1. Introduction
Benzylsuccinic acid, a natural product originally identified as carboxypeptidase inhibitor [
1,
2], has later been identified as first intermediate in the anaerobic degradation of toluene [
3,
4,
5]. Accordingly, benzylsuccinate and related compounds generated from other hydrocarbons have been detected in contaminated anaerobic environments such as groundwater aquifers or sediments and are used to evaluate the extent of both contamination and bioremediation [
6,
7,
8]. While chemical synthesis of benzylsuccinate has been reported by relatively complex procedures [
9] which yield racemic mixtures, only the separate (
R)- or (
S)-enantiomers show biological functions. For example, only (
R)-benzylsuccinate is produced during anaerobic toluene degradation or is active as carboxypeptidase inhibitor, whereas (
S)-benzylsuccinate is used as a specific building block for the diabetes drug mitiglinide [
10]. Benzylsuccinate has also been reported as component of a butylene succinate co-polymer with interesting characteristics [
11]. Thus, there are prospects for a potential industrial application of the benzylsuccinate enantiomers, which may be enhanced by establishing a biotechnological process capable of a more convenient and enantiospecific synthesis.
In nature, (
R)-benzylsuccinate is formed during anaerobic toluene degradation as an obligate intermediate by all known bacteria which couple this metabolic pathway to anaerobic respiration with nitrate, sulfate, metal ions or protons, or to anoxygenic phototrophy [
12]. Remarkably, the same principal reactions and highly similar orthologues of all the enzymes are used throughout by bacteria of very different taxonomic groups [
4,
12]. The pathway is initiated by the highly unusual stereospecific addition of the methyl group of toluene to the double bond of a fumarate cosubstrate to generate (
R)-benzylsuccinate [
13,
14]. This reaction is catalyzed by the glycyl radical enzyme benzylsuccinate synthase, a highly oxygen-sensitive enzyme that needs to be activated to the active glycyl radical state by a separate S-adenosylmethionine-dependent activating enzyme [
15,
16]. The reaction has been shown to involve the addition of a benzyl radical generated from toluene to the
Re-Re face of a bound fumarate and the return of the initially abstracted hydrogen atom to the resulting product radical in a
syn addition mode [
17]. In addition, the reaction involves a steric inversion of the configuration of the methyl group of toluene [
18]. All these mechanistic details are fully consistent to the predicted reaction mechanism from quantum mechanics modelling [
19] based on the X-ray structure of the enzyme[
20,
21].
Further degradation of (
R)-benzylsuccinate proceeds via β-oxidation to benzoyl-CoA and succinyl-CoA in five subsequent enzymatic steps [
22]. This pathway is initiated by benzylsuccinate CoA-transferase (BbsEF) which uses succinyl-CoA as CoA-donor for activating the intermediate to 2-(
R)-benzylsuccinyl-CoA [
13,
23], which is then dehydrogenated to (
E)-benzylidenesuccinyl-CoA by benzylsuccinyl-CoA dehydrogenase (BbsG)[
24]. The next steps consist of hydration of the double bond by benzylidenesuccinyl-CoA hydratase (BbsH) and another dehydrogenation of the alcohol intermediate by (
S,
R)-2-(α-hydroxybenzyl)succinyl-CoA dehydrogenase (BbsCD) [
25]. Finally, the resulting 3-oxoacyl-CoA intermediate (
S)-benzoylsuccinyl-CoA is thiolytically cleaved to benzoyl-CoA and succinyl-CoA by the thiolase BbsAB [
26] (
Figure 1). Succinyl-CoA is used as CoA-donor for activating benzylsuccinate, and benzoyl-CoA is further degraded by reducing the aromatic ring via benzoyl-CoA reductases [
27]. All enzymes involved in anaerobic toluene degradation have been biochemically characterized and while the benzylsuccinate synthase reaction appears to be thermodynamically irreversible [
12,
19,
28,
29], all reactions of the enzymes of the β-oxidation pathway have been shown to be reversible [
23,
24,
25,
26]. Moreover, the enzymes and their gene organization in two co-induced operons are completely conserved in all known anaerobic toluene degrading bacteria[
12]. These operons are the
bss operon containing the genes for the subunits of benzylsuccinate synthase (BssABC) and its activating enzyme (BssD), and the
bbs operon containing the genes for the enzymes of benzylsuccinate β-oxidation.
In this communication, we establish a synthetic pathway for benzylsuccinate production in Escherichia coli. Because of the extreme sensitivity of benzylsuccinate synthase against oxygen, we attempted to produce benzylsuccinate via the degradative β-oxidation pathway running in reverse. To acchieve this, we established one plasmid coding for a metabolic module for the uptake of benzoate and its activation to benzoyl-CoA and combined it with a second co-expressed plasmid containing the bbs genes. We indeed observed the production of benzylsuccinate under different growth conditions, especially anaerobic glucose-fermenting cultures, which provide the cosubstrate succinate as fermentation product.
3. Discussion
Synthetic pathways for producing benzylsuccinate can either be envisaged starting from toluene and fumarate or from benzoate and succinate. Although the sole natural pathway involving this intermediate, anaerobic toluene degradation, starts with the former reaction, the extreme oxygen sensitivity of benzylsuccinate synthase severely restricts its biotechnological applicability [
12]. In addition, toxicity effects by the required amounts of toluene needed for decent product yields and the relatively high costs for the fumarate cosubstrate pose additional problems for this approach. Therefore, we constructed a pathway for benzylsuccinate synthesis from succinate and benzoate, employing the enzymes ofβ-oxidation of benzylsuccinate in reverse [
22]. Since we have previously purified and characterized all five of these enzymes and found them all principally reversible [
23,
24,
25,
26], we regarded this approach as feasible. The only β-oxidation enzyme causing potential thermodynamic problems is benzylsuccinyl-CoA dehydrogenase (BbsG), because it delivers the electrons to the quinone pool via an electron transfer flavoprotein (ETF) and an ETF:quinone oxidoreductase [
24,
40]. The
in-vitro assays were performed with artificial electron carriers, ferricenium as electron acceptor for the forward and benzyl viologen as electron donor for the reverse reaction [
40]. These reaction conditions have been designed to pull the reaction in the desired direction, but do not represent the natural situation. Moreover, the electron transfer cascades from BbsG to the quinones appear to differ slightly depending on the physiology of the host bacteria: denitrifying species carry only single gene copies in their genomes encoding either the ETF protein or the ETF:quinone oxidoreductase available for interacting with BbsG and transferring the electrons into the ubiquinone pool [
30], while in ferric iron or sulfate-reducing bacteria, multiple copies of ETF proteins and associated ETF:menaquinone oxidoreductases (EMO;
orfX gene products,
Figure 4) are encoded in the operons of β-oxidation enzymes [
39,
44]. The different types of quinones in denitrifying vs. strictly anaerobic bacteria appear to be important, since they have quite different midpoint potentials (-80 mV for menaquinone, +110 mV for ubiquinone [
45]), with menaquinol as thermodynamically more favorable electron donor for the reverse-running pathway. The intended host species
E. coli is known to shift its quinone pool from ubiquinone under aerobic and nitrate-respiratory conditions to menaquinone during fumarate respiration and fermentation [
46]. Because we intended to use the mixed-acid fermentation pathway of
E. coli to produce the cosubstrate succinate from glucose as one of the substrates for benzylsuccinate synthesis, we opted to implement the
bbs operon of
G. metallireducens as source of the β-oxidation genes including the appropriate ETF and EMO (
Figure 4).
The generation of the second substrate for benzylsuccinate synthesis, benzoyl-CoA is of concern, because it is no naturally occurring metabolite of
E. coli. To enable the cells to obtain benzoyl-CoA from benzoate added to the medium, we established two separate synthetic modules for the uptake and activation of benzoate to benzoyl-CoA by combining the genes for the benzoate transporter BenK with those of either a benzoate-CoA ligase or a CoA-transferase. These enzymes are expected to activate benzoate to the CoA-thioester at different energy expense: benzoate-CoA ligase generates AMP, whose regeneration consumes two ATP equivalents, while the CoA-transferase utilizes succinyl-CoA, which is regenerated with consumption of only one ATP equivalent. Notably, the genes for transporter and activating enzymes were only tolerated on a common plasmid in
E. coli when we included additional genes for benzoyl-CoA-consuming enzymes. We tried this either with the
bbsABCD genes, which represent the last two enzymes of the β-oxidation pathway of benzylsuccinate (
Figure 1), or the
bis gene coding for a biphenyl synthase in the rowan tree
Sorbus acuparia, which synthesizes the secondary plant product 3, 5-dihydroxybiphenyl from benzoyl-CoA and three malonyl-CoA [
47,
48] (data not shown). The observation that the presence of additional genes coding for either type of benzoyl-CoA utilizing enzyme allowed the construction of the plasmids corroborates our hypothesis that the introduced metabolic module of a benzoate transporter and activating enzyme into
E.coli depleted the cellular CoA pool. Because we did not observe any negative effects from the presence of the
bbsABCD genes in the plasmids and planned to combine it with the full
bbs operon, we continued to work with these plasmids for the following steps. The presence of double copies of these genes in the production strains also did not cause any apparent problems.
After combining either type of benzoyl-CoA synthetic module with the β-oxidation enzymes from
G. metallireducens, we immediately observed the production of benzylsuccinate in the supernatants of aerobic cultures supplied with succinate and benzoate. However, the concentrations of 0.3 to 1.7 nM obtained in these experiments were very low and close to the detection limit, and the effects of CoA ligase vs. CoA-transferase for benzoate activation appeared to differ between minimal and rich media. After shifting to anaerobic conditions, benzylsuccinate production yields increased strongly, although only benzoate was fed to the medium and succinate needed to be produced as fermentation product from glucose (
Figure 5B). Since the cultures containing the CoA ligase module performed much better in benzylsuccinate production, only they were used for further optimization studies. These included the introduction of a mutant
mscS gene for an unspecific export protein, which increased benzylsuccinate concentration in the supernatant by more than 3-fold under fermentation conditions. Finally, growth under fumarate respiration conditions resulted in a 10-fold increase of benzylsuccinate yield, compared to fermentation conditions. The observed decrease of product yield with fumarate respiration in presence of MscS may be explained by adverse effects of the exporter on maintaining the proton gradient necessary for ATP regeneration via fumarate respiration. In the absence of any refinement procedures such as optimizing the medium composition, incubation time, temperature, pH, or other parameters, we regard the maximum yield of 4.8 µM benzylsuccinate (equals to ca. 1 mg/l) observed in this study as a promising first step to develop a viable process.
Further possible steps to improve the yield of benzylsuccinate produced are clearly necessary. Our initial studies indicate that one of the major bottlenecks is the lack of a proper export system for benzylsuccinate, since the measured intracellular concentrations of benzylsuccinate were more than 10-fold higher than those excreted in the medium. One of the reasons involved in higher productivity under anaerobic conditions may be the induction of C4-dicarbonic acid transporters in
E. coli [
49] which may also take part in benzylsuccinate export. Potentially more dedicated exporter candidates to be evaluated in further optimization attempts may be the products of conserved “solvent stress” operons encoded in the genomes of many anaerobic toluene degraders, one of which is actually co-induced with the
bss and
bbs operons in toluene-degrading
A. aromaticum [
50]. Further improvements may result from using succinate-overproducing strains of
E. coli [
51] which would allow access to much higher substrate concentrations and less unwanted fermentation products formed from glucose, or switching to other naturally succinate-overproducing species like
Basfia succiniproducens [
52].
The observed production of benzylsuccinate under fermentative and fumarate-respiratory conditions may be rationalized by some thermodynamic considerations. Succinate is one of the usual, albeit minor fermentation products of
E. coli [
53], and its production consumes both NADH equivalents generated during glycolysis per fermented glucose. Because the synthesis of succinate deviates branches off from the high-energy intermediate phospho-enol-pyruvate (PEP), only one ATP is conserved from the respective glucose molecule during glycolysis (
Figure 7A). The acetyl-CoA generated from pyruvate by pyruvate-formate lyase (PFL) is converted to acetyl-phosphate which allows for the conservation of a second ATP (
Figure 7A). Concomitantly, PEP is converted to oxaloacetate with the CO
2 generated from formate cleavage via formate:hydrogen lyase, which is converted to succinate via the reductive branch of the citric acid cycle (
Figure 7A). This includes the reaction of fumarate reductase, which establishes a redox loop with NADH:quinone oxidoreductase and conserves the energy difference between the NADH/NAD and the succinate/fumarate redox couples in the form of a proton gradient. The synthetic benzylsuccinate-generating pathway should allow to add further reductive steps to this cascade, starting with succinate, which is activated by the CoA-transferase BbsEF [
23], covalently bound to a benzoyl-CoA cosubstrate and then enters reductive reverse β-oxidation (
Figure 7). To obtain an overview of the thermodynamic feasibility of the proposed pathway, calculations were performed using ΔG
f°’ values of the molecules involved from [
54], except for benzylsuccinate, whose ΔG
f°’ value was calculated as -547 kJ mol
-1 from the results of a QM simulation of the benzylsuccinate synthase reaction [
29]. Using equation (1) we calculated a free enthalpy change of -262 kJ mol
-1 for the formation of acetate, H
2 and succinate from glucose, which occurs during mixed acid fermentation. The value correlates well to the three ATP equivalents (one ATP equal to values of 72 - 80 kJ mol
-1) predicted to be formed during the pathway via glycolysis, acetate kinase and fumarate reductase (
Figure 7A).
If benzylsuccinate formation is considered in a balanced equation with glucose degradation to acetate; H
2 and CO
2, the available energy value increases according to equation (2), but only marginally relative to one glucose molecule. However, the formation of benzylsuccinate as additional fermentation product may allow additional recycling of the released hydrogen or formate molecules from glucose fermentation by coupling either hydrogenase-2 [
55,
56] or formate dehydrogenase-N or -O of
E. coli [
57,
58] with fumarate reductase and EMO. Under these conditions, the energy yield value per glucose can become significantly higher and may approach up to four ATP equivalents per glucose as shown in equation (3). Therefore, benzylsuccinate production may actually be beneficial for anaerobic growth of
E. coli, and the additional costs for benzoate transport and activation should be covered by the additional gain of energy.
Concluding this study, we show that it is possible to use degradative β-oxidation pathways in reverse for biosynthetic purposes. In addition to the
bbs genes used in this study, almost identical operons are known to be involved in the degradation of succinate adducts of other hydrocarbons, such as 2-methylnaphthalene, cresols or xylenes [
12,
59]. In addition, many other natural products are degraded by β-oxidation. Therefore, the reversal of known degradation pathways may be an interesting concept to produce such molecules in an analogous manner as shown here. In recent years, several unrelated β-oxidation pathways have already been used to construct synthetic pathways for easy access to secondary plant compounds or other interesting metabolites [
60]. As a second building block, we established a simple metabolic module for the synthesis of benzoyl-CoA, which does not naturally occur in
E. coli. Similar uptake and activation modules are conceivable for many other substrates, enabling biosynthetic routes for more complicated derivatives without the need to establish a more complex pathway for synthesizing the activated molecule from scratch. Since benzoyl-CoA is used as intermediate in many different biosynthetic pathways, just the two modules described here may be combined with other enzymes to produce a variety of additional target compounds.
4. Materials and Methods
Cultivation of bacteria.
Aromatoleum aromaticum (DSMZ19018) and
Geobacter metallireducens (DSMZ 7210) were grown under denitrfying conditions in minimal media with benzoate as substrate as described previously [
26,
40].
Eschericha coli strains were routinely grown at 37 °C in LB medium or M9 minimal medium [
61], which were supplemented with substates or antibiotics as needed. In oder to induce the added genes, AHT (0.2 mg ml
-1) and IPTG (0.5 mM) were added at OD
578 values of 0.4 to 0.6, and the cells were subsequently incubated at 15 °C. The media used for these experiments were autoinduction medium [
62] (ZYP-5052, VWR life science, Radnor, PA), TGYEP [
63], LB or M9 minimal medium with 10 mM glucose. For producing recombinant enzymes, the induction phase lasted for 16 h, while the benzylsuccinate-producing cultures were incubated for 3 days. Growth was monitored by following the increase in OD
578.
Molecular biological techniques.
Chromosomal DNA was prepared according as described in [
64], plasmids were prepared using the GeneJet kit (Fermentas, St. Leon-Rot, Germany). PCR reactions were performed using the DNA primers listed in
Table A1. DNA fragments were electrophoretically separated in 1% agarose gels in TAE buffer and stained with ethidium bromide. Restriction and ligation assays were performed under standard conditions[
65] as recommended by the suppliers. Plasmids or ligation mixtures were transformed into competent
E. coli cells, which were prepared according to Inoue et al. (1990)[
66]. DNA sequencing was performed by SeqLab (Göttingen, Germany).
Combinatory cloning.
The expression vectors containing multiple genes in form of an artificial operon were produced by combinatory cloning according to the instructions of the Stargate cloning system (IBA, Göttingen, Germany). To this end, the genes of interest were initially amplified by Phusion DNA polymerase (Finnzymes, Espoo, Finland) and cloned into the pEntry donor vector (pE-IBA20), using appropriately engineered recognition sites of the type IIS restriction enzyme LguI in the PCR primers used (
Table A1). After insertion of the DNA fragment, the flanking LguI recognition sites are lost and replaced by Esp3I sites provided by the donor vector. In a second step, the genes are then transferred to the actual expression vectors (e.g. the pASG series) by oriented insertion of the Esp3I-fragments. The expression vectors provide an anhydrotetracyclin-inducible tet promotor and optional N- or C-terminal strep II-affinity tags. For constructing synthetic operons, the Esp3I-fragments containing the genes to be combined were transferred from the original donor vectors into vectors pNFUSE and pCFUSE, respectively. These vectors provide an intergenic region between the genes to be combined, and the genes are again flanked by LguI restriction sites. Cutting the insert out by LguI allows then to construct a new donor vector in pEntry containing the fused genes between Esp3I restriction sites, which can then be transferred to the appropriate expression vector. The same procedure has been repeated to create the multiple fusion constructs in the xpression plasmids pLigBen, pTtansBen and pLigBenEx (
Figure 4).
Cloning of the bbs operon.
Using a Long-Range PCR method with KOD Hot Start DNA polymerase (biotechrabbit, Berlin, Germany), the genes of the entire
bbs operon of
G. metallireducens as well as the broad-host-range vector pBBR2 [
42] were amplified and ligated together, producing an expression plasmid of 16.3 kb containing the
bbs operon behind an IPTG-inducible
lac promotor (pBeta, see
Figure 4).
Enzyme purification.
To obtain recombinant enzymes, cultures of 2 l of E. coli Rosetta (DE3) pLysS containing either the N-terminally strep-tagged bclA or bct gene on an AHT inducible plasmid were grown to an OD578 of 0.5, induced by adding AHT and incubated for further 16 h at 15 °C. The cells were harvested by centrifugation, suspended in 30 ml buffer A (10 mM Tris/HCl pH 8, 2 mM MgCl2, 2 mM dithiothreitol) and lysed by passage through a French Press cell. In case of benzoate-CoA ligase, the cell extract was then subjected to a fractionated ammonium sulfate precipitation to obtain the fraction precipitating between 33%, and 60% saturation. The precipitate was retrieved by centrifugation, resuspended in buffer A and desalted by a passage through a PD10 column (6 ml; GE Helthcare, Freiburg, Germany) using buffer A. Finally, the protein was applied to a UnoQ sepharose column (BioRad, München, Germany) and eluted by a gradient of 50-500 mM KCl in buffer A over 20 column volumes. The fractions were collected and tested for benzoate-CoA ligase activity. Succinyl-CoA:benzoate CoA-transferase. The CoA-transferase was purified from the extract in one step, using affinity chromatography on a 5ml streptactin column as indicated by the supllier (IBA, Göttingen, Germany).
Enzyme activity assays.
The activity of benzoate CoA ligase was determined by a coupled photometric assay as described previously, coupling the production of AMP from ATP to the oxidation of 2 NADH via added myokinase, pyruvate kinase, phospho-
enol-pyruvate, and lactate dehydrogenase [
34,
67]. Succinyl-CoA:benzoate CoA-transferase activity was measured using the HPLC-based detection of the respective thioesters. To this end, 30 µg enzyme was incubated for 10 min at 30 °C in 200 µl of buffer B (50 mM MES pH 6.2, 5 mM MgCl
2) with 1 mM benzoate and 250 mM succinyl-CoA. The reaction was stopped by adding 20 µl of a 2 M NaHSO
4 solution and incubation on ice. After removing the precipitated proteins by centrifugation, the supernatants were analysed by HPLC, using an RP-18 column (Varian Microsorb 100-5; 150X4.6 mm) which was developed over 20 min at a flow rate of 1 ml min
-1 and a gradient of 3-20 % acetonitrile in 50 mM MES buffer (pH 6.2). CoA thioesters were detected by their absorption at 260 nm via a diode array detector. The retention times of succinyl-CoA and benzoyl-CoA standards were at 2 and 10 min, respectively.
Extraction and detection of benzylsuccinate.
Detection and quantitation of produced benzylsuccinate was acchieved by HPLC-MS analytics. To this end, the induced cultures were separated into cell mass and supernatants by centrifugation. Subsequently, either the supernatants or both fractions (as well as the benzylsuccinate standard solutions) were spiked with known amounts of phenylsuccinate as internal standard. The cell pellets were washed by suspending and re-centrifuging them in 1 ml 100 mM Tris-HCl buffer (pH 7.5), then they were resuspended in 900 µl water containing 100 µM phenylsuccinate, acidified to pH 2 by adding 100 µl trifluoroacetic acid (TFA) and heated to 60 °C for 10 min. The supernatants and the standard solutions were likewise spiked with phenylsuccinate (at 2µM, which should be concentrated to 100 µM after extraction) and acidified with TFA. The organic acids from the acidified supernatants and cell pellet fractions were then extracted twice with equal volumes of ethyl acetate (50 ml for supernatants, 1 ml for cell pellets). After combining the organic phases, the solvent was evaporated and the residues were solved in 20% acetonitrile containing 0.1 % TFA. These samples as well as the benzylsuccinate standards spiked with phenylsuccinate were then separated by isocratic HPLC-MS runs over an RP-18 column (3 µm, 150x4.6 mm), using 20% acetonitrile/0.1 % TFA as solvent at a flow rate of 0.5 ml min
-1 on a 1100 HPLC system (Agilent). Mass spectrometric detection was achieved by coupling a LTQ-FT Ultra FT-ICR mass spectrometer (ThermoFisher Scientific) to the outlet of the HPLC column. Masses were measured in negative ion mode. Extracted ion chromatograms of benzylsuccinate ([M-H]
- = 207.0665 m/z) and phenylsuccinate ( [M-H]
- = 193.0507 m/z) were generated and the corresponding signals were quantified by integration. Benzylsuccinate showed a retention time of 17.2 min, phenylsuccinate of 19.8 min (
Figure A3). The internal standard Phenylsuccinate was used for normalization of the different extractions and HPLC-MS runs. Benzylsuccinate concentrations were normalised based on the recorded phenylsuccinate standards and converted to the supernatant and cytoplasmic values based on the concentrating factor from the extraction procedures and a volume (dry cell mass)
-1 ratio of 1 ml (0.4 g dry mass)-1 [
68].
Other techiques. Protein concentrations were determined by the Coomassie-binding assay using bovine serum albumin as standard [
69], and proteins were visualised by SDS-polyacrylamide gel electrophoresis using gels with 10-12% polyacrylamide concentrations, which were stained with coomassie brilliant blue R-250 [
70].
Figure 1.
Pathway of anaerobic toluene degradation. Enzymes involved are benzylsuccinate synthase (BssABC), benzylsuccinate CoA-transferase (BbsEF), benzylsuccinyl-CoA dehydrogenase (BbsG), benzylidenesuccinyl-CoA hydratase (BbsH), (α-hydroxybenzyl)succinyl-CoA dehydrogenase (BbsCD), and benzoylsuccinyl-CoA thiolase (BbsAB). The intermediates and their known or inferred stereochemical conformations are (R)-benzylsuccinate (1), (R)-2-benzylsuccinyl-CoA (2), (E)-2-benzylidenesuccinyl-CoA (3), (S,R)-2-(α-hydroxybenzyl)succinyl-CoA (4), and (S)-2-benzoylsuccinyl-CoA.
Figure 1.
Pathway of anaerobic toluene degradation. Enzymes involved are benzylsuccinate synthase (BssABC), benzylsuccinate CoA-transferase (BbsEF), benzylsuccinyl-CoA dehydrogenase (BbsG), benzylidenesuccinyl-CoA hydratase (BbsH), (α-hydroxybenzyl)succinyl-CoA dehydrogenase (BbsCD), and benzoylsuccinyl-CoA thiolase (BbsAB). The intermediates and their known or inferred stereochemical conformations are (R)-benzylsuccinate (1), (R)-2-benzylsuccinyl-CoA (2), (E)-2-benzylidenesuccinyl-CoA (3), (S,R)-2-(α-hydroxybenzyl)succinyl-CoA (4), and (S)-2-benzoylsuccinyl-CoA.
Figure 2.
A. Growth curves of E.coli Rosetta(DE3) pLysS containing expression plasmid pASG_mod-benK in LB medium with different added benzoate concentrations (0, 1, 2.5, 5 and 10 mM in red, orange, green, blue and purple). Gene induction was started 3 h after inoculation. The growth curve of the same strain without a plasmid in LB medium with 5 mM benzoate is shown (open black circles). B: Growth rates dependence of E. coli containing or lacking the benK gene from added benzoate (magenta and blue, respectively).
Figure 2.
A. Growth curves of E.coli Rosetta(DE3) pLysS containing expression plasmid pASG_mod-benK in LB medium with different added benzoate concentrations (0, 1, 2.5, 5 and 10 mM in red, orange, green, blue and purple). Gene induction was started 3 h after inoculation. The growth curve of the same strain without a plasmid in LB medium with 5 mM benzoate is shown (open black circles). B: Growth rates dependence of E. coli containing or lacking the benK gene from added benzoate (magenta and blue, respectively).
Figure 3.
Activity assessment of succinyl-CoA:benzoate CoA-transferase by HPLC analysis. Chromatograms: control without added enzyme (black), full assay at 0 (blue) and 10 min of incubation (purple), succinyl-CoA standard (1 mM; orange), benzoyl-CoA standard (1 mM, green).
Figure 3.
Activity assessment of succinyl-CoA:benzoate CoA-transferase by HPLC analysis. Chromatograms: control without added enzyme (black), full assay at 0 (blue) and 10 min of incubation (purple), succinyl-CoA standard (1 mM; orange), benzoyl-CoA standard (1 mM, green).
Figure 4.
Expression plasmids constructed for benzylsuccinate production. Both pLigBen (A) and pTransBen (B) contain a ColE1 replication origin, while pBeta (C) contains a broad range pBBR origin. Plasmid pLigBenEx was constructed by adding a mutant mscS gene as indicated.
Figure 4.
Expression plasmids constructed for benzylsuccinate production. Both pLigBen (A) and pTransBen (B) contain a ColE1 replication origin, while pBeta (C) contains a broad range pBBR origin. Plasmid pLigBenEx was constructed by adding a mutant mscS gene as indicated.
Figure 5.
Benzylsuccinate yields in the culture supernatants of cells carrying plasmid pBeta and either pLigBen or pTtansBen after three days incubation at 15 °C in rich (orange) and minimal media (yellow). A. Experiments under aerobic conditions with added succinate and benzoate. Results of control experiments without the plasmids or without added benzoate are included. B. Experiments under anaerobic conditions with added glucose and benzoate. The experiment from (A) yielding the most product under aerobic conditions is added to illustrate the different scales of the graphs.
Figure 5.
Benzylsuccinate yields in the culture supernatants of cells carrying plasmid pBeta and either pLigBen or pTtansBen after three days incubation at 15 °C in rich (orange) and minimal media (yellow). A. Experiments under aerobic conditions with added succinate and benzoate. Results of control experiments without the plasmids or without added benzoate are included. B. Experiments under anaerobic conditions with added glucose and benzoate. The experiment from (A) yielding the most product under aerobic conditions is added to illustrate the different scales of the graphs.
Figure 6.
Benzylsuccinate yields of cells carrying plasmids pBeta and pLigBen after anaerobic incubation for three days at 15 °C in minimal media. The addition of an MscS exporter is indicated by shifting from yellow to brown columns, fumarate-respiring cultures are indicated by hatching. A. Product concentrations in culture supernatants. B. Intracellular product concentrations.
Figure 6.
Benzylsuccinate yields of cells carrying plasmids pBeta and pLigBen after anaerobic incubation for three days at 15 °C in minimal media. The addition of an MscS exporter is indicated by shifting from yellow to brown columns, fumarate-respiring cultures are indicated by hatching. A. Product concentrations in culture supernatants. B. Intracellular product concentrations.
Figure 7.
Representation of the expanded benzylsuccinate-producing fermentation pathway. A. Scheme of the acetate- and succinate-forming branches of mixed acid fermentation including the added module for benzylsuccinate formation. Possible ATP regeneration sites are indicated. B. Detailed scheme of the synthetic pathway of benzyol-CoA-producing and β-oxidation modules involved in benzylsuccinate synthesis.
Figure 7.
Representation of the expanded benzylsuccinate-producing fermentation pathway. A. Scheme of the acetate- and succinate-forming branches of mixed acid fermentation including the added module for benzylsuccinate formation. Possible ATP regeneration sites are indicated. B. Detailed scheme of the synthetic pathway of benzyol-CoA-producing and β-oxidation modules involved in benzylsuccinate synthesis.
Table 1.
Purification of recombinant benzoate-CoA ligase.
Table 1.
Purification of recombinant benzoate-CoA ligase.
Purification step |
Volume (ml) |
Protein (mg) |
Activity (U) |
Specific activity (U mg-1) |
Yield |
Enrichment |
Cell extract |
12 |
365 |
2412 |
6.6 |
100% |
1 |
(NH4)2SO4-precipitation (33-60 % saturation) |
2.5 |
80 |
1593 |
20 |
66% |
3 |
PD10 fraction |
2.0 |
58 |
1124 |
19 |
47% |
3 |
UnoQ fraction |
3.0 |
2.6 |
274 |
107 |
11% |
16 |