Results
when metabolite values were esUmated using four other E. coli GEMs (Fig. S11).
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Figure 1: Correla'on between microbial metabolite release rates and metabolite values. A) Hypothesis: if metabolite release
generally cons:tutes a fitness cost that microbes have evolved to reduce, metabolite release rates should be nega:vely
correlated with metabolite values. Three metabolites are used to conceptually illustrate their rela:ve posi:on based on their
es:mated release rate and metabolite value, see panels B and C. B) Metabolite release rates were es:mated from :me-series
exometabolomics data from batch cultures by linear regression of extracellular concentra:ons vs area under the curve (AUC) of
biomass. This panel shows extracellular concentra:ons of 37 metabolites measured during exponen:al phase of E. coli cul:vated
in glucose medium by Paczia et al. (2012), and the linear regressions used to es:mate net release rates. Linear regressions with
an R2 0.05 (two-sided Wald test) are drawn in red. Full :me-series, including sta:onary phase and linear regression
for E. coli, B. sub:lis, C. glutamicum and S. cerevisiae are shown in Figs. S1-S4. Metabolite abbrevia:ons: α-KG: alpha-
ketoglutarate, DHAP: dihydroxyacetone phosphate, FBP: fructose 1,6-bisphosphate, F6P: fructose 6-phosphate, G6P: glucose 6-
phosphate, 2/3PG: 2/3-phosphoglycerate, GA3P: glyceraldehyde 3-phosphate, R5P: ribose 5-phosphate, PEP:
phosphoenolpyruvate, RU5P/X5P: ribulose 5-phosphate/xylulose 5-phosphate, E4P: erythrose-4-phosphate. C) We used enzyme-
constrained genome-scale metabolic models to es:mate metabolite values, quan:fied as the nega:ve change in growth rate
(Δy) on metabolite release (Δx) close to op:mal growth. D-F) Three different datasets were used to test our hypothesis: D) Paczia
et al. (2012), including S. cerevisiae, B. licheniformis, C. glutamicum and E. coli on glucose (12), E) E. coli on three other carbon
sources (this work), and F) Vila et al. (2023) covering a smaller number of metabolites on E. coli, P . pu:da and two environmental
strains of the genera Enterobacter and Pseudomonas on up to 8 different carbon sources (43). The scaeer plots show mean
es:mated rates +- standard errors vs es:mated metabolite values. Black-filled circles are datapoints where the lower error bar is
omieed because mean minus standard error is less than 0 and cannot be included on a log-scale. Axis labels and colour legend
are shared for panel D-F. Annota:ons in panel F show the Pearson correla:on and associated P value in parentheses.
Metabolite value is the most important factor explaining variability in metabolite release
rates
The consistent negaUve correlaUon between metabolite release rates and metabolite values
encouraged us to ask how well this factor explains release variability compared to other
metabolic or physiochemical properUes previously associated to metabolite release (33, 45). We
focused on the data from bioreactor batch cultures of E. coli with glucose, galactose, L-malate
or L-alanine as the carbon source, where condiUons were well-defined, the measured
metabolites were diverse and reference values for intracellular metabolite concentraUons were
available (46–49). We first built univariate linear models to quanUfy the importance of these
factors: metabolite value, intracellular concentraUon, compound class, solubility in oil vs water
(log P), molecular weight, topological polar surface area, charge, hydrogen bond acceptor and
donor count, rotatable bond count, turnover and carbon source (Fig. 2A). Metabolite value
explained 43% of the variability, more than any other factor (Fig. 2B). The structure-based
classificaUon of compound class also had good predicUve power (29% explained), primarily
because carboxylic and keto/hydroxy acids were released at significantly higher rates than
amino acids and other compounds (Fig. 2A). However, these two factors are clearly confounded
as class-level differences mirrored significant differences in metabolite values (Fig. 2C). The
number of rotatable bonds, solubility in oil vs water (log P) and the number of hydrogen bonds,
each related to membrane permeability (50, 51), were also predicUve of metabolite release,
suggesUng passive diffusion as a relevant mechanism. Metabolite turnover is predicted to
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correlate negaUvely with release rates, according to the noise-averaging cooperaUon hypothesis
(low turnover metabolites are more suscepUble to noise and therefore more useful to share
within the populaUon) (33), but our dataset shows likle support for this.
When we asked how well the best linear model could predict metabolite release rates, we
found that 63% of the variability could be explained by metabolite value, compound class,
intracellular concentraUon and charge (Fig. 2B). However, predicUve accuracy declined when
applied to out-of-sample condiUons (45%, P = 0.04, 52.9 ± 3.8% expected from random model,
Fig. S12) or out-of-sample metabolites (50%, P < 0.001, 55.2 ± 0.7% expected from random
model, Fig. S13), likely due to correlaUons among the factors, which warrants cauUon when
interpreUng factors’ relaUve importance (Fig. S14). Nevertheless, excluding metabolite value as
a factor reduced model performance on out-of-sample condiUons (10% decline in median R2, P
= 0.003, one-sided Mann-Whitney U, N = 20, Fig. S15), and model quality was largely dependent
on including metabolite value or compound class (Fig. S16). Furthermore, we found differences
in metabolite value between condiUons to be negaUvely correlated with differences in release
rate (Pearson ρ, P = 2e-3, Fig. S17). This not only supports the relevance of this factor in
predicUng out-of-sample rates but also raises the quesUon of whether microbes adapt their
release rates to context-dependent costs. Finally, when we esUmated each factor’s importance
separately for each microbe in each dataset (except C. glutamicum), metabolite value sUll
emerged as the most robust explanatory factor (Fig. 2D).
Cell lysis is commonly considered a key mechanism for metabolite release (31, 32). To measure
its importance in our experiments, we used E. coli batch cultures with paired sampling of intra-
and extracellular metabolites, as well as flow cytometry with live/dead staining to quanUfy the
fracUon of lysed cells. In general, less than 10% of extracellular concentraUons could be
explained by the release of intracellular metabolites following cell lysis, and osen much less
(Fig. 3A). We then extended this analysis by comparing our collecUon of E. coli extracellular
metabolite concentraUons to published intracellular concentraUons (46–49). To avoid asserUng
equal lysis rates across condiUons, we asked how large a fracUon of the cell populaUon would
need to be lysed to account for the extracellular levels, considering only the contribuUon from
intracellular metabolite pools (Fig. 3B). Only 10.4% (157/1508) of the data points fall within the
range of measured lysis fracUon (0.2-2.3%, mean ± std across condiUons = 0.6 ± 0.6%) or below,
and more than 56.3% (849/1508) are above the limit where more than the whole cell
populaUon is required. Glutamate, glutamine and NAD are the only metabolites where most
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data points can be accounted for by cell lysis, due to high intracellular concentraUons and
moderate to low extracellular levels (Fig. S18).
DegradaUon of cell debris may also contribute to extracellular metabolite pools (52). In E. coli,
this degradaUon is dependent on the presence of Lon protease in the cell lysate (53). However,
the benefit of cell debris degradaUon by Lon was only significant well beyond exponenUal
phase, and only 19 ± 6% of oligopepUdes (6-10 amino acids) in the lysate were catabolised by
Lon over 20 hours (53). Thus, in our dataset where 90% of the samples were collected before 26
hours (67% in exponenUal phase), we expect only a fracUon of the proteome from lysed cells to
contribute to the extracellular concentraUons of amino acids. When we included 10% proteome
degradaUon in our analysis, only the extracellular levels of tryptophan and threonine
addiUonally became fully explained by cell lysis (Fig. S19). However, apart from amino acids, the
metabolites in Fig. 3B are not typical degradaUon products. Overall, these results suggest that
cell lysis and proteome degradaUon are insufficient to explain extracellular levels of most
metabolites – consistent with previous work (12, 31).
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Figure 2: The importance of different factors in explaining metabolite release rates. A) Among the tested chemical and
metabolic factors, log-scaled metabolite value explains the most variability in log-scaled E. coli release rates. The tested factors
are shown in order of how much variability (R2) in log-scaled metabolite value they explain as a univariate linear model, shown
in panel B. Compound class abbrevia:ons: CA: Carboxylic acids, AA: Amino acids, KA: Keto/hydroxy acids, OC: Organooxygen
compounds, O: Other. Sta:s:cal test for compound classes and carbon source: Kruskal-Wallis H-test followed by Conover’s test
with BH correc:on. For the other factors the reported P values are from Pearson correla:ons. B) The best linear model, ranked
by BIC score, is a four-factor model that explains 63.4% of the variability in log-scaled release rates. C) Differences in metabolite
values between compound classes. Abbrevia:ons and sta:s:cal test as in Fig. 2A. D) Log-scaled metabolite value consistently
ranks among the most important factors when evaluated separately for each species in each dataset. Factor abbrevia:ons: RBC:
Rotatable Bond Count, HBDC: Hydrogen Bond Donor Count, TPSA: Topological Polar Surface Area, HBAC: Hydrogen Bond
Acceptor Count.
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Figure 3: Contribu'on from cell lysis and associated release of intracellular metabolites to extracellular concentra'ons. A)
Using paired intra- and extracellular metabolite samples from the exponen:al phase of E. coli batch cultures we quan:fy what
frac:on of extracellular metabolite concentra:ons can be explained by cell lysis. Point size reflects order-of-magnitude increase
in extracellular concentra:on from the 2-hour sample to the late-exponen:al phase sample (Fig. S30), and all values except
leucine in the L-malate condi:on were in the μΜ range. B) We expanded this analysis to all metabolite measurements in our E.
coli datasets by using literature values for intracellular concentra:ons (Methods). For each metabolite, we es:mated the frac:on
of cell popula:on that would need to be lysed for the intracellular concentra:ons released by cell lysis to explain the measured
extracellular concentra:ons. The green region covers the range of measured frac:ons of lysed cells from A), and the red region is
where more than the whole cell popula:on is required to explain extracellular concentra:ons. Abbrevia:ons: 2PG: 2-
phosphoglycerate, 3PG: 3-phosphoglycerate, α-KG: Alpha-ketoglutarate, DHAP: Dihydroxyacetone phosphate, E4P: Erythrose 4-
phosphate, FBP: Fructose 1,6-bisphosphate, F6P: Fructose 6-phosphate, G6P: Glucose 6-phosphate, PEP: Phosphoenolpyruvate,
R5P: Ribose 5-phosphate, RU5P: Ribulose 5-phosphate, XU5P: Xylulose 5-phosphate.
Metabolic disrup)on and evolu)on change metabolite release rates
Given the effect of gene deleUons on intracellular metabolite levels (54), we assumed that the
lack of negaUve correlaUon between metabolite value and release rate in C. glutamicum (Fig.
1D) could be a result of its engineered metabolism (42). To test the sensiUvity of metabolite
release pakerns to modificaUons in core metabolism, we measured the exometabolome of
eight E. coli knockout (KO) strains in late exponenUal phase in galactose medium (Fig. 4A). These
gene knockouts target different parts of core metabolism, were previously shown to affect
intracellular metabolite pools (54), and were predicted to change intracellular flux pakerns (Fig.
S20). In line with our expectaUons, 14-38% (16-42 of 111) of the extracellular metabolite
concentraUons differed significantly from the wild type across the KO strains (Welch’s t-test, FDR
< 0.05, Fig. 4B). In contrast, only 2.7% of metabolite concentraUons were different in the
negaUve control strain ΔlacA. Each KO strain displayed disUnct exometabolome pakerns (Fig.
4C), and we observed the most pronounced differences for metabolites in proximity of the
deleted reacUon (Figs. S21-S23), consistent with intracellular effects of enzyme-deleUons (54).
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The WT reference for these KO strains from the KEIO collecUon (55) - E. coli BW25113 - had
largely comparable rates as E. coli MG1655 used in the experiments presented in Fig. 1 (Fig.
S24).
Our central hypothesis for the negaUve correlaUon between metabolite value and release rate is
that bacteria face a trade-off: the cost of prevenUng metabolite release versus the energy lost
through that release. If this trade-off is under strong selecUon, then disrupUng the balance (e.g.
via a gene knockout) should trigger rapid evoluUonary compensaUon to restore it. To test this,
we evolved the ΔaceE and ΔsucB mutants – chosen for their severe growth defects and disUnct
exometabolome characterisUcs – for ~100 (replicates M2-M4) and ~200 generaUons (M5-M7) in
galactose medium, respecUvely (Fig. S25). The strains evolved in chemostats, where byproducts
are conUnuously removed to avoid accumulaUon and later uptake of metabolites. From each
chemostat endpoint, we isolated three strains and selected from each replicate the fastest
growing clone (Fig. 4, D and E). These clones showed 94-146% (ΔaceE) and 50-82% (ΔsucB)
growth rate increases relaUve to their ancestors (Fig. 4, F and G). To assess changes in
metabolite release, we measured extracellular concentraUons of 5 metabolites at the end of
exponenUal growth (Fig. 4, D and E). These metabolites were selected because their release was
strongly disturbed in the ancestors (Figs. S21-S23), and either near the deleted reacUon
(pyruvate and lactate for the ΔaceE; citrate, isocitrate and cis-aconitate for ΔsucB) where we
expected the strongest effects, or located elsewhere in the metabolic network and of different
chemical classes to probe more widespread effects. Lactate levels were significantly reduced in
2/3 ΔaceE isolates (Fig. 4F), which also exhibited the highest growth rates. The reducUons were,
however, not sufficient to reach WT concentraUons. In contrast, all three ΔaceE isolates showed
increased pyruvate release, contrary to expectaUons. These results were qualitaUvely invariant
to growth rate normalizaUon (Fig. S26). For the ΔsucB isolates, we found in general small
reducUons in extracellular concentraUons (Fig. 4G), but some of these differences change
qualitaUvely upon growth rate normalizaUon (Fig. S27). For the metabolites elsewhere in the
metabolic network, the outcomes were variable (Figs. S28 and S29).
To esUmate the fitness contribuUon of reducing metabolite release, we used ecGEMs to predict
relaUve growth rate penalUes associated with the observed release rates, using the ancestors’
mean growth rates as references. In the ΔaceE ancestor, lactate release is predicted to reduce
fitness by 23% whereas pyruvate release has negligible impact (0.02%). The reduced release of
lactate in the isolates from chemostat M2 and M4 is predicted to reduce the negaUve fitness
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effect to only 16% and 7%, respecUvely. These contribuUons are small compared to the
observed increase (94-146%). The pakern is similar for the ΔsucB isolates: the esUmated net
fitness reducUon of citrate, isocitrate and cis-aconitate in the ancestor is only 0.37%, far from
sufficient to explain the improved growth rates.
To beker understand the reasons for increased growth and changed release rates, we idenUfied
sequence variants in the selected fast-growing strains and mutaUons that had fixed in the
chemostat populaUons (Table S1-S4). Aside from the ΔaceE-M4 isolate, which likely
hypermutated due to a mutT mutaUon, the evolved ΔaceE isolates have few sequence variants,
and either related to galactose uptake (e.g. galS in M2, M4 and M7, regulaUng galactose uptake)
or modulaUng fluxes near the deleted reacUon (e.g. poxB in M2, ldhA in M4, and icd, aceK and
sdhA in M5, M6 & M7 and M7, respecUvely). Fixed non-synonymous variants in the chemostat
populaUons support these observaUons, e.g. ldhA and galS were fixed in M2 and ilvG was fixed
in M4. The ΔsucB populaUons have many more fixed mutaUons, but among the ones shared
across replicates we find again galS and aceK. Together, these results show that metabolite
release rates change as microbes evolve, but in our experiments, these changes were likely
secondary to other, more dominant drivers of fitness – leading to inconsistent changes in
metabolite release across replicates.
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Figure 4: Effect of gene knockouts on metabolite release rates and the effect of subsequent evolu'on to higher fitness. A)
Growth curves of selected KO mutants, with sampling :me-points indicated by open circles. B) Comparison of extracellular
metabolite concentra:ons in late exponen:al (OD600~1.2-1.3) between KO mutants and WT. Significant differences are marked
by solid black outlines (Welch’s t-test, FDR < 0.05). C) A PCA plot of exometabolome profiles, showing that each strain has a
dis:nct paeern. D & E) Batch culture growth curves and sampling :mepoints for isolates from the endpoint of the evolu:on
experiment for ΔaceE and ΔsucB, respec:vely. F & G) Growth rates and extracellular metabolite concentra:ons for metabolites
near the deleted reac:on, for ΔaceE and ΔsucB, respec:vely. Sta:s:cal significance was assessed using Welch’s t-test.
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Materials and methods
Strains
All experiments were conducted with either E. coli K-12 MG1655, E. coli K12 BW25113 (wild-type
ancestor for KEIO KO strains) or the following KO mutants from the KEIO collecUon (55): ΔaceE
(JW0110), ΔcyoD (JW0419), ΔlacA (JW0333), ΔnuoA (JW2283), Δpgi (JW3985), Δrpe (JW3349),
ΔsucB (JW0716), Δzwf (JW1841). The KEIO KO strains were verified by PCR with one primer
binding inside the KanR casseke inserted during gene knock-out (Keio_K1_Rev for genes on the (-
) strand; Keio_KT_RvComp_Fw for genes on the (+) strand) and one gene-specific primer binding
downstream of the knocked-out gene (primers are listed in Table S5) (55, 65). For all experiments,
the KEIO KO strains were used with the kanamycin resistance casseke in place.
Precultures and growth media
For all experiments detailed below the strains were precultured as described here unless
otherwise stated: From glycerol stocks stored at -70 °C each strain was streaked out onto LB
agar plates and incubated overnight (37 °C). Then, one colony of each strain was picked and
used to inoculate liquid precultures (10 mL LB in 50 mL Erlenmeyer flasks) that were incubated
overnight (37 °C, 200 rpm). The kanamycin-resistant KEIO KO strains and strains evolved from
these were always precultured in liquid LB and streaked out onto LB agar plates with 25 µg/mL
kanamycin, while E. coli K-12 MG1655 and E. coli K12 BW25113 were always precultured in LB
and streaked onto LB agar plates without selecUon. Unless otherwise noted, precultures were
washed three Umes by centrifugaUon, with the supernatant removed aser each step, and the
cells resuspended in M9 medium with no carbon source to eliminate residual LB before
inoculaUon. Unless otherwise stated, M9 medium was always prepared by mixing (per litre):
200 mL 5X M9 salts (M6030, Sigma-Aldrich, St. Louis, MO, USA), 2 mL 1M MgSO4, 0.1 mL 1M
CaCl2, 1 mL 0.5 g/L FeSO4·7H2O, MQ water and appropriate amounts of a carbon source stock
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soluUon. The final M9 medium was then pH-adjusted to pH = 7.0, filter sterilized (0.22 μm) and
stored at 4°C unUl use.
Selec)ng carbon sources for E. coli K-12 MG1655 batch cultures
To complement the exisUng exometabolome data from batch cultures of E. coli on glucose (12),
we aimed to select three carbon sources that differed in chemical class and caused variaUon in
metabolic flux pakerns. We used the ecGEM eciJO1366 of E. coli K-12 MG1655 without any
modificaUons and parsimonious FBA to simulate opUmal flux pakerns across 104 different
growth supporUng metabolites (35, 66). We then performed a PCA analysis of the predicted
fluxes (as Boolean values) to compare flux pakerns between the carbon sources (Fig. S5). We
used HDBSCAN (67) to idenUfy clusters and selected from the different clusters in total 10
compounds that also differed in chemical class (sugars, amino acids and organic acids) and their
entry point into central carbon metabolism (Fig. S5). We then screened the growth of the
selected carbon sources in triplicates over 48 hours in 96-well plates (Fig. S5). For this
experiment, we prepared M9 medium with each of the 10 different carbon sources to a
concentraUon scaled to 120 mM carbon atoms. From washed LB precultures, E. coli K-12 MG155
was inoculated to OD600 = 0.05 in 200 μL of media and culUvated with conUnuous shaking
(double orbital, 425 cpm) in a BioTek Synergy H1 (Agilent Technologies, Winooski, VT, USA) plate
reader at 37 °C for 48 hours. We ulUmately chose galactose, L-alanine and L-malate, as they
supported rapid growth, differed in chemical class, entered central metabolism at different
locaUons and were grouped into different clusters based on flux pakerns (Fig. S5).
E. coli K-12 MG1655 batch cultures in bioreactors with different carbon sources
E. coli K-12 MG1655 was culUvated in lab-scale bioreactors using the three chosen carbon
sources. Their concentraUons were normalized by the number of carbon atoms to a carbon
atom concentraUon of 120 mM, corresponding to 20 mM galactose (G0625, Sigma-Aldrich), 30
mM L-malic acid (02290, Sigma-Aldrich) and 40 mM L-alanine (A7627, Sigma-Aldrich). M9
medium with these three carbon sources were prepared as described above using 25X carbon
source stock soluUons.
The strain was streaked from a frozen glycerol vial onto an LB agar plate and incubated at 37 °C
overnight. One colony was transferred to a 250 mL baffled shake flask containing 40 mL LB
medium. Aser 7 hours, a culture volume corresponding to a start OD600 = 0.05 was inoculated
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to a 500 mL baffled shake flask containing 100 mL M9 + 40 mM L-alanine. This flask was
incubated for 36 h (200 rpm, 37 °C). For the two other carbon sources, the strain was incubated
in LB for 17 h before inoculaUng a culture volume corresponding to OD600 = 0.05 in a 500 mL
baffled shake flask containing 100 mL M9 + 20 mM L-galactose or M9 + 30 mM L-malic acid,
respecUvely. The flasks were incubated for 24 h (200 rpm, 37 °C). Before inoculaUon to
bioreactors, M9 precultures were centrifuged (3220 rcf, 10 min, 4 °C), supernatant removed,
and pellet resuspended in M9 medium without carbon.
Batch culUvaUons were performed in 1 L DASGIP bioreactors (Eppendorf DASGIP, Jülich,
Germany) with an iniUal volume of 600 mL M9 medium supplemented with either 20 mM
galactose, 30 mM L-malic acid or 40 mM L-alanine, three replicates per condiUon. The reactors
were equipped with two Rushton impellers and probes for measurements of dissolved oxygen
(DO) and pH. Submerged aeraUon was maintained at 0.5 vvm, and agitaUon was cascaded
between 400 and 800, controlled by a DO set point of 30 %. pH set point was 7.0 and controlled
using 2 M NaOH and 2 M HCl. Start OD 600 was 0.05.
Sampling was performed regularly during the exponenUal growth phase with addiUonal samples
collected during staUonary phase. OD600 was measured at all Ume points and supernatant
stored: 2 mL culture was centrifuged (3220 rcf, 10 min, 4 °C), and supernatant frozen in -20 °C.
At the end of exponenUal phase and at the end of the experiment, samples were collected for
cell dry weight (CDW). 50 mL culture was centrifuged (3220 rcf, 10 min, 4 °C), supernatant
removed, cell pellet resuspended in 50 mL MQ water, centrifuged, supernatant removed, cell
pellet resuspended in 5-10 mL MQ water and transferred to a pre-weighed aluminium beaker
and dried at 105 °C for 24 hours. Beakers were then weighed again and CDW calculated.
Exometabolome analyses of )me-series samples from E. coli K-12 MG1655 batch cultures
with different carbon sources
Four samples from each of the nine batch cultures (three replicates of three different media)
plus media samples were analysed with LC-MS and GC-MS to measure the extracellular
concentraUon of metabolites at different Ume points throughout the experiment. The Ume
points were selected based on Ume-series culUvaUon data to cover the exponenUal growth
phase (three samples) plus a staUonary phase sample (Fig. S6). Samples from the different
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replicates were aligned based on the Uming of the end of the exponenUal growth phase (Fig.
S6).
LC-MS of selected bioreactor samples was conducted by the Metabolomics facility at UNIL using
their method “h igh-coverage targeted analysis of polar metabolites”, following this procedure:
Media samples were thawed on ice. An aliquot (20 µL) was extracted with the addiUon of ice-cold
methanol (80 µL), vortexed (30 sec) and centrifuged (15000 rpm, 15 min, 4°C). The supernatants
were transferred to vials for liquid chromatography – tandem mass spectrometry (LC-MS/MS)
analyses. The extracts were analyzed by hydrophilic interacUon chromatography coupled to
tandem mass spectrometer (6496 iFunnel , Agilent Te chnologies) using mulUple reacUon
monitoring - MRM approach in both, posiUve and negaUve ionizaUon modes, to maximize the
polar metabolome coverage. The analyUcal condiUons have been described in detail elsewhere
(68, 69). Raw LC-MS/MS metabolome data were processed using the Mass Hunter QuanUtaUve
analysis sosware (Agilent Technologies). The peak areas (or extracted ion chromatograms (EICs)
for the monitored MRM transiUons) were used for relaUve comparison of metabolit e levels
between different condiUons or groups of samples. Data quality assessment, including signal dris
correcUon, was performed using pooled quality control (QC) samples analyzed periodically
throughout the enUre batch.
Metabolite quanUficaUon was performed using stable isotope labeled internal standards and
calibraUon curves following the signal dris correcUon. Data processing was done using
MassHunter QuanUtaUve analysis. Peak area integraUon was manually curate d, and
concentraUons were reported by selecUng a 6-point porUon of the linear standard curves relevant
for the observed concentraUons.
The relaUve LC-MS data was standardized before subsequent analyses and data processing.
Both the relaUve and absolute LC-MS data were cleaned of obvious outliers. For the absolute
data the outliers were caused by carry-over from previous samples leading to too high malate
(six samples) and succinate (one sample) values. For the relaUve LC-MS data there were
addiUonal outliers of unknown reasons (39 values in total) related to in total 14 metabolites. For
several metabolites there were more missing values (not detected/not quanUfied) in the
absolute than in the relaUve data. For a few metabolites (phenylalanine, proline, creaUne) we
leveraged good linear relaUonships between relaUve and absolute data (R2>0.8) to esUmate the
missing absolute values using a simple linear transformaUon.
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GC-MS analysis of the same samples was conducted in the following way: AnalyUcal standards
were prepared as M9 medium with increasing concentraUons of acetate, lactate, pyruvate,
formate and propionate and stored at -70°C unUl use. Samples from the E. coli bioreactor batch
cultures and analyUcal standards were thawed on iced. Then, 100 μL was transferred to an
Eppendorf tube and kept on a cold block (-20 °C) while adding 5 μL 11% HCl and 500 μL diethyl
ether. Tubes were capped, vortexed on a thermoblock (2000 rpm, 10 min, 1°C) and centrifuged
(13 000 rcf, 5 min, 4°C). The top organic phase layer was pipeked to a glass vial and derivaUzed
with 20 μL N-(t-butyldimethylsilyl)-N-methyltrifluoroacetamide (MTBSTFA) and vortexed briefly.
Samples were then placed on a heat block (90 min, 35°C) and kept at 16°C unUl analysis. The
samples were injected (1 μL) by a Pal3 autosampler onto an Agilent 8890-5977B GC-MSD
(Agilent Technologies) with a VF-5MS (30 m x 0.25 mm x 0.25 mm) column. The samples were
injected with a split raUo of 15:1, helium flow rate of 1 mL/min and inlet temperature of 230 °C.
The temperature was held for 2 min at 50 °C, raised at 25 °C/min to 175 °C, 30 °C/min to 280 °C
and held for 3.5 min. The MSD was run in scan mode from 40-500 Da. Analyte abundances were
calculated using the MassHunter QuanUtaUve Analysis sosware (Agilent Technologies).
Absolute concentraUons were calculated using standard curves.
Galactose concentraUons were measured using the L-Arabinose/D-Galactose assay kit (K-ARGA,
Megazyme, Bray, Ireland), following their rapid protocol for analyses in 96-well plates.
Es)ma)on of metabolite release rates of E. coli, B. licheniformis, C. glutamicum and S.
cerevisiae in glucose medium
Time-series data on biomass (in OD600) and absolute extracellular metabolite concentraUons
from batch culUvaUons of E. coli, B. licheniformis, C. glutamicum and S. cerevisiae in high
glucose concentraUons (10-20 g/L) (12) was kindly provided by the authors (mean and standard
deviaUons). For metabolites reported as a sum of two metabolites we akributed equal amounts
to those metabolites to enable direct comparison with metabolite values esUmated for
individual metabolites (described below). This includes 2-phosphoglycerate/3-phosphoglycerate
and ribulose 5-phosphate/xylulose 5-phosphate. To esUmate the metabolite release and uptake
rates of each species we first converted the OD600 values to gDW/L. For E. coli we used the
conversion factor we esUmated from our own cell dry weight measurements in M9 galactose
medium (0.346 gDW/L/OD600), which is comparable, but on the lower end of values found in the
literature (0.36-0.515 gDW/L/OD600) (70, 71). For the three other species we used literature
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values: B. licheniformis (data from B. subUlis) 0.48 gDW/L/OD600 (72); C. glutamicum 0.27
gDW/L/OD600 (73); S. cerevisiae (mean of literature values) 0.746 gDW/L/OD600 (70). We then
integrated the translated biomass Ume-series data to obtain biomass AUC data that we
leveraged together with the mean absolute exometabolome data to esUmate the uptake or
release rates for each measured metabolite for each species using linear regression (Figs. S1-
S4). Rates were only esUmated for the exponenUal growth phase, and only unUl each
metabolite either saturated or was clearly being re-consumed.
Theore&cal jus&fica&on of es&ma&ng uptake or release rates from extracellular concentra&ons
We start out from a simple assumpUon that the change in extracellular concentraUon 𝐶! of
metabolite i can be explained by the net release or uptake 𝑎!(𝑡) (by any mechanism) by the
microbes with biomass density 𝑋(𝑡) in the batch culture:
𝑑𝐶!
𝑑𝑡 = 𝑋(𝑡) ⋅ 𝑎!(𝑡)
The concentraUon 𝐶!(𝑡) at a given Umepoint t is thus:
𝐶!(𝑡) = + 𝑋(𝑡) ⋅ 𝑎! (𝑡)𝑑𝑡
"
"#
+ 𝐶!(𝑡#)
If we assume that the uptake or release rate 𝑎!(𝑡) is constant, we see that the concentraUon
𝐶! (𝑡) is described by a linear funcUon of the constant release rate and the integrated biomass
(area under the curve, AUC):
𝐶!(𝑡) = 𝑎! + 𝑋(𝑡)𝑑𝑡
"
"#
+ 𝐶! (𝑡#) = 𝑎! ⋅ 𝑋$%& (𝑡) + 𝐶#
Hence, when metabolites are released at constant rates the dynamics should be well explained
by a linear regression of extracellular metabolite concentraUons on biomass AUC, and the
specific net rate (uptake or release) is the slope of the curve.
Es)ma)on of metabolite release rates of E. coli in galactose, L-malate and L-alanine
For our bioreactor batch culUvaUons of E. coli in galactose, L-malate and L-alanine, we used
paired cell dry weight measurements and OD600 readings to calculate conversion factors used to
translate OD600 values for all Ume points (galactose: 0.346 ± 0.016; L-malate: 0.279 ± 0.017; L-
alanine: 0.296 ± 0.011; mean ± std in gDW/L/OD600). The translated Ume-series data was used
to calculate the biomass area under the curve used to esUmate metabolite release and uptake
rates further described below.
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We esUmated the metabolite uptake or release rate by performing for each metabolite and
each carbon source a linear regression of measured concentraUon (relaUve or absolute) vs
biomass AUC using the three samples (Umepoints T1-T3) acquired from the three replicate
batch cultures during exponenUal phase plus the iniUal M9 medium (T0; Figs. S7-S9). To avoid
underesUmaUng release rates for metabolites that potenUally were being re-consumed at the
end of the exponenUal phase we discarded the last Umepoint from the exponenUal phase in
cases where the rate was posiUve (indicaUng metabolite release) but there was a significant
reducUon in extracellular concentraUon from T2-T3 (P < 0.05, one-sided t-test). For 17 (of 126)
metabolites we chose to not include T0 for at least one of the three condiUons in the linear
regression, either because of very large variability of T0 or because the trend from T0 to T1 was
clearly different from the general trend from T1-T3. We only esUmated the rate for metabolites
where we had at least three data points from at least two different Ume points. For the
metabolites where we had both relaUve and absolute data, we used the absolute data if there
were enough absolute data points to get adequate slope esUmates. For seven metabolites
(glutamine, alpha-aminoadiapate, serine, lysine, lactate, NAD and isocitrate) where both
absolute and relaUve quanUficaUon was performed, we could esUmate the rate more accurately
on the relaUve data set (because of more missing data points in the absolute data set).
However, there were sufficient absolute measurements to esUmate the absolute spread
(standard deviaUon) of these data points, enabling translaUon of the slope value from Z-score to
μmol/gDW/h.
Es)ma)on of metabolite release rates of E. coli, P. p u 9 d a, an Enterobacter sp. and a
Pseudomonas sp. in various carbon source environments
The dataset from Vila et al. (2023) was kindly provided by the authors. The dataset contains
exometabolome data from three Umepoints (16, 28, and 48 hours) of E. coli MG1655, P. p u G d a
KT2440, and two environmental isolates of the genera Enterobacter and Pseudomonas,
respecUvely (43). All species were culUvated in M9 medium with one of five carbon sources (D-
glucose, D-fructose, glycerol, pyruvate or L-malate). AddiUonally, the dataset includes
exometabolome data from two Umepoints (28 and 48 hours) of E. coli and the Enterobacter sp.
on D-ribose, L-arabinose and D-galactose, and of P. p u G d a and the Pseudomonas sp. on acetate,
fumarate and succinate. To esUmate metabolite release rates, we first used the plate reader
growth curves to calculate biomass AUC aser 16, 28 and 48 hours and to idenUfy the end of
exponenUal growth of each organism in each condiUon. The end of exponenUal phase was
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automaUcally idenUfied as the first peak in the second derivaUve of the smoothed growth curve
with an OD600 above 60% of maximum. We converted the AUC from OD600 to gDW/L using the
same conversion factor for all the different carbon source environments: 0.36 gDW/L/ OD600 for
E. coli and the Enterobacter sp., mean of measured values and literature values (70, 71); 0.476
gDW/L/ OD600 for P. p u G d a and the Pseudomonas sp, mean of literature values (74, 75). Finally,
we performed a linear regression between extracellular metabolite concentraUons and AUC on
both duplicates of each strain/carbon source combinaUon including all datapoints before the
end of exponenUal growth + 2 hours (a buffer to account for some inaccuracy in the automaUc
detecUon). We only included rate esUmates for metabolites that were quanUfied at least twice
for each strain. As the dataset did not include an early Umepoint or media measurement we
assumed the iniUal concentraUon of each metabolite to be 0. If a metabolite was detected more
at more than one Umepoint we discarded the esUmated rate if there was a qualitaUve
discrepancy in slope value when the slope was esUmated with or without the T0 concentraUon
assumed to be 0. If the carbon source was among the measured metabolites, this metabolite
was excluded from rate esUmaUon in those specific condiUons.
Genome-scale metabolic models
For E. coli, S. cerevisiae and C. glutamicum we used the previously developed enzyme-
constrained genome-scaled metabolic models (GEMs) eciJO1366 (35), ecCGL1 (76) and
ecYeastGEM 8.3.4 (34), respecUvely. For B. licheniformis there was no available enzyme-
constrained GEM, and we therefore opted to use the enzyme-constrained GEM ecBSU1 of the
closely related species B. subGlis (77), which was available at github.com/Ubbdc/ecBSU1. A
normal GEM for B. licheniformis is available (78), but with this model we could not achieve any
feasible flux balance soluUon. To simulate the environmental isolate of the genus Enterobacter
we used the E. coli GEM eciJO1366. For the environmental isolate of the genus Pseudomonas
and for P. p u G d a we used the enzyme-constrained version of the P. puGda GEM iJN1463 (79)
automaUcally generated by the ECMpy2 method (80), which we here refer to as eciJN1463.
We made a few minor changes to the published GEMs before predicUng metabolite values. In
the E. coli GEM eciJO1366 the proteome weight of the forward reacUon GALKr (galactokinase)
was extremely high (0.016), limiUng the growth rate on galactose to much less than the growth
rate we measured in M9 galactose medium. To enable eciJO1366 to reach the measured growth
rate with galactose as the only carbon source we replaced the proteome weight of the forward
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GALKr reacUon with the proteome weight of the reverse GALKr reacUon which was much
smaller (0.00037). For the ecYeastGEM we only merged exchange reacUons that were previously
split to simplify its use. Both ecBSU1 and eciJN1463 were translated from json to sMOMENT
format in xml (35), modified by merging split exchange reacUons and fixing metabolite
compartment names and annotaUons. For ecBSU1 we also removed the enzyme constraint on
the reacUon “PPAm_num1” (inorganic diphosphatase) as it caused unrealisUc uptake and
release rates of phosphate and diphosphate, respecUvely. The C. glutamicum GEM ecCGL1 was
also converted from the ECMpy format (36) to the sMOMENT format (35) but otherwise kept
unchanged. All GEMs were used with their default biomass equaUons as objecUve when
maximizing growth in all FBA or pFBA analyses (81). Reframed 1.5.3
(github.com/cdanielmachado/reframed) or COBRApy 0.29.1 (82) were used to load, manipulate
and run constraint-based analyses with Gurobi 10 (Gurobi OpUmizaUon, LLC) as the solver.
Calcula)on of metabolite values and metabolite turnover using genome-scale metabolic
models
In constraint-based modelling a shadow price is an esUmate of how sensiUve the objecUve
funcUon in a flux balance analysis (FBA) is to increased influx or efflux of a metabolite (83, 84).
Hence, one can interpret the shadow price as metabolite value as it quantifies the impact on
growth caused by the release of a metabolite (to have positive values we here define
metabolite value as the shadow price multiplied by -1). A similar approach to measure the cost
of metabolite release has been used to identify costless secretions (41). The metabolite value
(or the shadow price) can be predicted for a specific organism in a specific context by using a
GEM of the corresponding organism (or closely related) and then constraining this GEM to the
specific context (i.e. primarily defining metabolite uptake rates). While shadow prices are
usually estimated directly by the solver used to run FBA (37), the robustness of these values is
often questioned because of numerical issues. To get more robust shadow price estimates we
solved for each metabolite in each context a separate FBA, where we constrained the GEM to
have an (additional) release of 0.01 mmol/gDW/h of that metabolite and quantified the change
in the objective function, i.e. the change Δy in growth rate caused by the forced metabolite
release. The metabolite value was then quantified as Δy/0.01. If the metabolite was predicted
to be released by FBA, we added 0.01 mmol/gDW/h to the FBA-predicted value to estimate the
rate. This was only relevant for acetate for E. coli in the L-malate condition, for ethanol, acetate,
formate and pyruvate for S. cerevisiae, and for pyruvate for P. putida in the L-malate condition.
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Using this approach, we esUmated metabolite values for E. coli in batch cultures with glucose,
galactose, L-malate or L-alanine as the carbon source by constraining the uptake of the
corresponding exchange reacUon in eciJO1366 to the uptake rate of the carbon source as
esUmated from the experimental data. The same approach was used for C. glutamicum, B.
licheniformis and S. cerevisiae using the corresponding models. For E. coli, P. p u G d a and the two
environmental isolates of the genera Enterobacter and Pseudomonas we first extracted
maximum growth rates for each organism in each environment from growth curves (using
curveball (85)). Then, we used the respecUve GEMs to calculate the uptake rates of the
corresponding carbon sources required to sustain the maximum growth rates. These uptake
rates were then used to constrain the GEMs when esUmaUng the metabolite values as
described above. The turnover (i.e. the sum of posiUve fluxes producing an intracellular
metabolite) was esUmated by running parsimonious FBA (66), using the same GEMs constrained
in the same way as described for above for metabolite values.
To validate that the negaUve correlaUon between log-transformed metabolite values and
release rates we compared esUmates from eciJO1366 with esUmates from the 4 benchmark E.
coli K-12 MG1655 GEMs iJR904 (86), iAF1260 (87), iJO1366 (88) and iML1515 (89) that are of
increasing complexity. We then compared esUmated metabolite values and esUmated release
rates using data from E. coli in bioreactors with glucose, galactose, L-malate or L-alanine as the
sole carbon source, the same data used in Fig. 2A (Fig. S11). In the L-malate condiUon for the
iJR904 model we discarded the metabolite value for formate as an outlier because it was
extremely small (<10-12), below the solver tolerance. Note that no metabolite values were
negaUve and hence no other values were discarded upon log-transformaUon.
Metabolite classifica)on, chemical proper)es and intracellular concentra)ons
The charge and molecular weight of metabolites were obtained from eciJO1366 (35). All other
chemical properUes and InChIKeys were obtained from PubChem using the python interface
PubChemPy (github.com/mcs07/PubChemPy). The InChIKeys were then used to classify
metabolites into a chemical taxonomy using ClassyFire (90). To get an appropriate level of detail
of metabolic classificaUon we used the “Class” level category. However, we separated the class
“Carboxylic acids and derivaUves” into “Amino acids” and “Carboxylic acids” based on the
“Subclass” level. We also merged the classes “Hydroxy acids and derivaUves” and “Keto acids
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and derivaUves” into the joint class “Keto / hydroxy acids”. Finally, metabolites that did not fall
into either of the abovemenUoned categories nor the class “Organooxygen compounds” were
joined into the category “Other”.
Linear models for evalua)ng the importance of different factors for predic)ng metabolite
release rates
Linear models were created and analysed using statsmodels (91). Compound class and carbon
source was incorporated as categorical variables. Metabolites predicted to have zero turnover
was given a value of 10-4, less than the minimum predicted turnover. Release rates where
corresponding values were missing in any of the compared factors were discarded before model
fing. To evaluate the staUsUcal significance of the out-of-sample predicUons we performed 104
permutaUons of model fing and out-of-sample esUmaUons where the labels (either
metabolite or condiUon) was shuffled on each permutaUon. We then calculated the fracUon of
out-of-sample R2 values from these permutaUons below the observed R2 value to esUmate the P
value.
Cul)va)on and exometabolome analyses of KEIO knockout strains
One objecUve was to study how disrupUon of key metabolic fluxes would affect extracellular
metabolite concentraUons and how this would change if these strains were allowed to evolve in
a simple nutrient environment. The KEIO collecUon is a collecUon of non-essenUal E. coli KO
strains that we could use for this purpose (55). To idenUfy relevant KEIO KO strains we used
eciJO1366 and parsimonious FBA (81) to predict the effect of a gene knockout on opUmal
metabolic fluxes, and previous metabolomics data (54) of these strains to see the effect on
intracellular concentraUons (Fig. S20A). We eventually chose seven strains (ΔaceE, ΔcyoD,
ΔnuoA, Δpgi, Δrpe, ΔsdhB, ΔsucB) that were predicted to have different opUmal flux
distribuUons, had many significantly changed intracellular metabolite concentraUons, and
targeted different part of key metabolic pathways (Fig. S20). We included ΔlacA as a negaUve
control expected to behave like the WT as done previously (92).
The selected strains from the KEIO collecUon were precultured on LB agar and liquid LB as
previously described, and glycerol stocks used for experiments described below were prepared
by adding glycerol to a final concentraUon of 25 %.
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For exometabolome sampling, the KEIO strains and E. coli BW25113 were precultured as
detailed above. They were then re-inoculated to OD600 = 0.05 in 10 mL M9 + 40 mM galactose (+
25 µg/mL kanamycin for KEIO strains) in 50 mL Erlenmeyer flasks (200 rpm, 37 °C, 31 h). 1 mL
culture was sampled into Eppendorf tubes and washed twice with M9 without carbon source by
centrifugaUon (6000 rcf, 6 min, 4°C). UlUmately, samples were resuspended in 0.5 mL M9
without carbon source and used to inoculate 200 μL M9 + 40 mM galactose (+25 µg/mL
kanamycin for KEIO strains) in a flat bokom 96-well plate to OD600 = 0.05 and 6 mL M9 + 40 mM
galactose (+25 µg/mL kanamycin for KEIO strains) to straight glass tubes (15.8 cm tall, 1.5 cm
diameter) to OD600 = 0.005. The 96-well plate was incubated in a Synergy H1 plate reader with
conUnuous shaking (double orbital, 425 cpm, 37 °C), and the glass tubes in a shaking incubator
(200 rpm, 37 °C, 45° angle), both for 108 hours. The experiment in the well plate was used to
monitor more closely the growth (as OD600) of these strains and to help with the Uming of the
exometabolome sampling. All strains were culUvated in three replicates. Two samples were
collected during mid-exponenUal growth phase for all cultures, mostly to ensure that at least
one sample from each replicate was obtained before the end of exponenUal phase. 1 mL culture
volume was centrifuged (14 000 rpm, 10 min, 4 °C), and supernatant stored in -70 °C for
exometabolome analysis. The second sample for each replicate (Fig. 4A) was analysed using LC-
MS at the UNIL Metabolomics facility, following their protocol described above. AddiUonally, we
also analysed three samples of pooled inoculums to verify that any carry-over with the
inoculum was much lower (or below detecUon limit) of than the sample metabolite
concentraUons. Three replicate pooled samples were obtained by inoculaUng 6 mL M9 + 20 mM
galactose medium with all the strains, each strain to an OD600 = 0.005, and subsequently
handled as described above for the culture samples.
Chemostat evolu)on experiment with ΔaceE and ΔsucB in bioreactors
Two of the KEIO KO strains, ΔaceE and ΔsucB, were selected for the evoluUon experiment with
conUnuous culUvaUon (chemostats) in bioreactors based on their reduced growth compared to
their ancestor and difference in exometabolome pakerns (Figs. 4A and S21-S23). The strains
were streaked from glycerol vials onto LB + 25 µg/mL kanamycin agar plates and incubated at 37
°C overnight. 5-6 colonies were transferred to 500 mL baffled shake flasks containing 75 mL LB +
25 µg/mL kanamycin and incubated for 22 h (200 rpm, 37 °C).
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Chemostat culUvaUons were performed in 1 L DASGIP bioreactors with a constant volume of
300 mL M9 + 20 mM galactose medium + 25 µg/mL kanamycin (prepared as previously
described, but without pH adjustment because of pracUcal challenges with the large volumes
required, so pH ≈ 7.1). CulUvaUon was performed at 37 °C with a submerged airflow maintained
at 0.5 vvm, and a cascaded agitaUon of 400-700 rpm, controlled by a DO set point of 30 %. pH
control was started at day 6 (ΔaceE) or day 20 (ΔsucB) with a set point of 7.1, controlled using 2
M NaOH (Fig. S25A).
The reactors (three replicates per strain) were inoculated to OD600 = 0.1. During the late stage of
exponenUal growth, pumps were started to feed fresh culture medium and remove used
medium. Medium was fed using a pre-calibrated peristalUc pump and used medium was
removed by a steel pipe placed right above the culture surface. The steel pipe was coupled to a
peristalUc pump operaUng at a flow rate approximately 1.5x of the medium in flow, to avoid
volume accumulaUon. The set diluUon rate was adjusted several Umes during the experiment to
compensate for (someUmes surprising) changes in growth dynamics (from 0-0.1 h-1 for ΔaceE, 0-
0.3 for ΔsucB, Fig. S25B). The actual diluUon rate was monitored by keeping the flasks with fresh
culture medium on scales. OD600 was measured daily, and weekly, larger samples were
collected. Culture was centrifuged (3220 rcf, 10 min, 4 °C), and supernatant and pellet stored at
-70 °C. In addiUon, cultures were preserved at -70 °C as glycerol stocks. The number of
generaUons were esUmated from the measured diluUon rates across the experiment plus the
generaUons during the iniUal batch culture phase before the culture diluUon was started.
Cul)va)on of single colonies from evolu)on experiment and sampling of exometabolome
Culture samples from different bioreactors and Umepoints collected in the chemostat
experiment were streaked out onto LB + 25 µg/mL kanamycin agar plates and incubated
overnight at 37 °C. Three colonies were picked and individually inoculated in 20 mL LB + 25
µg/mL kanamycin in 100 mL Erlenmeyer flasks and incubated (37 °C, 200 rpm, 16 h). 12 mL of
the culture was then centrifuged (3220 rcf, 6 min, RT), and the pellets stored at –20 °C for
sequencing. The isolates were stored as glycerol stocks at -70 °C made from these cultures.
2 mL samples from the precultures were washed as previously described, resuspended in M9
without carbon source, and used to inoculate a flat bokom 96-well plate to OD600 = 0.05 with
200 µL M9 + 25 mM galactose + 25 µg/mL kanamycin. The M9 medium was prepared as
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previously described, but to a pH of 7.1 as in the chemostats. The well plate was incubated in a
Synergy H1 plate reader with conUnuous shaking (double orbital, 425 cpm, 37 °C, 120 h) and the
OD600 was read every 20 minutes.
Based on these growth measurements we selected the fastest growing isolates from the last
Umepoint of each of the six bioreactors (three bioreactors per strain). These isolates, the iniUal
KEIO KO strains ΔaceE and ΔsucB, and the KEIO ancestor E. coli BW25113 were precultured and
subsequently washed as described above. The washed preculture were used to inoculate 10 mL
M9 + 20 mM galactose to OD600 = 0.01 in straight glass tubes (15.8 cm tall, 1.5 cm diameter) in
triplicates and incubated for 20-84 hours (200 rpm, 37 °C, 45° angle). 1 mL samples for
exometabolome analysis were collected at OD600 ≈ 1 (Fig. 4, D and E), filtered using a 0.22 μm
Millex-GV PVDF syringe filter (SLGVR33RS, MilliporeSigma, Darmstadt, Germany) into a 1.5 mL
Eppendorf tube stacked in a cold block (-20 °C), and then stored at -70 °C unUl it was analysed.
The exometabolome LC-MS analyses were conducted by the UNIL Metabolomics facility,
following the procedure described above.
DNA extrac)on of samples from selected isolates and chemostat culture samples
The DNA extracUon of 14 different samples from the chemostat cultures (#37A D44 M2 Pellet,
#38A D44 M3 Pellet, #39A D44 M4 Pellet, #28B D30 M5 Pellet, #29B D30 M6 Pellet, #30B D30
M7 Pellet) and the selected isolates (sucB-M5-D30-4, sucB-M6-D30-6, sucB-M7-D30-4, sucB-
Ancestor, aceE-M2-D44-2, aceE-M3-D44-3, aceE-M4-D44-1, aceE-Ancestor) was performed by
adapUng the protocol from the FastPure Bacteria DNA IsolaUon Mini Kit (DC103-01, Vazyme,
Nanjing, China). 1 mL GA buffer was added to the thawed pellet samples, and 230 µL of these
resuspensions were kept in Eppendorf tubes for DNA extracUon. The rest was centrifuged (4000
rpm, 6 min, RT) and the pellet stored at –20 °C. Genomic DNA (gDNA) was extracted from the
230 µL sample following the manufacturer’s protocol. In the final step, eluUon of the DNA was
performed twice with fresh eluUon buffer, eluUng a total of 100 µL DNA. Extracted gDNA was
stored at –70 °C unUl sequencing.
Genomic sequencing processing
Genomic DNA from the selected isolates and chemostat samples was sequenced by Novogene
(Planegg, Germany) using the Illumina NovaSeqX PE 150. The isolates and the bioreactor
samples were sequenced to 1 Gb and 10 Gb sequencing depth, respecUvely. Good quality of
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both datasets was ensured using fastqc v. 0.12.1 before trimming the reads with fastp v. 0.24.0
(--qualified_quality_phred 20 --cut_front --cut_tail --average_qual 20 --length_required 50) (93,
94). Both read sets were mapped against the E. coli BW25113 reference genome (NCBI RefSeq
assembly GCF_000750555.1) with minimap2’s v. 2.28 default “sr” parameters (95). The resulUng
alignments were filtered with samtools view v. 1.20 (-b -f 3 -q 60) to filter out reads not properly
mapped in pairs or mapped to the reference with a MAPQ lower than 60 (96). Average coverage
was assessed for both datasets showing a minimum average coverage for the chemostat culture
samples of 2017 and 190 for the sequenced isolates.
For both datasets, variants were idenUfied with freebayes v. 1.3.6 (--min-alternate-count 3 -p 1 -
-min-alternate-fracUon 0.05 --pooled-conUnuous --haplotype-length 0) and annotated with
snpEff v. 5.0 using the BW25113 reference genome (97, 98). A custom python script was used to
filter the annotated variants. For the isolates, variants with a frequency lower than 0.95 and a
coverage lower than 100 were filtered out. For the chemostat culture samples, variants with a
frequency lower than 0.05 and coverage lower than 100 were filtered out. A variant was
considered fixed if its alle frequency was at least 0.9.
Paired intracellular and extracellular metabolomics and live/dead staining
M9 medium with 20 mM galactose, 30 mM malate or 40 mM L-alanine was prepared as
detailed above. E. coli K-12 MG1655 was precultured on LB agar plates and in liquid LB as
detailed above. 1 mL preculture was washed as described above and used to start a second
preculture in 20 mL M9 + 40 mM L-alanine, inoculated to OD600 = 0.05. Another LB preculture of
E. coli K-12 MG1655 was used to inoculate a second M9 + 20 mM galactose and a M9 + 30 mM
malate preculture in the same way 12 hours later. Aser 36/24 hours, 1 mL was collected from
each of the three precultures and washed twice as detailed above. These washed precultures
were used to inoculate 10 mL of the same media (M9 + either 20 mM galactose, 30 mM malate
or 40 mM L-alanine) in straight glass tubes (15.8 cm tall, 1.5 cm diameter). These glass tubes
were incubated for two days (200 rpm, 37 °C, 45° angle). Growth was monitored by measuring
OD600 directly in the glass tubes (NANOCOLOR VIS II, MACHEREY-NAGEL, Düren, Germany) at 21
Umepoints. The glass tubes were vortexed briefly before any OD reading or sampling.
A reference exometabolome 0.5 mL sample was collected aser 2 hours following the procedure
detailed below. Then, 2 mL samples for paired intra- and extracellular metabolome and
live/dead analyses were collected in the late exponenUal phase (at OD600 ≈ 1.1, Fig. S30).
Exometabolome samples were obtained by filtering 0.5 mL culture using a 0.22 μm Millex-GV
PVDF syringe filter (SLGVR33RS, MilliporeSigma) into a 1.5 mL Eppendorf tube stacked in a cold
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block (-20 °C). The samples for intracellular metabolomics, i.e. cells, were obtained immediately
aser following this procedure: A 25 mm 0.22 μm Durapore PVDF filter (GVWP02500,
MilliporeSigma) was placed in a new filter holder. A 5 mL syringe was connected to the inlet of
the filter holder and a vacuum pump (250 mbar) was connected to the outlet of the filter
holder. Then, 2 mL of 37 °C MQ water was added to pre-wet the filter. Immediately aser, 1 mL
of culture sample was added to the syringe and allowed to pass through the filter. If the culture
did not pass through solely based on the vacuum pump, light addiUonal pressure was added by
using the syringe itself to push the culture through the filter. This process took 10-30 seconds.
SUll using the same set-up, the filter was finally rinsed with 5 mL of 37 °C MQ water as
previously recommended (49). Two tweezers were quickly rinsed in MQ water and used to
carefully transfer the filter from the filter holder to 2 mL lysis tubes filled with 1.4 mL of 80:20
methanol:water (v/v), pre-chilled to -20 °C and kept on a cold block also pre-chilled to -20 °C. All
samples were then quickly transferred to -70 °C for storage. Live/dead staining was performed
using a similar approach as previous work (99): Briefly, the live sample was made by diluUng 10
μL culture in 990 μL PBS and the dead sample was made by mixing 100 μL culture with 1 mL
70% isopropanol. Both samples were vortexed and incubated at room temperature for 1 h.
Then, the isopropanol was removed from the dead sample by centrifugaUon (8000 rcf, 4 min,
RT), pipeng off the supernatant, resuspending the pellet in 1 mL PBS and vortexing. This
procedure was repeated once. Then, both the live and the dead sample were stained with
propidium iodide (PI; P4170, Sigma-Aldrich) and SYBR green (Invitrogen S7563, Thermo Fisher
ScienUfic, Carlsbad, CA, USA) with the following procedure: 48 μL sample (live or dead) was
mixed in a 96-well plate with 49 μL PBS, 2 μL 0.5 mg/mL PI and 1 μL 100X SYBR green and
incubated for 15 min in the dark. Then, a 0.1X samples of both the stained live and the stained
dead samples were created by diluUng 10 μL of each sample in 90 μL of PBS. The stained
live/dead samples were then analyzed immediately on a CytoFLEX S flow cytometer (Beckman
Coulter, Brea, CA, USA) and the CytExpert sosware (v2.4.0.28). The dead samples were used to
make the gaUngs required to quanUfy the fracUon of dead cells in the live samples (Table S6).
The extra- and intracellular metabolomics samples were analysed by the metabolomics facility
at UNIL to quanUfy the five metabolites leucine, glutamate, aspartate, fructose 6-phosphate and
cis-aconitate. These metabolites were chosen because they were chemically and metabolically
diverse and likely to be quanUfiable both intracellularly and extracellularly based on previous
experience with similar samples. Also, as glutamate is the most abundant intracellular
metabolite (49, 100), it serves as a best-case scenario in our akempt to test how much of the
extracellular metabolite levels that can be explained by cell lysis and the associated release of
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intracellular metabolites. Intracellular metabolite samples were first normalized by the amount
of protein detected in the same sample and subsequently converted to absolute intracellular
concentraUons using the esUmated protein density in E. coli (13.5 ⋅ 10'( µg µm)⁄ ) (101). The
fructose 6-phosphate value for sample 1B, Umepoint 1, was discarded as an outlier as it was one
order of magnitude larger than any other fructose 6-phosphate measurements.
Calcula)on of contribu)on from intracellular metabolites and cell lysis to extracellular
concentra)ons
Approximate cell volume was esUmated from measured OD600 and a previous esUmate of OD to
cell volume for E. coli of 3.6 μL/ΟD600/mL (102). From approximate cell volume, measured
absolute intracellular concentraUons and cell lysis fracUons we then calculated the
corresponding change in extracellular concentraUons. This potenUal contribuUon was then
compared to the net change in extracellular concentraUons between the T0 reference sample
(aser 2-hours) and the late exponenUal phase sample. If all T0 values were below the detecUon
limit, we assumed the iniUal concentraUon of this metabolite to be 0. If only some values at T0
were below the detecUon limit we imputed these values to the mean of the detected values,
giving conservaUve esUmates for the net change in extracellular concentraUons. To esUmate a
potenUal contribuUon from protein depolymerizaUon we esUmated cell density in gDW/L from
OD600 (0.346 gDW/L/OD600) and from this specific amino acid density (in g/L) from recent
esUmates of E. coli amino acid mass fracUons (103). Where mass fracUons were akributed to
pairs of amino acids (glutamate/glutamine and aspartate/asparagine) we assumed equal
contribuUons. Amino acid density was converted from g/L to μΜ by dividing by the amino acids’
molecular weight subtracted the weight of a water molecule to account for the condensaUon
reacUon in protein polymerizaUon. A similar procedure as described above was followed when
we extended this analysis by using literature values for intracellular concentraUons. When
extracellular concentraUons were reported as two indisUnguishable molecules, we akributed
equal amounts to the two metabolites. This includes 2-phosphoglycerate/3-phosphoglycerate
and ribulose 5-phosphate/xylulose 5-phosphate. To idenUfy typical biomass degradaUon
products we used the metabolites consumed by the biomass equaUon of the E. coli model
iML1515 (89), although excluding the soluble pool (as categorized in (87)) since this should
correspond to the intracellular concentraUons already accounted for. Of the metabolites in our
dataset (Fig. 3B), only the amino acids were among the consumed biomass components and
therefore considered to be typical biomass degradaUon products.
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