Simultaneous production of isopropanol, butanol, ethanol and 2,3-butanediol by Clostridium acetobutylicum ATCC 824 engineered strains

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.


Introduction
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 Woods 1986;Rogers et al. 2006). Many resources are currently being devoted to develop economically-viable fermentation processes based primarly on lignocellulosic biomass hydrolysates as substrates (Dürre 2007(Dürre , 2008López-Contreras et al. 2010;Green 2011).
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 Keasling 2010). Isopropanol can be catalytically condensed into di-isopropyl ether (DIPE) (Logsdon and Loke 2000). DIPE displays good fuel properties and could substitute methyl tert-butyl ether (MTBE) as isooctane index enhancer in gasoline composition (Huang and Sorensen 1990). Another important potential application of biologicallyproduced 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 Hiu 1986). ABE and IBE batch fermentations are similar, displaying a biphasic kinetic pattern (Jones and Woods 1986;Girbal and Soucaille 1998). 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 (Chen 1995) 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 Luyben 1986;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 laboratoryscale bioreactors with or without pH-control and compared to those of the wild-type IBE or ABEproducing 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.

Strains and cultivation conditions
The microorganisms used are listed in Table 1. E. coli culture stocks were stored at −80°C in 20% (v/v) glycerol. E. coli strains were cultivated at 37°C with agitation (250 rpm) in LB (lysogeny broth) medium (Bertani 2004). For cultivation of E. coli BW25113 harbouring pMTL500E based plasmids, the LB medium was supplemented with 2% (w/w) glucose.
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; KH 2 PO 4 , 1.0 g; K 2 HPO 4 , 0.76 g; ammonium acetate, 3.0 g; p-aminobenzoic acid, 0.10 g; MgSO 4 •7 H 2 O, 1.0 g; and FeSO 4 •7 H 2 O, 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.
Microbial growth was monitored by optical density measurements at 600 nm (Pharmacia Biotech Ultrospec 2000).

Plasmid construction and transformation
Genomic DNA from Clostridium strains was isolated using GenElute bacterial genomic DNA kit from Sigma-Aldrich. Plasmid DNA from E. coli strains was extracted using the GeneJet plasmid miniprep kit from Fermentas. PCR amplifications were done using high fidelity PCR master mix (Roche). DNA restrictions and ligations were performed using New England Biolabs restriction enzymes (ApaI, Fnu4H1, SpeI, SphI, XbaI and XhoI) and T4 DNA-Ligase enzyme, respectively. The oligonucleotides used are listed in Table 2 and were synthesized by Eurogenetec. Chemically competent E. coli strains were prepared using the Z-competent kit from Zymo-research. Kits were used according to supplier protocols.
The constructs used for the C. acetobutylicum transformation were based on the E. coli/Clostridium shuttle vector pMTL500E (Table 1). The thiolase promoter was PCR-amplified from genomic-DNA of C. acetobutylicum ATCC 824 using thlp_for and thlp_rev oligonucleotides and digested by ApaI and SphI. The adh gene was PCRamplified from C. beijerinckii NRRL B593 genomic-DNA using adh_for and adh_rev oligonucleotides and digested by ApaI and XhoI. The thl promoter and adh gene sequences were simultaneously cloned into pMTL500E plasmid (digested by SphI and XhoI) 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 XhoI and SpeI restriction enzymes and cloned into pFC002 digested XhoI and XbaI to yield pFC005 and pFC006, respectively. PCR amplification of adc gene was subsequently cloned into pFC006 digested XhoI and XbaI to yield pFC007.
Plasmid DNA constructs were introduced into chemically competent E. coli DH10B harbouring pAN2 (Heap et al. 2007) for methylation prior to transformation into C. acetobutylicum as described earlier . Correct methylation was checked by restriction analysis with Fnu4HI. Methylated pFC002, pFC005, pFC006, pFC007 and methylated pMTL500E plasmids (Table 1) 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.

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 (OD 600 : 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).

Analytical procedures
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 (Table 1). 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 Gatenbeck 1984;Tummala et al. 1999;Alsaker and Papoutsakis 2005). To upregulate 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 (Table 1). 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 ( Table 1).
Effect of expression of the adh gene on the product pool of C. acetobutylicum Plasmids pMTL500E, pFC002, pFC005, pFC006 and pFC007 were independently electroporated into C. acetobutylicum. The fermentation performance of the different C. acetobutylicum transformant strains was studied and compared with those of the wildtype strains (WT) in batch cultures performed in bioreactors with a 1 L-working volume. Cultures were performed with or without pH regulation. When pH regulated, the system was setup in such a way that once the pH had dropped to 5.0 it was kept at that level by the addition of KOH. Table 3 shows final fermentation performances of C. acetobutylicum transformants with pH regulation at 5.0.
Expression of adh by strains ATCC 824(pFC002), ATCC 824(pFC005), ATCC 824(pFC006) and ATCC 824 (pFC007) resulted in the reduction to isopropanol of about 95% of the acetone natively produced. In contrast to ATCC 824 WT or ATCC 824(pMTL500E) that produced between 0.5 and 1.1 g/L acetoin (3-hydroxy-2-  Figure 1 Concentrations of ethanol, acetone and isopropanol in 48-h cultures of E. coli BW25113 transformants. Each strain harboured the pTHL plasmid containing the thl transcription unit. butanone) (Jones and Woods 1986;Xiao and Xu 2007), very low concentrations of acetoin were detected in cultures of transformants expressing the adh gene. However, D and/or L 2,3-butanediol (2,3-BD) accumulated at 0.5-0.6 g/L when the pH was regulated at 5.0 and at 0.6-1.2 g/L when the pH was not regulated. No meso-2,3-BD was identified. Production of 2,3-BD was concomitant with production of IBE. It is worth noting that 2,3-BD was not detected in cultures of C. beijerinckii NRRL B593, probably because the organism does not produce acetoin. The enzymatic reduction of acetone and acetoin by cell-free extracts of ATCC 824(pMTL500E), ATCC 824(pFC002), ATCC 824(pFC007) and NRRL B593 WT was tested in vitro (Table 4). The cell-free extracts of ATCC 824(pFC002), ATCC 824(pFC007) and NRRL B593 WT displayed significantly higher reduction activities towards acetone and acetoin than those of ATCC 824(pMTL500E) used as control (Table 4).

Early isopropanol production in static flask culture
As the constitutive promoter of the thl gene 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   Cultures were performed in 1 L-working volume of CM1 containing 3.0 g/L ammonium acetate and 90 g/L glucose. All data are given as the mean of two or three fermentations the standard error to the mean is indicated in brackets. 1 a negative value (−) indicates that initial acetic acid from culture medium was partially consumed. 2 Fermentations were carried out at pH 5.0 but the pH set-point was not reached. 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 (Table 3). 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 g IBE /g glc for NRRL B593 vs 0.29-0.30 g IBE /g glc for ATCC 824(pFC002)). ATCC 824(pFC007) surpassed ATCC 824(pFC002) in the production of IBE, indicating that the overall metabolic activity was stimulated by the expression of pFC007 genes. ATCC 824(pFC007) produced more solvents (20.4 g/L IBE of which 7.3 g/L) and less acids than ATCC 824(pFC002) (15.1 g/L IBE of which 4.8 g/L isopropanol). In addition, the fermentation period was shorter and stopped about 10-15 hours earlier than for ATCC 824(pFC002) (Figure 2). Consequently, the solvent productivity after 30 h by ATCC 824(pFC007) (0.67 g/L h) was 2.6 times higher than that of 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 (Table 3). 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) ( Table 3). 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 ( Figure 2). 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
In order to assess the effect of the culture mode, another set of fermentations was performed without pH control (Table 5). For every strain tested, the minimum pH value reached was 4.7-4.8 (data not shown). The glucose consumptions were roughly similar to those without pH regulation. A better reassimilation of acetic and butyric acids was observed leading to better solvent titres, yields and productivities. The excretion profiles of metabolites for each strain were similar to the corresponding ones with pH regulation at 5.0. The highest solvent productions were obtained with ATCC 824(pFC007) that produced 24.4 g/L IBE (of which 8.8 g/L was isopropanol) and ATCC 824(pFC006) that produced 24.0 g/L IBE (of which 8.0 g/L was isopropanol). Lack of sporulation and extensive cell lysis were observed in cultures of ATCC 824(pFC006) or ATCC 824(pFC007) performed without pH control, highlighting the strong inhibitory effect of solvents in the early phase of cellular growth.

Discussion
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 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 Blaschek 1999).
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 Bond 1967). 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 Liao 2008;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 Papoutsakis 1988). 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 (logK ow ) values i.e. 0.05 for isopropanol and −0.25 for acetone (Yaws and Sachin 1999). The logK ow was reported to be a good estimation for solvent toxicity (Vermue et al. 1993;Heipieper et al. 1994), high logK ow 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  Butanol [g/L] 11.6 (0.2) 12.6 (1. Cultures were performed in 1 L-working volume of CM1 containing 3.0 g/L ammonium acetate and 90 g/L glucose. All data are given as the mean of two or three fermentations the standard error to the mean is indicated in brackets. * a negative value (−) indicates that initial acetic acid from culture medium was partially consumed.
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 (Table 3). 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 . 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 Bond 1967).

Conclusion
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.