- Research article
- Open Access
Difference in C3–C4 metabolism underlies tradeoff between growth rate and biomass yield in Methylobacterium extorquens AM1
© The Author(s). 2016
- Received: 19 August 2015
- Accepted: 12 July 2016
- Published: 19 July 2016
Two variants of Methylobacterium extorquens AM1 demonstrated a trade-off between growth rate and biomass yield. In addition, growth rate and biomass yield were also affected by supplementation of growth medium with different amounts of cobalt. The metabolism changes relating to these growth phenomena as well as the trade-off were investigated in this study. 13C metabolic flux analysis was used to generate a detailed central carbon metabolic flux map with both absolute and normalized flux values.
The major differences between the two variants occurred at the formate node as well as within C3–C4 inter-conversion pathways. Higher relative fluxes through formyltetrahydrofolate ligase, phosphoenolpyruvate carboxylase, and malic enzyme led to higher biomass yield, while higher relative fluxes through pyruvate kinase and pyruvate dehydrogenase led to higher growth rate. These results were then tested by phenotypic studies on three mutants (null pyk, null pck mutant and null dme mutant) in both variants, which agreed with the model prediction.
In this study, 13C metabolic flux analysis for two strain variants of M. extorquens AM1 successfully identified metabolic pathways contributing to the trade-off between cell growth and biomass yield. Phenotypic analysis of mutants deficient in corresponding genes supported the conclusion that C3–C4 inter-conversion strategies were the major response to the trade-off.
- Methylobacterium extorquens AM1
- Physiological trade-off
- Metabolic flux analysis
Recent studies have shown that cobalt is an important trace metal for methylotrophic growth in M. extorquens AM1. Cobalt is needed for vitamin B12 production used as cofactor for two enzymes involved in methylotrophy growth, methylmalonyl-CoA mutase (Mcm) and ethylmalonyl-CoA mutase (Ecm) in the ethylmalonyl-CoA pathway, and plays a role in strain fitness [8, 9, 11]. Three research groups have published optimized media recipes, including optimization of cobalt levels [8–11]. However, the effect of cobalt on the overall central carbon metabolism in M. extorquens AM1 remains unknown.
Strain integrity can become compromised when the same strain is transferred between labs using different storage procedures, as illustrated recently for M. extorquens AM1 . Phenotypic divergence was observed between an archival strain and a modern strain in terms of growth rate and fitness across various culture conditions . The literature shows that two other strains have diverged in Mary Lidstrom’s lab and Julia Vorholt’s lab, after these strains were separated for 14 years. Different growth rates were reported from previous studies for both strains [13, 14], which could be ascribed to a combination of culturing environment and unintended domestication of the M. extorquens AM1 strain, but the basis for this difference is not known.
It has been well-documented that a trade-off exists between rate and yield for heterotrophic organisms in which growth rate is predicted to be limited by ATP [15, 16]. However, it was not known whether such a tradeoff occurs in the M. extorquens AM1 strain variants. In M. extorquens AM1, the cell growth is predicted to be limited by reducing power instead of ATP , making the metabolic basis for such tradeoffs unclear. The availability of two strain variants with differences in growth rate and possibly in biomass yield offers an opportunity to decipher system-wide metabolic responses in M. extorquens AM1, including the possible trade-off between growth rate and biomass yield.
13C metabolic flux analysis is a powerful tool, which combines both experimental and computational approaches to quantitatively understand the metabolic pathways in a living organism. It is based on a stoichiometric reaction model and extracellular consumption and secretion, along with 13C labeling information to calculate in vivo reaction rates [17–21]. It generates both flux maps with absolute values as well as flux distribution normalized to specific substrate uptake rate, offering insights into cell behavior at the metabolic activity level. This technique provides an approach to address the metabolic changes underlying the physiological differences observed in the two M. extorquens strain variants noted above.
In this study, it was established that a tradeoff exists between growth rate and biomass yield in these two M. extorquens AM1 strain variants, and 13C metabolic flux analysis (MFA) was applied to both strain variants in order to assess the metabolic differences underlying the trade-off. In addition, MFA was applied to the same strain with different cobalt supplements to assess the effect of cobalt on overall central carbon metabolism and its contribution to the trade-off.
Tradeoff between growth rate and biomass yield exists in M. Extorquens AM1 for two strain variants as well as two cobalt levels
Observations of growth rate differences prompted a more in-depth study of two M. extorquens AM1 strains, a parent strain from the laboratory of Mary Lidstrom (LL strain), and a strain that originated from the Lidstrom laboratory, but was carried in the laboratory of Julia Vorholt (VL strain) since 2001. Both genomes of the two variants were sequenced in this study. A small number of genomic differences were detected between three different M. extorquens strains (VL, LL and Chris Marx modern strain ) (see Additional file 1: Table S1). However, these differences did not provide an obvious solution to the trade-off or suggest how the divergence in genome sequence affects growth rate. Growth experiments were conducted for the two strains with methanol as the sole carbon substrate. A minimal medium from the Lidstrom laboratory (called hypho medium, HY) was used to be consistent with previous work done in the Lidstrom laboratory. In addition, since levels of cobalt in the medium also affect growth rate of M. extorquens AM1 strains [8, 9] but the effect on biomass yield is unknown, this factor was also studied. Three different levels of cobalt were tested for growth rate experiments (data not shown). For both strains, the most dramatic differences were between 1.35 and 6.31 μM. These two concentrations were then chosen to test the effect of cobalt supplementation.
In summary, within the four conditions tested in this study, LL in HY medium has the slowest growth rate but highest biomass yield while VL in HYC medium has the fastest growth rate but lowest biomass yield. Since both strain difference and cobalt level were taken into account in this set of comparisons, analysis of the metabolic response to the trade-off includes both factors.
Flux distribution reveals different metabolic strategies in C3–C4 interconversions and the formate branch node
Likewise, two routes exist for conversion of phosphoenolpyruvate (PEP) into acetyl-CoA (AcCoA). In the first route, the classic serine cycle involves conversion of PEP into oxaloacetate (OAA) through a carboxylation pathway involving PEP carboxylase (PEPCL), and then conversion of OAA into malate (MAL) by malate dehydrogenase (MDH), which is then further converted into glyoxylate and AcCoA by malyl-coA lyase (MCL). A reaction also exists to decarboxylate OAA back to PEP by phosphoenolpyruvate carboxykinase (PEPCK). An alternative route utilizes PEP to synthesize pyruvate through pyruvate kinase (PK), and then pyruvate is decarboxylated by pyruvate dehydrogenase (PYRDH) to produce AcCoA. Pyruvate could also be produced from decarboxylation of malate through malic enzyme (ME). The flux distribution shows that PEPCL had a higher normalized flux in the LL strain than the VL strain by 91 % in HY and by 55 % in HYC. For each strain grown at different cobalt concentrations, the normalized PEPCL flux decreased by 53 % at the higher cobalt concentration in HYC for the LL strain and 42 % for the VL strain. PEPCK is active for the LL strain in HY, but is negligible for the LL strain in HYC. For the VL strain, PEPCK is negligible regardless of the level of cobalt. For the malic enzyme pathway (ME), the LL strain has 97 % higher flux than the VL strain in HY, but the difference became smaller in HYC, with the higher cobalt concentration. PK in the LL strain is 49 % lower than VL in HY with the lower cobalt level, 25 % in HYC. A similar trend was observed for PYRDH for both conditions but to different extents, 67 and 61 % respectively.
Phenotypic differences of mutants
Based on the flux analysis results, three genes were targeted for mutation (dme encoding ME, pck encoding PEPCK and pyk encoding PK), to assess mutant phenotypes in the two strains. It is known that PEPCL, MCL, and MDH are required for growth on methanol  so those mutants were not generated.
Growth rate and biomass yield for dme, pck, and pyk mutants of both strain variants, base cases included, marked asa
Strain + medium condition
Biomass yield (g cdw/mol methanol consumed)
Absolute change in biomass yield
(g cdw/mol methanol consumed)
Percent of original strain biomass yield under same condition
Growth rate (per hr)
Absolute change in growth rate(per hr)
Percent of original strain growth under same condition
LL + HY
8.90 ± 0.59
0.09 ± 0.01
VL + HY
6.44 ± 0.90
0.13 ± 0.01
LL + HYC
6.09 ± 0.04
0.13 ± 0.01
VL + HYC
4.38 ± 0.31
0.15 ± 0.01
LL: Dpck + HY
4.84 ± 0.98
54 % ± 11 %
0.10 ± 0.01
111 % ± 12 %
VL: Dpck + HY
5.26 ± 0.52
82 % ± 8 %
0.10 ± 0.01
77 % ± 8 %
LL: Dpck + HYC
4.76 ± 1.67
78 % ± 27 %
0.09 ± 0.01
75 % ± 10 %
VL: Dpck + HYC
5.06 ± 0.49
115 % ± 11 %
0.09 ± 0.01
60 % ± 8 %
LL: Ddme + HY
4.07 ± 2.06
46 % ± 23 %
0.09 ± 0.01
100 % ± 10 %
VL: Ddme + HY
4.62 ± 1.02
72 % ± 16 %
0.09 ± 0.01
69 % ± 8 %
LL: Ddme + HYC
5.92 ± 0.37
97 % ± 6 %
0.07 ± 0.01
58 % ± 10 %
VL: Ddme + HYC
6.01 ± 0.76
137 % ± 17 %
0.10 ± 0.01
67 % ± 7 %
LL: Dpyk + HY
7.77 ± 0.45
87 % ± 6 %
0.10 ± 0.01
108 % ± 6 %
VL: Dpyk + HY
6.30 ± 0.17
98 % ± 4 %
0.06 ± 0.01
44.9 % ± 6 %
LL: Dpyk + HYC
7.60 ± 0.56
125 % ± 8 %
0.11 ± 0.01
86 % ± 10 %
VL: Dpyk + HYC
6.63 ± 1.14
151 % ± 17 %
0.10 ± 0.01
63 % ± 10 %
Strains and plasmid
Apr, Knr,Tcr; pCM182 with kan from pCM183; allelic exchange vector
Secondly, metabolic flux map results also indicate that the non-essential pathways associated with biomass yield were ME encoded by dme and PEPCK encoded by pck. The higher biomass yield conditions have higher carbon flux through both ME and PEPCK. This predicts that both of these mutants should have a more negative impact on conditions with higher biomass yield. The experimental results on biomass yield for these two mutants agree with the prediction shown in Table 1. As shown in Table 1, the dme mutation had a negative effect on biomass yield in the LL strain in HY medium (54 % decrease) compared to wild type LL. A smaller decrease in biomass yield (28 %) occurred in VL: Δdme. Likewise, the pck mutation also had a negative impact on biomass yield in the LL strain (46 % decrease compared to wild type LL), while for VL: Δpck in HY, it decreased by only 18 %. The effect on biomass yield for both strains was less when the cells were grown with the higher level of cobalt. For both VL: Δdme and VL: Δpck, the biomass yield increased. Noticeably, the dme mutant in VL and LL strain had the same biomass yield in HYC when extra cobalt was supplied to the medium, while the difference was more pronounced in HY medium. The Δpck and Δdme strains did not have large impacts on growth rate, but showed different extents of growth defects (Table 1). These two pathways involve NADH and ATP consumption, respectively. Therefore these two mutants are expected to alter consumption of ATP and NADH, which might be expected to affect growth rate.
This work generated four detailed flux distribution maps for two strain variants of M. extorquens AM1 (the LL and VL strains) grown with different cobalt levels. 13C MFA has previously been applied to the VL strain during growth on methanol at a higher cobalt level . However, it is not possible to compare the flux maps directly, as in the previous study the culture was grown with 5 % CO2 purging the culture system. The influence of 5 % CO2 on metabolism in M. extorquens AM1 is unknown, but given the number of carboxylation and decarboxylation reactions involved in growth on one-carbon compounds, it might alter fluxes. In this study we used air (0.5 % CO2) and also a slightly different medium recipe, to allow direct comparisons with previous metabolic studies of this bacterium carried out in this medium with 0.5 % CO2.
We have shown that the VL strain grew faster with lower biomass yield than the LL strain, regardless of the cobalt supplementation. From these results we conclude that a tradeoff exists between growth rate and biomass yield that is strain-specific. This suggests that these two strains are an example of unintended domestication, which has been reported previously for M. extorquens AM1 . In addition, the cobalt level also affects growth rate and biomass yield in a manner that is not strain-specific. Improved growth rate and increased absolute fluxes through the EMC cycle in response to higher cobalt are in keeping with previous studies [8, 11] suggesting that the EMC pathway could be a potential bottleneck for methanol assimilation under cobalt limitation conditions.
The occurrence of natural strain variants with growth rate/biomass yield tradeoffs along with the cobalt affect provided the opportunity to determine features of metabolic network response underlying these major physiological attributes of growth rate and biomass yield. 13C-flux labeling revealed that FTHFL, the pathway involving the standard serine cycle (PEPCL, MDH, and MCL), and PEPCK and ME all had higher relative flux in conditions when biomass yield was higher, while the alternate pathway to AcCoA involving PK and PYRDH had higher relative flux in conditions when growth rate was faster. These differences were predicted to affect NADH and ATP usage. PEPCK consumes one ATP, while PK and PYRDH produce one ATP and one NADH, respectively. MDH and MCL consume NADH and ATP, respectively. These results suggest that higher biomass yield is achieved under conditions that result in relatively higher relative fluxes through the standard serine cycle-based carbon assimilation pathways, even though this metabolic scheme consumes more NADH and ATP than the one involving conversion of pyruvate to AcCoA, at the expense of growth rate. Likewise, higher growth rate is achieved by diverting carbon through pathways with higher NADH and ATP production, with concomitant decrease in biomass yield.
There must be a genetic explanation for the trade-off. However, genome sequence results did not provide a clear clue, since none of the genomic changes is predicted to directly impact any of the C3/C4 reactions that show altered flux. One of the possible explanations is that the mutants in the gene cluster with unknown functions lead to shifted flux through C3/C4 enzymes due to the change in small molecule pools, which in turn affects yield versus growth rate.
The results of mutant phenotypes are consistent with these conclusions regarding metabolic network response, since loss of the biomass yield-related enzymes resulted in an impact on biomass yield, and loss of a growth-rate related enzyme resulted in an impact on growth rate. It is more difficult to predict the impact of the pyk mutant on yield, and of the dme and pck mutants on growth rate. C3-C4 interconversion pathways in this bacterium are flexible due to the fact that some of the enzymes are reversible (such as MDH, ME) as well as the fact that different enzymes are present that catalyze forward and reverse reactions (such as PK, PEP synthase, PEPCL and PEPCK). In the two strain variants, two C3/C4 pathways dominate but with different ratios, as shown in Fig. 3, but we do not know how the network will change in the mutants. Therefore, although we can predict that removing the optimal variant would decrease growth rate or yield, respectively, the mutation may or may not also affect the other parameter, depending on how the metabolic network rearranges.
The cobalt concentration used in the growth medium also affected the fluxes and mutant phenotypes. In both strains, growth in higher cobalt resulted in higher growth rates and a correspondingly higher absolute flux through the assimilatory pathways. Since the EMC pathway contains two steps requiring B12-utilizing mutases (ethylmalonyl-CoA mutase and methylmalonyl-CoA mutase), it is expected that higher availability of cobalt would affect flux through the EMC shown by others [8, 11]. The increased absolute flux through the EMC suggests that a cobalt-related component of one or both of these enzymes might limit flux under the lower cobalt growth condition. However, although the absolute flux increased through all of the central assimilatory pathways with increased cobalt, the flux distribution (normalized to the methanol uptake rate) did not. The flux distribution through the EMC was essentially the same for both the high and low cobalt conditions. This result suggests that the assimilatory flux is well balanced with both the methanol uptake rate and the formate branchpoint distribution, and that the metabolic network has the capacity to increase flux to this level. The significant changes in the flux distribution that occur in response to cobalt are not in the EMC pathway, but instead, are in the nexus between the serine cycle, the partial TCA cycle, the pentose-phosphate pathway, and the EMC pathway. It seems likely that this redundancy in C3–C4 interconversions at this metabolic intersection provides robustness for the metabolic network. The mechanism(s) for these changes are not yet known, but could occur at the transcriptional or post-transcriptional level.
The flux distribution maps presented here provide information that is potentially useful in guiding strain development for biotechnical applications. For applications in which faster strain growth is favored to create optimal economic conditions for a product (for instance, when a biomass product is the target), reactions identified in this study associated with faster growth are targets for manipulation. Similarly, if instead higher biomass yield is favored, for instance with an excreted product, the reactions associated with higher biomass yield could be manipulation targets. It should also be noted that as shown in this study, a single trace mineral change in the medium changes the flux distribution, pointing out the importance of flux analysis in assessing metabolic dynamics and growth conditions.
Growth rate and biomass yield measurements for two culture conditions with two strain variants suggest trade-offs exist between growth rate and biomass yield. 13C flux analysis was successfully applied to identify metabolic differences that could contribute to the trade-off. Pathways with different activities were identified, which were used to generate a hypothesis of the metabolic changes responding to the trade-off, focused on C3–C4 inter-conversion strategies. The hypothesis was tested using mutants, and their phenotypes supported the conclusion that the flux difference mainly involves C3–C4 interconversion strategies.
Chemicals and medium composition
13C methanol of 99 % purity was purchased from Cambridge Isotope Laboratories (Tewksbury, MA). All other chemicals including metabolite standards were purchased from Sigma-Aldrich (St. Louis, MO). Phusion DNA polymerase, dNTP, buffer, ligases, OneTaq Quick-Load 2X Master Mix and the Gibson Assembly Master Mix kits used in this study were from New England Biolabs (Ipswich, MA). Primers, the sequences of which are shown in Table 1, were obtained from Invitrogen (Grand Island, NY) and IDT (Coralville, IA). Acetonitrile and water used as UPLC solvents were UPLC-MS grade. Hypho minimal medium as previously described  was used for 13C flux analysis cell culture and growth rate determination, involving two different concentrations of cobalt (1.35 and 6.31 μM respectively).
Bacterial strains, plasmid and growth condition
Gene sequences for primers used for PCR amplification in this study
dme upstream flank forward
dme upstream flank backward
dme downstream flank forward
dme downstream flank backward
pck upstream flank forward
pck upstream flank backward
pck downstream flank forward
pck downstream flank backward
pCM184 cre-km forward
pCM184 km-cre backward
pCM184 backbone forward
pCM184 Backbone backward
Methanol measurements in supernatant
Methanol consumption rates were determined by taking time course samples for supernatant methanol measurements. At least 2 points were taken during exponential phase growth. 750 ul of the supernatant sample were centrifuge filtered through 0.22 μm centrifuge filters (Costar® Spin-X® centrifuge tube filters, cellulose acetate membrane, pore size 0.22 μm, non-sterile, Sigma-Aldrich, (St. Louis, MO) for 2 min at 14,000 rpm. GC-FID (Aglient, Santa Clara, CA) was used for methanol detection with a 6890 Gas Chromatograph equipped with flame ionization detector (FID). Data were collected and converted into matlab input files with LabVIEW 2010. Data analysis was later done in Matlab. SLB-IL60 column (Supelco, Bellefonte, PA, USA) with a 30 m × 0.25 mm inner diameter (i.d.) × 0.2 μm thickness was installed for gas chromatograms. 1 μl of supernatant was injected and separated in the column and then entering into FID detector with a split ratio 50:1. Oven temperatures were programmed as follows. An initial temperature of 120 °C was held for 1 min, and then ramped at 35 °C /min until a final temperature of 200 °C was achieved. The FID was operated at 220 °C. All measurements were done in triplicate. With each run, a new calibration curve was then generated using the same instrument setting.
Metabolite extraction and biomass hydrolysis for isotopomer distribution measurements
Both proteinogenic amino acids and intracellular metabolites were used for isotopomer measurements in order to obtain good coverage of central carbon metabolism under methylotrophic growth. 20 ml of cell culture were collected and quenched using fast filtration using 0.2 μm nylon membrane filters (0.2 μm, 47 mm from PALL life science, Port Washington, NY) and liquid nitrogen. Cell pellets on 0.22 μm filters were lyophilized using FreeZone 4.5 l benchtop freezedry system (Labconco, Kansas) for 8–12 h to remove medium residue. The filter was incubated in 20 ml of boiling water for 10 min, and then placed on ice for at least 20 min for protein precipitation. The whole broth was then centrifuged at 4 °C, 5000 rpm for 10 min. The clear supernatant was transferred into a clean 50 ml falcon tube, and then frozen using liquid nitrogen. The remaining tubes containing protein and cell debris were centrifuged again, at 4 °C, 5000 rpm for 20 min, and supernatants were removed carefully. Frozen samples were then lyophilized twice, and reconstituted in 100 μl nanopure water. The 100 μl of sample was distributed into 2 vials. One 50 μl sample was used for LC/MS/MS measurements, and the other was dried using a Speedvac (Labconco, Kansas), and derivatized with TBDMS and methoxyamine hydrochloride O-Methylhydroxylamin-hydrochlorid (Sigma-Aldrich, St. Louis, MO) using a previously described method . Cell pellets were then hydrolyzed using 1 ml of 6 N HCl at 105 °C for 22–24 h. The remaining HCl was later evaporated with nitrogen flow. Dried samples were reconstituted in 500 μl nanopure water, and ash and cell debris were then filtered out of the sample using centrifuge tube filter (spin-x costar, 0.22 μm, Sigma-Aldrich). 50 μl of the reconstituted sample was then dried and derivatized using TBDMS as noted above.
Both TBDMS-derivatized proteinogenic amino acids and intracellular metabolites were detected using an Agilent (Santa Clara, CA) GCMS with an Agilent J&W HP-5 ms Ultra Inert GC Column (30 m × 0.25 mm × 0.25 μm, catalog number: 19091 s-433). Each sample was run in duplicate on the GCMS with the same temperature program, and also as one more run with a slower oven temperature ramping rate. The oven temperature was programmed as follows: for regular runs, the oven temperature was programmed as follows:, initial temperature at 100 °C, hold for 4 min, then ramp to 300 °C with ramp rate at 5 °C/min, then hold for 5 min, with total run time 49 min. In order to further separate compounds with similar retention times a slower run was developed. For the slower run, the ramp rate slows down to 2.5 °C/min with total run 89 min. MS source temperature was set at 230 °C and MS quad temperature set as150 °C.
Sugar phosphate was separated by a Zic-pHilic column (SeQuant, PEEK 150 mm length × 2.1 mm metal free, with 5 μm polymeric film thickness) using LC-MS/MS (Xevo, Waters, Milford, MA). Mobile phase A is LC grade water with 2 mM formic acid and 4 mM ammonium, mobile phase B is acetonitrile with 0.1 % formic acid. Column temperature was set at 30 °C. The LC condition starts with 0.15 ml/min flow rate with initial gradient A = 15 %, hold for 2 min, then increased to 40 % over the next 2 min. At 7 min, A = 50 %, at 10 min, A = 80 %, at 11 min, A is set to 90 %, held for 0.5 min, and then switched to 15 % at 11.50 min to re-equilibrate the column for another 4.5 min.
Waters Xevo G2-S Q-Tof equipped with Waters Acquity UPLC I class (Milford, MA) was used for some of the proteinogenic amino acids using HILIC-BEH-amide (Waters Acquity, part number 186004802, with dimension 2.1 mm × 150 mm, 1.7um). Mobile phase A is water with 20 mM ammonium formate and 0.1 % formic acid, mobile phase B is acetonitrile with 0.1 % formic acid. LC solvent gradient was set as follow, starting at 10 % A for 1 min, at 2 min, A = 35 %, at 3 min, A = 40 %, at 6 min, A = 50 %, at 7.5 min, A = 80 %, holding for another 2 min. Then the column is re-equilibrated at 9.51 min by running 10 % A through the column until 5.5 min.
Central carbon metabolism model construction and 13C flux analysis
The central carbon metabolism pathway model used for 13C flux analysis is shown in Fig. 1. It was constructed based on a previous model , and details are shown in Additional files 2, 3, 4 and 5: Table S2, S3, S4 and S5. The pathways included are: oxidation of methanol to CO2 via formaldehyde and formate, conversion of formate to methylene-H4F using the H4F pathway; assimilation of methylene H4F via the serine cycle; the TCA cycle; the ethylmalonyl-CoA pathway; gluconeogenesis; and anaplerotic reactions [reactions catalyzed by pyruvate kinase, PEP carboxylase and malic enzyme] overlapping with the serine cycle in key intermediate metabolites nodes (such as 2-O-Phosphono-D-glyceric acid (2PGA) and phosphoenolpyruvate (PEP). Some of the C3 and C4 metabolites were involved in more than one pathway in this interconnected set of cycles. For instance, 1) 2PGA is the branch node for the serine cycle and gluconeogenesis, 2) PEP and pyruvate are both in the serine cycle and anaplerotic pathways, 3) Malate and OAA were both in the serine cycle, TCA cycle and anaplerotic pathway. This complexity and redundancy offers the cell alternatives for the connections between the serine cycle and EMC pathway under environmental perturbation and gene manipulation.
Methanol uptake rates and biomass yields were measured for individual conditions. Extracellular metabolite secretion was measured using 1H NMR with a previously described protocol . For in silico simulation, Influx_s was used .
AM1, Methylobacterium extorquens AM1; HY, hypho medium with 1.35 μM cobalt; HYC, Hypho medium with 6.31 μM
The author would also like to thank Martin Sadilek, Laura T. Carlson and Brian Fitz for help with instrumentation, Ludmila Chistoserdova for construction of pyk mutant, Serguei Sokol for help and useful discussions regarding the influx_s software, and Chris Marx for helpful discussion regarding the genome sequences.
This work was funded by a grant from the Department of Energy DOE-SC0006871.
Availability of data and materials
All data generated or analyzed during this study are included in this published article [and its supplementary information files].
Experiment design, implementation: YF. Genomic sequence analysis: DB. Overall concept design and oversight: ML. Manuscript writing and editing: YF, DB, and ML. All authors read and approved the final version of the manuscript.
The authors declare that they have no competing interests.
Consent to publish
Ethical approval and consent to participate
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