- Original article
- Open Access
Simultaneous production of isopropanol, butanol, ethanol and 2,3-butanediol by Clostridium acetobutylicum ATCC 824 engineered strains
© Collas et al.; licensee Springer. 2012
Received: 2 July 2012
Accepted: 6 July 2012
Published: 21 August 2012
Isopropanol represents a widely-used commercial alcohol which is currently produced from petroleum. In nature, isopropanol is excreted by some strains of Clostridium beijerinckii, simultaneously with butanol and ethanol during the isopropanol butanol ethanol (IBE) fermentation. In order to increase isopropanol production, the gene encoding the secondary-alcohol dehydrogenase enzyme from C. beijerinckii NRRL B593 (adh) which catalyzes the reduction of acetone to isopropanol, was cloned into the acetone, butanol and ethanol (ABE)-producing strain C. acetobutylicum ATCC 824. The transformants showed high capacity for conversion of acetone into isopropanol (> 95%). To increase isopropanol production levels in ATCC 824, polycistronic transcription units containing, in addition to the adh gene, homologous genes of the acetoacetate decarboxylase (adc), and/or the acetoacetyl-CoA:acetate/butyrate:CoA transferase subunits A and B (ctfA and ctfB) were constructed and introduced into the wild-type strain. Combined overexpression of the ctfA and ctfB genes resulted in enhanced solvent production. In non-pH-controlled batch cultures, the total solvents excreted by the transformant overexpressing the adh, ctfA, ctfB and adc genes were 24.4 g/L IBE (including 8.8 g/L isopropanol), while the control strain harbouring an empty plasmid produced only 20.2 g/L ABE (including 7.6 g/L acetone). The overexpression of the adc gene had limited effect on IBE production. Interestingly, all transformants with the adh gene converted acetoin (a minor fermentation product) into 2,3-butanediol, highlighting the wide metabolic versatility of solvent-producing Clostridia.
The limited supply and the negative environmental effects of the use of petroleum-derived fuels and chemicals have stimulated efforts for the development of more environmentally-friendly processes. In this respect, the fermentation of carbohydrates into acetone, butanol and ethanol (ABE) or isopropanol, butanol and ethanol (IBE) is a promising way for the production of green chemicals and fuels. In the past, both ABE and IBE fermentations were performed worldwide at industrial scale until they were replaced by petrochemical processes (Jones and Woods1986; Rogers et al.2006). Many resources are currently being devoted to develop economically-viable fermentation processes based primarly on lignocellulosic biomass hydrolysates as substrates (Dürre20072008; López-Contreras et al.2010; Green2011).
For fuel applications, the IBE mixture appears to be more attractive than the ABE one. Isopropanol shows a higher energy density than acetone (23.9 MJ/L vs 22.6 MJ/L) and this mixture has already been used as an additive for gasoline or diesel oil (Peralta-Yahya and Keasling2010). Isopropanol can be catalytically condensed into di-isopropyl ether (DIPE) (Logsdon and Loke2000). DIPE displays good fuel properties and could substitute methyl tert-butyl ether (MTBE) as isooctane index enhancer in gasoline composition (Huang and Sorensen1990). Another important potential application of biologically-produced isopropanol is as a precursor for green propylene, which is the second most important chemical intermediate in the petrochemical industry after ethylene. Propylene is used in many chemical reactions for the synthesis of a wide variety of products, including plastic materials.
The clostridial species that produce neutral solvents (ABE or IBE) are strictly anaerobes, rod-shaped and spore-forming bacteria. Most of them, such as C. acetobutylicum ATCC 824, produce ABE but some others, such as C. beijerinckii NRRL B593, excrete IBE (George et al.1983; Chen and Hiu1986). ABE and IBE batch fermentations are similar, displaying a biphasic kinetic pattern (Jones and Woods1986; Girbal and Soucaille1998). After production of acetic and butyric acids in exponential growth, fermentation switches to formation of neutral solvents shortly before entering stationary phase. In the IBE fermentation, depending on the strain and the cultivation conditions, residual acetone may also be an end-product (Ismaiel et al.1993).
In C. beijerinckii NRRL B593, the reduction of acetone into isopropanol is catalyzed by a NADPH-dependent secondary-alcohol dehydrogenase (s-Adh), which has been extensively characterized (Yan et al.1988; Ismaiel et al.1993; Korkhin et al.1998; Goihberg et al.2010). Although the s-Adh was clearly distinct from clostridial primary-alcohol dehydrogenases (Chen1995) that reduce butyraldehyde into butanol, the s-Adh showed activity on both primary and secondary alcohols, with a preference for secondary ones (Ismaiel et al.1993). Kinetic studies confirmed that the physiological substrate was acetone.
Metabolic engineering has been used to create pathways for isopropanol production in Escherichia coli. Introduction of four genes from C. acetobutylicum (ctfA, ctfB, adc and thiolase (thl)) into E. coli generated a strain capable of producing acetone (Bermejo et al.1998). By introduction of the C. beijerinckii adh gene in combination with the aforementioned genes, isopropanol excretion by E. coli was achieved up to the concentrations of 4.9 g/L (Hanai et al.2007) and 13 g/L (Jojima et al.2008). The engineered E. coli strains surpassed the best reported wild-type clostridial strains, C. beijerinckii and C. isopropylicum, excreting approximately 4 g/L isopropanol (Groot and Luyben1986; Matsumura et al.1992). A major advantage of the engineered E. coli strains was the lack of important competing pathways for by-products. Recently, the adh gene from C. beijerinckii was cloned into the ABE-producing strain C. acetobutylicum ATCC 824. The resulting transformants excreted 6.1 g/L isopropanol and a minor amount of acetone (Lee et al.2012).
In the present study, different IBE-producing transformants of C. acetobutylicum that showed high isopropanol excretion capacities have been constructed. The fermentation performances of the transformants were characterized in batch cultures using laboratory-scale bioreactors with or without pH-control and compared to those of the wild-type IBE or ABE- producing strains. In addition, formation of 2,3-butanediol by C. acetobutylicum transformant strains harbouring the adh gene was described and characterized for the first time.
Materials and methods
Strains and cultivation conditions
Strains and plasmids used in this study
Strain or plasmid
E. coli XL1 blue
Cloning and plasmid maintenance
E. coli DH10B(pAN2)
E. coli BW 25113
Ipa operons expression
C. beijerinckii NRRL B593
Wild type, Isopropanol natural producer
C. acetobutylicum ATCC824
(Jones and Woods 1986 )
Empty vector (ermB R /amp R )
(Oultram et al. 1988 )
thlp_[adh; ctfA; ctfB]
thlp_[adh; adc; ctfA; ctfB]
thlp_[thl], kan R
Clostridial wild-type and transformants were stored as spore suspensions at −20°C in 15% (v/v) glycerol. Prior to the inoculation of pre-cultures, each spore suspension (500 μL) was heat-shocked in a water bath for 10 min at 70°C (C. acetobutylicum ATCC 824 and its transformants) or 1 min at 100°C (C. beijerinckii NRRL B593). Culture media for Clostridia were made anaerobic by sparging with nitrogen gas. Cultures and pre-cultures were performed in CM1 medium (Kuit et al.2012) which contains, per liter: yeast extract, 5.0 g; KH2PO4, 1.0 g; K2HPO4, 0.76 g; ammonium acetate, 3.0 g; p-aminobenzoic acid, 0.10 g; MgSO4·7 H2O, 1.0 g; and FeSO4·7 H2O, 0.5 g, glucose, 90 g. Pre-cultures of C. beijerinckii were grown in medium containing 60 g/L glucose.
Batch fermentations were carried out anaerobically in 2-L (1-L working volume) Applikon glass bioreactors (Applikon, The Netherlands) using CM1 medium. When needed, pH was maintained at 5.0 by automatic addition of 4 M KOH solution. Static flask fermentations were carried out anaerobically in 120 mL serum bottles with 50 mL of CM1 medium.
For the preparation of clostridial competent cells, cells were grown on CG medium (Roos et al.1985), as described previously (Oultram et al.1988). When required, culture media were supplemented with ampicillin (100 μg/mL), chloramphenicol (30 μg/mL), erythromycin (50 μg/mL or 30 μg/mL for liquid cultures and plates, respectively).
Microbial growth was monitored by optical density measurements at 600 nm (Pharmacia Biotech Ultrospec 2000).
Plasmid construction and transformation
Oligonucleotides used for the plasmid constructions
CAACTACTCGAGA TAATTTTTCT AG AGAATTTAAAAGGAGG GATTAAAATG
AATGGTACTAG TTATTTTTTGTCG AC TGTTTCATAGTATTTC TTTCTAAACAGCC
AAACAACTC GA GTTATAATC TAG ATATAAATAAATAGGA CTAGAGG CG
AAAAATACT AGTTACCATTTAAGTC GACTCTTATTTTTATTA CTTAAG
The constructs used for the C. acetobutylicum transformation were based on the E. coli/Clostridium shuttle vector pMTL500E (Table1). The thiolase promoter was PCR-amplified from genomic-DNA of C. acetobutylicum ATCC 824 using thlp_for and thlp_rev oligonucleotides and digested by Apa I and Sph I. The adh gene was PCR-amplified from C. beijerinckii NRRL B593 genomic-DNA using adh_for and adh_rev oligonucleotides and digested by Apa I and Xho I. The thl promoter and adh gene sequences were simultaneously cloned into pMTL500E plasmid (digested by Sph I and Xho I) to yield pFC002 construct. Genes from C. acetobutylicum ATCC 824 were amplified by PCR on genomic DNA using adc_for and adc_rev oligonucleotides for adc, ctfAB_for and ctfAB_rev oligonucleotides for ctfA and ctfB. PCR amplifications of adc gene and ctfA_ctfB genes were digested by Xho I and Spe I restriction enzymes and cloned into pFC002 digested Xho I and Xba I to yield pFC005 and pFC006, respectively. PCR amplification of adc gene was subsequently cloned into pFC006 digested Xho I and Xba I to yield pFC007.
Plasmid DNA constructs were introduced into chemically competent E. coli DH10B harbouring pAN2 (Oultram et al.2007) for methylation prior to transformation into C. acetobutylicum as described earlier (Mermelstein and Papoutsakis1993). Correct methylation was checked by restriction analysis with Fnu 4HI. Methylated pFC002, pFC005, pFC006, pFC007 and methylated pMTL500E plasmids (Table1) were electroporated into C. acetobutylicum ATCC 824 as described by Oultram et al (Oultram et al.1988). Erythromycin-resistant colonies were cultivated in CGM liquid medium and total DNA was extracted as described above. The presence of the respective construct in the transformants obtained was confirmed by PCR on DNA extracted from the different colonies using specific oligonucleotides for the specific inserts. Transformant strains harbouring the right construct were found for all constructs (results not shown). Transformant strains were stored as spore suspensions and kept at −20°C.
The thiolase transcription unit was amplified from C. acetobutylicum genomic DNA using oligonucleotides thlp_for and thlp_rev (Table2). The amplificate was cloned into pCR blunt II Topo (Invitrogen) to yield pTHL. The plasmid pTHL was cotransformed with pFC002, pFC005, pFC006, pFC007 or pMTL500E in chimiocompetent E. coli BW25113.
Reduction of ketones by cell-free extracts
For preparation of cell-free extracts (CFEs) for enzymatic assays, C. acetobutylicum transformants and C. beijerinckii wild type strains were grown anaerobically in 100 mL of CM1 medium with 60 g/L glucose. After 15–20 h of culture, cells were harvested at 4°C by centrifugation at 15,000 g for 7 min (OD600: 1.5-2.0). Pellets were suspended in 20 mL of 50 mM sodium-HEPES buffer (pH 8.5) containing DTT (0.2 mM) and a set of protease inhibitors (Complete; Mini, Roche, 1 tablet in 50 mL) and washed twice. Pellets were then suspended in 3 mL of 50 mM sodium-HEPES buffer. Cell suspensions were frozen in liquid nitrogen and stored overnight at −80°C in anaerobic conditions. Cell suspensions were then slowly thawed, loaded in a French Press (Thermo Electron Corporation) and homogenized by two passes at 16,000 psi. When used, CFEs were kept on ice. Protein content in the CFEs was determined by the Bradford method (Biorad) with BSA as standard.
Reduction of acetone or racemic acetoin (D/L 3-hydroxy-2-butanone, Fluka) by s-Adh was carried out at 37°C in 50 mM of Tris buffer (pH 7.5) with 0.2 mM of NADPH and 50 mM of substrate. NADPH decrease was monitored by absorbance decrease at 340 nm using a Safire spectrophotometer (Tecan).
Samples taken during fermentation were centrifuged at 20,000 g for 5 min and supernatants were stored at −20°C. Metabolite concentrations (sugars, organic acids, solvents and 2,3-butanediol) were determined by HPLC as previously described (Gosselink et al.1995; Siemerink et al.2011). A solution of 4-methyl valeric acid (Sigma-Aldrich) at 30 mM was used as an internal standard.
Construction of expression vectors
The well-studied ABE-producing strain C. acetobutylicum ATCC 824 was engineered to be an IBE producer. For this purpose, the coding sequence of the adh gene from C. beijerinckii NRRL B593 was cloned downstream of the promoter sequence of the thiolase gene (thl) from C. acetobutylicum ATCC 824 to form pFC002 plasmid (Table1). The promoter sequence of the thiolase gene was chosen in order to maximize expression of the adh gene, since the thiolase gene of C. acetobutylicum was reported to be constitutively expressed (Hartmanis and Gatenbeck1984; Tummala et al.1999; Alsaker and Papoutsakis2005). To up-regulate the acetone pathway in the host organism, genes encoding the enzymes active in acetoacetyl-CoA to acetone conversion i.e. acetoacetate decarboxylase (adc) and acetoacetyl-CoA : acetate/butyrate:CoA transferase subunits A and B (ctfA and ctfB) were cloned into pFC002, downstream of the adh gene, resulting in the construct pFC007 (Table1). Genes adc, ctfA and ctfB were expressed under the control of the thl-promoter. The role of each gene over expressed in pFC007 was subsequently assessed by constructing different combinations of adh, adc, ctfA and ctfB genes. The plasmid pFC005 contained adh and adc genes and pFC006 contained adh, ctfA and ctfB genes (Table1).
Expression of isopropanol pathway genes in E. coli
Effect of expression of the adh gene on the product pool of C. acetobutylicum
Performance of C. acetobutylicum ATCC 824 and its transformants in 45‐h cultures performed with pH regulation at 5.0
C. beijerinckii 2 NRRL B5932
C. acetobutylicum ATCC 824
Glucose consumed [g/L]
Acetic acid 1 [g/L]
Butyric acid [g/L]
2,3-Butanediol ( D or L ) [g/L]
Final solvents [g/L]
Final solvent yield [g A/IBE /g glc. ]
Productivity after 30 h [g/L h]
Carbone recovery [%]
Reduction activities of acetone and acetoin measured in cell-free extracts of C. beijerinckii NRRL B593 and C. acetobutylicum ATCC 824 transformants harbouring pMTL500E, pFC002 and pFC007
Specific activity[μmol/min mgprotein]
Early isopropanol production in static flask culture
As the constitutive promoter of the thlgene was used to control gene expression (Tummala et al.1999), the isopropanol production by ATCC 824(pFC007) was expected to start concomitantly with the production of butyric acid. Product excretion in the first hours of fermentation was studied in static flask fermentations. Butyric acid was detected prior to any solvent in all cultures of ATCC 824 transformants. The transformants expressing ctfA and ctfB genes i.e. harbouring pFC006 and pFC007 excreted isopropanol earlier than the wild type strain or other transformants (data not shown) and prior to any other solvent.
Kinetics of IBE production by C. acetobutylicum transformants
The fermentation kinetics of ATCC 824 transformants were first investigated using a pH set-point of 5.0. The fermentation profile and performances of the control strain ATCC 824(pMTL500E) were similar to those of C. acetobutylicum ATCC 824 WT in the first 45 h of fermentation (Table3). The expression of only the adh gene in ATCC 824(pFC002) resulted in lower solvent production (15.1 g/L IBE of which 4.8 g/L isopropanol) than ATCC 824(pMTL500E) without the adh gene. Moreover, the productivity of ATCC 824(pFC002) at 30 h was 25% lower than that of ATCC 824(pMTL500E). In comparison to ATCC 824(pFC002), the wild-type IBE-producer C. beijerinckii NRRL B593 excreted less IBE (13.2 g/L of which 4.5 g/L isopropanol), but reassimilated more efficiently the acids previously excreted. Thus NRRL B593 displayed higher solvent yield (0.36 gIBE/gglc for NRRL B593 vs 0.29-0.30 gIBE/gglc for ATCC 824(pFC002)).
Cultures of ATCC 824(pFC005) and ATCC 824(pFC006) were performed to evaluate the contribution of each gene to the improvement of the ATCC 824(pFC007) phenotype (Table3). Both strains produced more IBE than ATCC 824(pFC002). The combined overexpression of the ctfA and ctfB genes along with expression of adh conferred to ATCC 824(pFC006) a fermentation profile similar to that of ATCC 824(pFC007) (Table3). The final concentration of acids in the ATCC 824(pFC006) culture was slightly lower than that of ATCC 824(pFC002). As with ATCC 824(pFC007), fermentations with ATCC 824(pFC006) stopped 10–15 hours earlier than with the other transformants (Figure2). The resulting solvent productivity after 30 h (0.62 g/L h) was 2.0 times higher than ATCC 824(pFC002). In ATCC 824(pFC005), the overexpression of adc along with expression of adh gene had a more pronounced effect on the production of isopropanol (+27%) than on the production of butanol (+7%) when compared with ATCC 824(pFC002). The fermentation performances of ATCC 824(pFC005) were lower than those of ATCC 824(pFC006) or ATCC 824(pFC007) and no shortening of the fermentation period was observed. Besides, ATCC 824(pFC005), ATCC 824(pFC006) and ATCC 824(pFC007) exhibited the same solvent yield than ATCC 824(pFC002), ATCC 824(pMTL500E) and the WT.
Effect of pH control
Performance of C. acetobutylicum ATCC 824 and its transformants in 45‐h cultures performed without pH regulation
C. acetobutylicum ATCC 824
Glucose consumed [g/L]
Acetic acid * [g/L]
Butyric acid [g/L]
2,3-Butanediol ( D or L ) [g/L]
Final solvents [g/L]
Final solvent yield [g A/IBE / g glc. ]
Productivity after 30 h [g/L h]
Carbone recovery [%]
In the latest developments related to the ABE fermentation process, acetone was considered to be indesirable co-product, whereas butanol is the main product of interest. Over the past few decades, various strategies have been developed to decrease the production of acetone and increase the production of butanol (Nair et al.1994; Nair and Papoutsakis1994; Harris et al.2000; Sillers et al.2008; Jiang et al.2009; Sillers et al.2009; Han et al.2011). The intracellular conversion of acetone into isopropanol was an attractive alternative to avoid acetone excretion and produce a valuable alcohol. The C. beijerinckii NRRL B593 strain reduced acetone naturally thanks to a secondary-alcohol dehydrogenase (s-Adh) but the final titres of solvents by the NRRL B593 (George et al.1983; Survase et al.2011) were lower than those of the best ABE producers (Monot et al.1982; Qureshi and Blaschek1999).
In this study, we have constructed four plasmids harbouring the adh gene from C. beijerinckii NRRL B593 and the genes from C. acetobutylicum ATCC 824 that are part of the metabolic pathway from acetoacetyl-CoA to acetone. The cloned genes were successfully expressed in both E. coli BW25113 and C. acetobutylicum ATCC 824. In E. coli, the expression of ctfA and ctfB along with adh and thl genes allowed for the production of isopropanol. The lack of the adc gene did not prevent the decarboxylation of acetoacetate by E. coli harbouring pFC006, probably because of the instability of the molecule in acidic conditions (Hay and Bond1967). The final concentration of isopropanol in cultures of E. coli strains expressing ctfA and ctfB genes (pTHL and pFC006 or pTHL and pFC007) was lower than those previously reported by other groups (Hanai et al.2007; Atsumi and Liao2008; Jojima et al.2008; Yoshino et al.2008). In our study, E. coli cultures were not optimised, but carried out with the purpose of checking the validity of each construct.
The plasmids were electroporated in C. acetobutylicum ATCC 824. The expression of adh gene allowed transformants to reduce natively produced acetoin and acetone to 2,3-BD and isopropanol, respectively. Either the D or L forms of 2,3-BD or a combination of both but no meso-2,3-BD was produced. The achiral HPLC used in the present study did not differentiate between the D and L enantiomers. Since the activity of s-Adh on acetoin had never been described, this result extends the range of substrates known for this enzyme (Ismaiel et al.1993). Recently, the production of 2,3-BD by C. acetobutylicum transformants expressing an acetoin reductase (acr) from C. beijerinckii NCIMB 8052 was reported (Siemerink et al.2011). The resulting strains also produced 2,3-BD but did not produced isopropanol. For future applications, the production of 2,3-BD by ATCC 824 transformants is still very far from that of Klebsiella pneumoniae (up to 150 g/L of 2,3-BD) (Ma et al.2009).
Each transformant of ATCC 824 was characterised in a batch culture either with pH regulation at 5.0 or without pH regulation. All transformants of ATCC 824 and the wild type displayed higher solvent production levels when grown without pH-regulation. The solvent yield based on glucose consumption did not depend on the genetic modifications, but rather on the culture conditions (pH control or not). Acid assimilation was improved in the cultures without pH regulation, as also suggested by the increase of the C3 compound (acetone or isopropanol) productions. When the pH was not regulated, the pH value of the culture dropped below 5.0, increasing the concentrations of the protonated form of the acids. This has been associated with the onset of solventogenesis (Monot et al.1984; Hüsemann and Papoutsakis1988). Therefore, the high level of protonated acid forms in pH not-regulated cultures of ATCC 824 transformants might trigger solventogenesis at a lower concentration of total acids (protonated plus ionized) and drive more the carbon flux towards butanol or ethanol formation.
The expression of only the adh gene lowered total solvent production by ATCC 824(pFC002) compared to the wild type and the transformant harbouring the empty vector (pMTL500E). The lower solvent excretion by ATCC 824(pFC002) could be explained by the higher toxicity of isopropanol compared to acetone, as suggested by the octane/water partition coefficients (logKow) values i.e. 0.05 for isopropanol and −0.25 for acetone (Yaws and Sachin1999). The logKow was reported to be a good estimation for solvent toxicity (Vermue et al.1993; Heipieper et al.1994), high logKow compounds are generally more toxic than compounds with lower value. It has to be noted that the final IBE concentration of ATCC 824(pFC002) cultures (16 g/L) was still higher than that of NRRL B593 cultures (13 g/L) suggesting that the solvent sensitivity is a strain-dependent characteristic.
Under all culture conditions tested, the overexpression of all genes encoding enzymes of the acetone route (ctfA, ctfB and adc), along with expression of adh gene, conferred to ATCC 824(pFC007) high solvent production rate and high final solvent titres. The use of thl promoter to control the expression of ctfA and ctfB genes initiated excretion of isopropanol before those of other solvents. Recently, (Lee et al.2012) have developed a transformant comparable with ATCC 824(pFC007) in which expression of isopropanol pathway genes were controlled by two adc promoters. In batch culture with pH regulation at 5.0, the maximal end-concentration of IBE was only 17.1 g/L of which 6.1 g/L was isopropanol. The difference in solvent productions observed in the two studies might result from the culture mode applied. Fed-batch with gas stripping was used and was found to improve IBE production by 35.6 g/L (Lee et al.2012) but this type of process has never been scaled up.
The role of each gene involved in the pathway from acetoacetyl-CoA to acetone in the enhancement of ATCC 824(pFC007) fermentation performances was clarified by expressing two derivative plasmids. The overexpression of the ctfA and ctfB genes increased both the speed and the extent of acid assimilation while the overexpression of the adc gene had a little effect (Table3).
This result indicates that decarboxylation of acetoacetate is not the real bottleneck. In a previous study on ABE production by ATCC 824, the overexpression of ctfA, ctfB and adc genes controlled by the adc promoter was studied at pH 5.5 (Mermelstein et al.1993). As with our results, the combined overexpression of ctfA, ctfB and adc increased the solvent production by transformants, whereas expression of adc gene alone had little effect. Unlike our results, the combined expression of ctfA and ctfB genes without adc was found to have a limited effect. Therefore, the impact of ctfA and ctfB overexpression observed in our study might have been supported by the chemically acid-calalysed decarboxylation of acetoacetate (Hay and Bond1967).
The expression of ctfA and ctfB genes along with the adh gene in C. acetobutylicum appears to be a promising way for constructing efficient isopropanol/ethanol producers. The transformants in the present study produce the highest total IBE concentration reported for clostridial batch cultures without online IBE removal (24.4 g /L). As the IBE alcohol mix is considered to be a valuable fuel additive, the transformants obtained represent a step forward towards the development of an industrial IBE process for the production of biofuels.
This work was supported by the program EnerBio of the French Tuck foundation. The authors wish to thank Ms Hetty van der Wal, Ms Miriam Budde for their assistance in fermentation work and Rachel Licht for her critical reading of the manuscript and improvement of the English.
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