network re-construction is of utility from both the experimental and theoretical perspectives and allows insight into the details and global features of microbial growth and metabolism.
Course-Grained Models of Microbial Metabolism
Besides the detailed and metabolically realistic FBA models mentioned above, simpler “course-grained” modeling approaches to understanding growth and global features of microbial growth have been developed. Of these, the models of heterotrophic microbial growth (Molenaar et al.,
Another course-grained modeling approach, which from the Hwa group, also considers the size of the proteome as a fundamental limiting factor in heterotrophic microbial growth (Scott et al.,
Figure 2

Allocation of the proteome among different sectors as defined by the analysis of growth in the development of a phenomenological theory regarding its control (Scott et al.,
While these approaches have not been applied to cyanobacteria, there is already a rich and advanced set of modeling efforts for algae and cyanobacteria that are oriented toward autotrophic productivity in natural marine and aquatic environments [c.f. Ross and Geider (
Overflow Metabolism is a Dissipative Process That Reflects the Proteomic Constraints of Microbial Growth
It is useful to consider one of the puzzles of microbial physiology: the seeming wastefulness in the phenomenon of metabolic spilling. In heterotrophic microbes, metabolic spilling involves the release of incompletely catabolized energy-rich metabolites and has physiological roles that extend beyond biochemical considerations such as redox balancing. Instead, it appears necessary for maximal growth under certain trophic conditions despite the apparent wastefulness of the process. When heterotrophic cells have an excess of a carbon/energy source they may metabolize this compound using less efficient pathways (e.g., lower ATP yield per substrate) with the consequent wasteful release of energy-rich compounds such as ethanol, acetate, and lactate despite the fact that environmental and physiological conditions would allow for more energy-efficient utilization of the carbon source. For example, the well-known Pasteur effect, which involves metabolic switching between efficient and less efficient pathways. Here, yeast cells are observed to switch between less energy-efficient fermentation and more efficient aerobic metabolism by depending upon the availability of oxygen. However, what is less discussed are the circumstances where the Pasteur mechanism is over-ridden and fermentative metabolism occurs even under aerobic conditions – i.e., overflow metabolism occurs. This situation, known as the Crabtree effect in yeasts (van Dijken et al., 1993), occurs under conditions of excess substrate carbon and is characterized by the operation of fermentation pathways even when oxygen as a terminal electron acceptor is present, potentially allowing the more efficient utilization of substrate. This phenomenon also occurs in bacteria and tumor cells under conditions of heterotrophic substrate excess and, interestingly, under conditions of nitrogen limitation. Although metabolically wasteful, utilization of low efficiency enzymes appears to allow for faster growth under these regimes. Apparently, the wasteful metabolism reflects a tradeoff that also rewards the minimization of costs for the catabolic enzymes, with the cost of the enzymes being either the relative costs of synthesis of the enzymes or the relative costs of cytoplasmic space occupancy by the enzymes of limited cytosolic space (see next section). These costs are summarized by the phrase “proteomic limitation” as modeled in advanced FBA models that take account macromolecular expression (O’Brien et al.,
Overflow metabolism in autotrophs is less studied than in heterotrophs, but may also play important physiological roles. Though not metabolic energy spilling per se, all organisms capable of oxygenic photosynthesis, including cyanobacteria, have the ability to dissipate excess light energy in the form of non-photochemical quenching (NPQ) (Niyogi and Truong,
“Proteomic Limitation” of Growth Rates is Due to Crowding Limits within the Cell
A common thread that emerges in the different modeling approaches discussed above is the necessity to include a constraint on the size or expression cost of the cellular proteome in order to derive critical features of microbial growth. Only when protein costs are explicitly included in the optimization models do we find that comprehensive predictions of metabolism possible. The case in point is the prediction of overflow metabolism in heterotrophs. Expression of metabolically inefficient, but less costly (protein expression cost) pathways leads to maximal growth rates under conditions of nutrient excess and accounts for the efficacy of overflow metabolism in maximizing cell growth rates. On the other hand, expression of metabolically more efficient (non-overflow) pathways catalyzed by enzymes with a higher proteomic cost, lead to maximal growth rates under conditions of nutrient limitation (Molenaar et al.,
What sets the upper bound on the maximal growth rate rates under saturating nutrient and light conditions for cyanobacteria? There is compelling evidence that the packing density of molecules and the solvent capacity of the cytoplasm along with the packing density of membrane complexes in microbial cell membranes all place severe limits on the size of the proteome in a microbial cell (Beg et al.,
Macromolecular processes may be rate-determined by crowding limitations and this may affect the rate that the components of the cell can be duplicated. These limitations can be expressed in terms of characteristic transit times for the occurrence of productive collisions of metabolic and macromolecular reactants, which is controlled by the intercellular diffusional parameters involved. Theoretical analysis using this approach and using the simplifying assumption of spherical cell shapes, calculates the optimal size for a generic bacterial cell to be slightly larger than one micron, close to actual sizes in nature (Soh et al.,
While there is a good argument that proteomics costs in the form of limited space constrain maximal growth rates, one can ask whether the same constraints apply to growth in the nutrient-limited region of the growth versus nutrient availability curve? It is possible that under certain conditions, the expression of additional nutrient uptake and assimilation proteins could partially or entirely alleviate the nutrient limitation, but this up-regulated expression may begin to compete for cellular occupancy space with other important functional classes of protein. Nevertheless, there are also conditions where no amount of increased expression of uptake proteins can alleviate a deficiency of an essential nutrient if the nutrient is present only in vanishingly small amounts. Thus, it is conceptually useful to consider the two domains of growth limitation as metabolically limited and proteomically limited (Figure 1), referring to the nutrient-limited submaximal growth rate and the nutrient saturated maximal growth rate, respectively (O’Brien et al.,
Hypothesis: Proteomic Limitations within the Cyanobacterial Cell Constrain Maximal Growth Rates and Photosynthetic Adaptation
The overall hypothesis is that growth rates are constrained by the limits on the total amount of proteins and other macromolecules that can be fit inside a cyanobacterial cell. Space and crowding constraints combined with the restrictions on surface-to-volume ratios are hypothesized to be the fundamental physical restrictions on the composition and function of the microbial cell, including cyanobacteria. As suggested below, this results in a novel and testable explanation for reductions in growth under conditions of osmotic stress. Surface-to-volume ratios, combined with cell shape, determine the capacity for nutrient and waste exchange across the cell boundaries and give an upper limit on the size of microbial cells (Soh et al.,
Hypothesis 1
Lowered rates of cell growth in salt-adapted cultures are due to global reductions in the concentrations of macromolecules and metabolites in the cytoplasm. There is strong evidence that growth rates in E. coli are inversely proportional to osmotic stress and that this is due to molecular crowding that is exacerbated by the necessity for the accumulation of compatible osmolytes in the cytoplasm (Cayley et al.,
Hypothetical Modeling of the Consequences of Proteomic Limitations in the Growth and Allocation of Proteomic Resources in Cyanobacteria
To evaluate the imposition of the constraint of a finite proteome in relation to photosynthetic growth of a microbe, an optimization model was constructed based upon the “autocatalytic replicator” models of Molenaar et al. (
Figure 3

A simplified autocatalytic replicator model of cyanobacterial growth. The model consists of a simple set of enzymes (blue outlined boxes), metabolites (yellow boxes), and membrane structural components (green objects) representing functional classes of molecules (e.g., enzyme “ribosome” represents are ribosomal proteins and those affiliated with protein synthesis). The proteins interrelated by a stoichiometric matrix and kinetic equations as described in the text. The model optimizes the allocation of finite proteomic resources among the different proteins (as protein synthesis, blue arrows) to achieve maximal growth rates. Consistent with the observation that microbial growth rates scale in direct proportion to the number of ribosomes, this “ribosome centric” model defines a set of “enzymes” (light blue boxes) that feed precursors to ribosomes and are, in turn, subject to synthesis by the ribosomes. Growth rates correspondingly correlate with flux rates for the generation of precursors for protein synthesis. The model was implemented in GAMS software environment (Andrei,
Effects of Light Intensity on Growth Rates at Different Concentrations of Available Inorganic Substrate
The behavior of the model under different light and substrate conditions was explored by iteratively varying these two environmental conditions. Each iteration computed the optimal distribution of proteomic resources among each of the different enzyme groups with the overall mathematical objective of maximizing the growth rate. Figure 4 shows the increase in growth rate as a function light intensity at three different substrate levels. The simulated growth rate as a function of light intensity was observed, as expected, to exhibit a saturation behavior that is modulated by substrate availability. Although the model is too simple to specify it, the substrate could represent inorganic carbon and each of the three curves would represent the light saturation behavior of autotrophic cell as a function of inorganic carbon availability. Besides this lack of specificity, the present model has the additional limitation of not considering important physiological characteristics, such as the photosystem II to photosystem I ratio, which are known to be regulated as a function of irradiance and inorganic nutrient availability. Nevertheless, the current model does provide a first approximation of predicted optimal physiological responses to alterations in environmental conditions. When the allocation of the proteome is examined for one of the curves (high light) in this computational experiment, it is found that the fraction of light-harvesting complexes (LHC) decreases when plotted as a function of growth rate. This is expected since light is limiting growth early in the light saturation curve and at low growth rates with these conditions is reflected by the near linear decrease in the fraction of the proteome composed of LHC due to the fact that a smaller antenna provides the sufficient excitation of the PSET. It is worth noting that PSET is also predicted to be changing in relative abundance as a function of growth rate during light-limited growth, so that the amount of LHC providing excitation energy is adjusted to a “moving target” of different PSET levels. The model predicts that PSET increases with increasing growth rates, which fits with the expectation that it should parallel the rate of carbon fixation and thus biomass accumulation in vivo. A similar predicted increase in the allocation of proteome toward PSET is also observed for substrate limitation simulation (not shown). Since most chlorophyll in cyanobacteria is associated with reaction centers, the prediction of higher PSET with increasing growth rates leads to the prediction that faster growing cyanobacteria should have higher chlorophyll contents on a per cell basis. Evidence for higher levels of chlorophyll per cell in cyanobacteria have indeed been observed for light-limited (Deblois et al.,
Figure 4

Simulated effect of light intensity and inorganic substrate concentration on photoautotrophic growth rate and proteome allocation. Growth rates increase with light intensity, but rates saturate at different levels set by different levels of substrate concentration (Left). Allocation of the proteome to ribosomes (RIB) and photosynthetic electron transport (PSET) and light-harvesting complexes (LHC) as a function of growth rate (Right Panel) using data from the high light simulation shown in the left panel.
Hypothesis 2
Species-specific differences in the maximal growth rates of cyanobacteria are due to different proteomic allocations into niche-specific proteins.
The reported doubling times of cyanobacteria ranges from ~3 h to one or more days. We can use the above considerations to formulate the following hypothesis for why different species of cyanobacteria have different maximal growth rates: depending upon the niche they are evolutionarily adapted to, different species may have more or less total allocation of protein resources to NAPs. Hypothetically, cyanobacteria that are adapted to complex environments will need to express additional proteins beyond the core set of proteins needed for autotrophy. Cyanobacteria with smaller “fixed” fractions of NAPs will have the capacity for faster growth because they will be able to devote a greater fraction of the proteome to this core set of proteins, although they would correspondingly have less capacity to adapt to non-ideal environments. The fastest growing cyanobacteria would thus have the most proteomic resources devoted to core functions of autotrophic metabolism and minimal allocation of proteomic resources to specialized nutrient uptake and assimilation, defense mechanisms, and other NAPs. To simulate this, the model (Figure 3) includes a fraction of the proteome that is fixed and representing the NAP. To explore this idea, the simulation was performed at two different levels of NAP with the outcome showing that a large investment in NAP indeed predicts a large decrease in growth rate as might be expected (Figure 5, top panels). This observation is formally identical to the production of heterologous protein in the original heterotrophic models (Molenaar et al.,
Figure 5

The effects of the expression of non-core, “niche-adaptive protein (NAP)” on growth and expression of core autotrophic functions. Upper graphs depict the simulated distribution of the proteome holding the NAPs at 5% (upper left) or 60% (upper right) of the total proteome and the corresponding growth rates (μ) at saturating levels of light (hν) and substrate (S). Lower graphs show that the relative proportions of the other sectors are similar despite the reduction of their net amount due to displacement by the NAPs. Sectors correspond to functional protein groups: inorganic substrate transport and assimilation proteins (STA), photosynthetic electron transport chain (PSET) that generates ATP and reductant, precursor biosynthesis enzymes (PRB). The main difference with the original models of Molenaar et al. (
The last set of simulations that were performed to investigate the consequence of engineering cells to divert metabolic precursors toward an excreted “energy” product (Figure 6). This scenario might apply to cells that are engineered for biofuel production, for example. The simulation is highly simplified in the sense that it only considers the diversion of ATP and reductant toward a hypothetical excreted product and ignores the more realistic inclusion of diversion of a fraction of the material substrates (S) toward this end. A more realistic model will result in proteome allocations that depend upon the chemical characteristics of the excreted product, most notably, the C/H ratio of its chemical formula. Nevertheless, the findings are interesting and show that under these simplified circumstances, the model predicts a resultant re-distribution of the proteome in accord with what is observed in experiment. It has been shown that the cyanobacteria engineered to excrete sugar have adjusted their metabolism to have increased total photosynthetic capacity presumable to compensate for the genetically imposed drain on their metabolism (Ducat et al.,
Figure 6

Simulated diversion of energy precursors to excreted products alters the allocation of the proteome. Product diversion is defined as the excretion of 80% of the energy precursor for engineered product synthesis. Only ATP and reductant are considered in this highly simplified model, whereas a more realistic model will depend upon the chemical characteristics of the excreted product, most notably, the C/H ratio of its chemical formula. See Figure 5 and text for definitions of the functional protein groups of the model.
Conclusion
The statistician, George Box stated that “essentially, all models are wrong, but some are useful” (Box and Draper,
Optimal growth ultimately requires that allocation of the proteins constituting different functional modules of the proteome result in a set of flux balances between the production and utilization of cellular metabolites. It has been argued here that the main reason for protein allocation being a zero sum game is that molecular crowding places a ceiling on the amount of protein in a bacterial cell. In the ARM, the amount and activity of the PSET proteins is assumed to be sufficient to supply ATP and reductant at rates that match the demand of enzymes involved in the generation precursors (PRC) for macromolecular synthesis. Natural selection has tuned the regulation to ensure optimal protein levels to achieve this balance. As noted, the ARM does not specify mechanisms, but it seems likely that metabolic intermediates that accumulate or are depleted under conditions of imbalance are good candidates to serve as allosteric modulators of gene expression. This type of regulation is observed, as one example, for control of the inorganic carbon uptake mechanism proteins (Nishimura et al.,
Supplementary Material
The Supplementary Material for this article can be found online at http://www.frontiersin.org/Journal/10.3389/fbioe.2015.00001/abstract
Statements
Acknowledgments
I would like to thank the authors of Molenaar et al. (
Conflict of interest
The author declares that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
Footnotes
1.^As far as the author is aware, information on possible changes in the total size of the metabolome as a function of different conditions is not readily available.
2.^However, this situation has dramatically changed with the development of FBA metabolic models that have been extended to include gene expression and proteomic constraints, which correspondingly gives predictions for conditions where overflow metabolism occurs (O’Brien et al.,
References
1
AkashiH.GojoboriT. (2002). Metabolic efficiency and amino acid composition in the proteomes of Escherichia coli and Bacillus subtilis. Proc. Natl. Acad. Sci. U.S.A.99, 3695–3700.10.1073/pnas.062526999
2
AndreiN. (2013). Nonlinear Optimization Applications Using the GAMS Technology. New York: Springer.
3
AngermayrS. A.PaszotaM.HellingwerfK. J. (2012). Engineering a cyanobacterial cell factory for production of lactic acid. Appl. Environ. Microbiol.78, 7098–7106.10.1128/AEM.01587-12
4
AtkinsonD. E. (1977). Cellular Energy Metabolism and its Regulation. New York: Academic Press.
5
BartonM. D.DelneriD.OliverS. G.RattrayM.BergmanC. M. (2010). Evolutionary systems biology of amino acid biosynthetic cost in yeast. PLoS ONE5:e11935.10.1371/journal.pone.0011935
6
BegQ. K.VazquezA.ErnstJ.De MenezesM. A.Bar-JosephZ.BarabásiA.-L.et al (2007). Intracellular crowding defines the mode and sequence of substrate uptake by Escherichia coli and constrains its metabolic activity. Proc. Natl. Acad. Sci.U.S.A.104, 12663–12668.10.1073/pnas.0609845104
7
BerlaB. M.SahaR.ImmethunC. M.MaranasC. D.MoonT. S.PakrasiH. (2013). Synthetic biology of cyanobacteria: unique challenges and opportunities. Front. Microbiol.4:246.10.3389/fmicb.2013.00246
8
BinderB. J.ChisholmS. W. (1990). Relationship between DNA-cycle and growth-rate in Synechococcus Sp strain Pcc6301. J. Bacteriol.172, 2313–2319.
9
BoxG. E. P.DraperN. R. (1987). Empirical Model-Building and Response Surfaces. New York, NY: Wiley.
10
CarrN. G.WhittonB. A. (1982). ““The biology of cyanobacteria”,” in Botanical Monographs, Vol. 19, eds CarrN. G.WhittonB. A. (Oxford: Blackwell Scientific). 677 p.
11
CarrieriD.PaddockT.ManessP.-C.SeibertM.YuJ. (2012). Photo-catalytic conversion of carbon dioxide to organic acids by a recombinant cyanobacterium incapable of glycogen storage. Energy Environ. Sci.5, 9457–9461.10.1039/c2ee23181f
12
CayleyD. S.GuttmanH. J.RecordM. T.Jr. (2000). Biophysical characterization of changes in amounts and activity of Escherichia coli cell and compartment water and turgor pressure in response to osmotic stress. Biophys. J.78, 1748–1764.10.1016/S0006-3495(00)76726-9
13
CayleyS.RecordM. T.Jr. (2003). Roles of cytoplasmic osmolytes, water, and crowding in the response of Escherichia coli to osmotic stress: biophysical basis of osmoprotection by glycine betaine. Biochemistry42, 12596–12609.10.1021/bi0347297
14
CovertM. W.SchillingC. H.FamiliI.EdwardsJ. S.GoryaninI. I.SelkovE.et al (2001). Metabolic modeling of microbial strains in silico. Trends Biochem. Sci.26, 179–186.10.1016/S0968-0004(00)01754-0
15
DaleyS. M.KappellA. D.CarrickM. J.BurnapR. L. (2012). Regulation of the cyanobacterial CO2-concentrating mechanism involves internal sensing of NADP+ and alpha-ketogutarate levels by transcription factor CcmR. PLoS ONE7:e41286.10.1371/journal.pone.0041286
16
DebloisC. P.MarchandA.JuneauP. (2013). Comparison of photoacclimation in twelve freshwater photoautotrophs (Chlorophyte, Bacillaryophyte, Cryptophyte and Cyanophyte) isolated from a natural community. PLoS One8:e57139.10.1371/journal.pone.0057139
17
DengM. D.ColemanJ. R. (1999). Ethanol synthesis by genetic engineering in cyanobacteria. Appl. Environ. Microbiol.65, 523–528.
18
DittrichJ. (2013). Cyclic Electron Flow: Powering Unique Motility and Alternative Nitrogen Uptake in Synechococcus WH8102 During Nitrogen Limited Growth. Corvallis, OR: Baccalaureate of Science Honors Bachelor of Science, Oregon State University.
19
DucatD. C.Avelar-RivasJ. A.WayJ. C.SilverP. A. (2012). Rerouting carbon flux to enhance photosynthetic productivity. Appl. Environ. Microbiol.78, 2660–2668.10.1128/AEM.07901-11
20
EllisR. J. (2001). Macromolecular crowding: obvious but underappreciated. Trends Biochem. Sci.26, 597–604.10.1016/S0968-0004(01)01938-7
21
ErdmannN.FuldaS.HagemannM. (1992). Glucosylglycerol accumulation during salt acclimation of two unicellular cyanobacteria. J. Gen. Microbiol.138, 363–368.10.1099/00221287-138-2-363
22
FeistA. M.HerrgardM. J.ThieleI.ReedJ. L.PalssonB. O. (2009). Reconstruction of biochemical networks in microorganisms. Nat. Rev. Microbiol.7, 129–143.10.1038/nrmicro1949
23
FoleaI. M.ZhangP.NowaczykM. M.OgawaT.AroE. M.BoekemaE. J. (2008). Single particle analysis of thylakoid proteins from Thermosynechococcus elongatus and Synechocystis 6803: localization of the CupA subunit of NDH-1. FEBS Lett.582, 249–254.10.1016/j.febslet.2007.12.012
24
GründelM.ScheunemannR.LockauW.ZilligesY. (2012). Impaired glycogen synthesis causes metabolic overflow reactions and affects stress responses in the cyanobacterium Synechocystis sp. PCC 6803. Microbiology158, 3032–3043.10.1099/mic.0.062950-0
25
HagemannM. (2011). Molecular biology of cyanobacterial salt acclimation. FEMS Microbiol. Rev.35, 87–123.10.1111/j.1574-6976.2010.00234.x
26
KimH. W.VannelaR.ZhouC.RittmannB. E. (2011). Nutrient acquisition and limitation for the photoautotrophic growth of Synechocystis sp. PCC6803 as a renewable biomass source. Biotechnol. Bioeng.108, 277–285.10.1002/bit.22928
27
KirchhoffH.HallC.WoodM.HerbstováM.TsabariO.NevoR.et al (2011). Dynamic control of protein diffusion within the granal thylakoid lumen. Proc. Natl. Acad. Sci.U.S.A.108, 20248–20253.10.1073/pnas.1104141109
28
KlumppS.ScottM.PedersenS.HwaT. (2013). Molecular crowding limits translation and cell growth. Proc. Natl. Acad. Sci.U.S.A.110, 16754–16759.10.1073/pnas.1310377110
29
KnoopH.GrundelM.ZilligesY.LehmannR.HoffmannS.LockauW.et al (2013). Flux balance analysis of cyanobacterial metabolism: the metabolic network of Synechocystis sp. PCC 6803. PLoS Comput. Biol.9:e1003081.10.1371/journal.pcbi.1003081
30
KnoopH.ZilligesY.LockauW.SteuerR. (2010). The metabolic network of Synechocystis sp. PCC 6803: systemic properties of autotrophic growth. Plant Physiol.154, 410–422.10.1104/pp.110.157198
31
LabbeR. G.HuangT. H. (1995). Generation times and modeling of enterotoxin-positive and enterotoxin-negative strains of Clostridium perfringens in laboratory media and ground beef. J. Food Prot.58, 1303–1306.
32
LanE. I.LiaoJ. C. (2011). Metabolic engineering of cyanobacteria for 1-butanol production from carbon dioxide. Metab. Eng.13, 353–363.10.1016/j.ymben.2011.04.004
33
LindbergP.ParkS.MelisA. (2010). Engineering a platform for photosynthetic isoprene production in cyanobacteria, using synechocystis as the model organism. Metab. Eng.12, 70–79.10.1016/j.ymben.2009.10.001
34
LudwigM.BryantD. A. (2011). Transcription profiling of the model cyanobacterium Synechococcus sp. strain PCC 7002 by NextGen (SOLiD™) sequencing of cDNA. Front. Microbiol.2:41.10.3389/fmicb.2011.00041
35
MikaJ. T.Van Den BogaartG.VeenhoffL.KrasnikovV.PoolmanB. (2010). Molecular sieving properties of the cytoplasm of Escherichia coli and consequences of osmotic stress. Mol. Microbiol.77, 200–207.10.1111/j.1365-2958.2010.07201.x
36
MoalG.LagoutteB. (2012). Photo-induced electron transfer from photosystem I to NADP(+): characterization and tentative simulation of the in vivo environment. Biochim. Biophys. Acta1817, 1635–1645.10.1016/j.bbabio.2012.05.015
37
MolenaarD.Van BerloR.De RidderD.TeusinkB. (2009). Shifts in growth strategies reflect tradeoffs in cellular economics. Mol. Syst. Biol.5, 323.10.1038/msb.2009.82
38
MonodJ. (1949). The growth of baterial cultures. Annu. Rev. Microbiol.3, 371–394.10.1146/annurev.mi.03.100149.002103
39
NeidhardtF. C.IngrahamJ. L.SchaechterM. (1990). Physiology of the Bacterial Cell: A Molecular Approach. Sunderland: Sinauer Associates.
40
NishimuraT.TakahashiY.YamaguchiO.SuzukiH.MaedaS. I.OmataT. (2008). Mechanism of low CO2-induced activation of the cmp bicarbonate transporter operon by a LysR family protein in the cyanobacterium Synechococcus elongatus strain PCC 7942. Mol. Microbiol.68, 98–109.10.1111/j.1365-2958.2008.06137.x
41
NiyogiK. K.TruongT. B. (2013). Evolution of flexible non-photochemical quenching mechanisms that regulate light harvesting in oxygenic photosynthesis. Curr. Opin. Plant Biol.16, 307–314.10.1016/j.pbi.2013.03.011
42
NogalesJ.GudmundssonS.KnightE. M.PalssonB. O.ThieleI. (2012). Detailing the optimality of photosynthesis in cyanobacteria through systems biology analysis. Proc. Natl. Acad. Sci.U.S.A.109, 2678–2683.10.1073/pnas.1117907109
43
NogalesJ.GudmundssonS.ThieleI. (2013). Toward systems metabolic engineering in cyanobacteria: opportunities and bottlenecks. Bioengineered4, 158–163.10.4161/bioe.22792
44
NomuraC. T.PerssonS.ShenG.Inoue-SakamotoK.BryantD. A. (2006). Characterization of two cytochrome oxidase operons in the marine cyanobacterium Synechococcus sp. PCC 7002: inactivation of ctaDI affects the PS I:PS II ratio. Photosyn. Res.87, 215–228.10.1007/s11120-005-8533-y
45
O’BrienE. J.LermanJ. A.ChangR. L.HydukeD. R.PalssonB. O. (2013). Genome-scale models of metabolism and gene expression extend and refine growth phenotype prediction. Mol. Syst. Biol.9, 693.10.1038/msb.2013.52
46
ParryB. R.SurovtsevI. V.CabeenM. T.O’HernC. S.DufresneE. R.Jacobs-WagnerC. (2014). The bacterial cytoplasm has glass-like properties and is fluidized by metabolic activity. Cell156, 183–194.10.1016/j.cell.2013.11.028
47
RossO. N.GeiderR. J. (2009). New cell-based model of photosynthesis and photo-acclimation: accumulation and mobilisation of energy reserves in phytoplankton. Mar. Ecol. Prog. Ser.383, 53–71.10.3354/meps07961
48
SchaechterM.MaaloeO.KjeldgaardN. O. (1958). Dependency on medium and temperature of cell size and chemical composition during balanced grown of Salmonella typhimurium. J. Gen. Microbiol.19, 592–606.10.1099/00221287-19-3-592
49
SchluchterW. M.BryantD. A. (1992). Molecular characterization of ferredoxin NADP+ oxidoreductase in cyanobacteria: cloning and sequence of the petH gene of Synechococcus sp. PCC 7002 and studies on the gene product. Biochemistry31, 3092–3102.10.1021/bi00140a037
50
SchuurmansR. M.SchuurmansJ. M.BekkerM.KromkampJ. C.MatthijsH. C.HellingwerfK. J. (2014). The redox potential of the plastoquinone pool of the cyanobacterium Synechocystis species strain PCC 6803 is under strict homeostatic control. Plant Physiol.165, 463–475.10.1104/pp.114.237313
51
ScottM.GundersonC. W.MateescuE. M.ZhangZ.HwaT. (2010). Interdependence of cell growth and gene expression: origins and consequences. Science330, 1099–1102.10.1126/science.1192588
52
ScottM.HwaT. (2011). Bacterial growth laws and their applications. Curr. Opin. Biotechnol.22, 559–565.10.1016/j.copbio.2011.04.014
53
SohS.BanaszakM.Kandere-GrzybowskaK.GrzybowskiB. A. (2013). Why cells are microscopic: a transport-time perspective. J. Phys. Chem. Lett.4, 861–865.10.1021/jz3019379
54
SteuerR.KnoopH.MachnéR. (2012). Modelling cyanobacteria: from metabolism to integrative models of phototrophic growth. J. Exp. Bot.63, 2259–2274.10.1093/jxb/ers018
55
TadmorA. D.TlustyT. (2008). A coarse-gained biophysical model of E. coli and its application to perturbation of the rRNA operon copy number. PLoS Comput. Biol.4:e1000038.10.1371/journal.pcbi.1000038
56
TchernovD.SilvermanJ.LuzB.ReinholdL.KaplanA. (2003). Massive light-dependent cycling of inorganic carbon between oxygenic photosynthetic microorganisms and their surroundings. Photosyn. Res.77, 95–103.10.1023/A:1025869600935
57
UngererJ.TaoL.DavisM.GhirardiM.ManessP.-C.YuJ. (2012). Sustained photosynthetic conversion of CO2 to ethylene in recombinant cyanobacterium synechocystis 6803. Energy Environ. Sci.5, 8998–9006.10.1039/c2ee22555g
58
van DijkenJ.WeusthuisR.PronkJ. (1993). Kinetics of growth and sugar consumption in yeasts. Antonie Van Leeuwenhoek63, 343–352.10.1007/BF00871229
59
VazquezA.BegQ. K.DemenezesM. A.ErnstJ.Bar-JosephZ.BarabasiA. L.et al (2008). Impact of the solvent capacity constraint on E. coli metabolism. BMC Syst. Biol.2:7.10.1186/1752-0509-2-7
60
WordenA. Z.BinderB. J. (2003). Growth regulation rRNA content in Prochlorococcus and Synechococcus (marine cyanobacteria) measured by whole-cell hybridization of rRNA targeted peptide nucleic acids. J. Phycol.39, 527.10.1046/j.1529-8817.2003.01248.x
61
XueY.ZhangY.ChengD.DaddyS.HeQ. (2014). Genetically engineering Synechocystis sp. Pasteur culture collection 6803 for the sustainable production of the plant secondary metabolite p-coumaric acid. Proc. Natl. Acad. Sci.U.S.A.111, 9449–9454.10.1073/pnas.1323725111
62
YouC.OkanoH.HuiS.ZhangZ.KimM.GundersonC. W.et al (2013). Coordination of bacterial proteome with metabolism by cyclic AMP signalling. Nature500, 301–306.10.1038/nature12446
63
YoungJ. D. (2014). INCA: a computational platform for isotopically nonstationary metabolic flux analysis. Bioinformatics30, 1333–1335.10.1093/bioinformatics/btu015
64
YoungJ. D.ShastriA. A.StephanopoulosG.MorganJ. A. (2011). Mapping photoautotrophic metabolism with isotopically nonstationary 13C flux analysis. Metab. Eng.13, 656–665.10.1016/j.ymben.2011.08.002
65
ZimmermanS. B.TrachS. O. (1991). Estimation of macromolecule concentrations and excluded volume effects for the cytoplasm of Escherichia coli. J. Mol. Biol.222, 599–620.10.1016/0022-2836(91)90499-V
Summary
Keywords
cyanobacteria, growth rate, molecular crowding, optimization, photosynthesis, ribosomes
Citation
Burnap RL (2015) Systems and Photosystems: Cellular Limits of Autotrophic Productivity in Cyanobacteria. Front. Bioeng. Biotechnol. 3:1. doi: 10.3389/fbioe.2015.00001
Received
06 September 2014
Accepted
04 January 2015
Published
20 January 2015
Volume
3 - 2015
Edited by
Toivo Kallas, University of Wisconsin-Oshkosh, USA
Reviewed by
Niels-Ulrik Frigaard, University of Copenhagen, Denmark; Weiwen Zhang, Tianjin University, China
Copyright
© 2015 Burnap.
This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) or licensor are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.
*Correspondence: Robert L. Burnap, Department of Microbiology and Molecular Genetics, Oklahoma State University, 307 Life Sciences East, Stillwater, OK 74078, USA e-mail: rob.burnap@okstate.edu
This article was submitted to Synthetic Biology, a section of the journal Frontiers in Bioengineering and Biotechnology.
Disclaimer
All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article or claim that may be made by its manufacturer is not guaranteed or endorsed by the publisher.