- Open Access
Metabolic flux and transcriptional analysis elucidate higher butanol/acetone ratio feature in ABE extractive fermentation by Clostridium acetobutylicum using cassava substrate
© Li et al.; licensee Springer. 2014
Received: 21 April 2014
Accepted: 8 August 2014
Published: 6 September 2014
In acetone-butanol-ethanol (ABE) fermentation by Clostridium acetobutylicum ATCC 824 using corn-based substrate, the solvents are generally produced at a ratio of 3:6:1 (A:B:E, w/w).
A higher butanol/acetone ratio of 2.9:1 was found when cassava was used as the substrate of an in-situ extractive fermentation by C. acetobutylicum. This ratio had a 64% increment compared to that on corn-based substrate. The metabolic flux and (key enzymes) genes transcriptional analysis indicated that weakened metabolic fluxes in organic acids (especially butyrate) formation and re-assimilation pathways, which associated with lower buk and ctfAB transcriptional levels, contributed to higher butanol and lower acetone production rate in fermentations on cassava. Moreover, NADH generation was enhanced under the enriched reductive environment of using cassava-based substrate, which converted more carbon flux to butanol synthesis pathway, also leading to a higher ratio of butanol/acetone. To further increase butanol/acetone ratio, tiny amount of electron carrier, neutral red was supplemented into cassava-based substrate at 60 h when butonal production rate reached maximal level. However, neutral red addition enhanced NADH production, followed with strengthening the metabolic fluxes of organic acids formation/re-assimilation pathways, resulted in unchanged in butanol/acetone ratio.
A further increase in butanol/acetone ratio could be realized when NADH regeneration was enhanced and the metabolic fluxes in organic acids formation/reutilization routes were controlled at suitably low levels simultaneously.
Clostridium acetobutylicum, a Gram-positive, spore-forming, and obligate anaerobe, has the ability to produce solvents with renewable biomasses including acetone, butanol, and ethanol . In acetone-butanol-ethanol (ABE) fermentation by C. acetobutylicum using corn-based substrate, the solvents are generally produced at a ratio of 3:6:1 (A/B/E, w/w). Among these solvents, butanol has the most attraction since it has been considered as a high-performance biofuel, as well as an important platform chemical. However, high substrate (such as corn) price and too much purification cost due to very low solvent concentrations are the two major factors impacting on economics of butanol production . A cost sheet from an ABE fermentation plant using corn indicated that the substrate price accounted for up to 79% of the overall production cost, while energy cost consumed in product distillation almost contributed the rest 14% of the entire cost . Therefore, seeking cheaper feedstock and increasing butanol ratio in total solvents have become the major challenges for the economic viability of ABE fermentation.
Some low-priced agriculture residues for example corn fiber and wheat bran have been used in ABE fermentation by clostridia, but butanol concentration and productivity in these fermentations are much lower than those in corn-based fermentation -. Cassava, a non-grain and high starch content crop, is recognized as an economical and practical substrate for industrial fermentation. In some previous studies, cassava was successfully used instead of corn as substrate in ABE fermentation by C. acetobutylicum, and higher butanol/acetone ratios were observed when fermenting on cassava as compared with the same procedures using corn ,. In these cases, the online monitored parameters (pH, ORP, H2/CO2 ratio, etc.) and organic acid formation/reassimilation patterns were quite different from those on corn-based substrate. But the mechanism of higher butanol ratios in cassava-based fermentation has still not been illustrated clearly, for the activities of key enzymes in vivo were difficult or impossible to be measured, caused by hardly separating cells from mixed solid residues of substrate.
Some efforts have investigated the special features presented in ABE fermentation by C. acetobutylicum, using either metabolic flux analysis or transcriptional analysis -. Metabolic flux analysis is a systematic approach developed to evaluate each individual reaction rate within a metabolic network. Investigation on genetic transcriptional levels directly correlates the activities of relevant enzymes. To solve the problems mentioned above, the methods of metabolic flux analysis was combined with genes (key enzymes) transcriptional measurements to explore the mechanism of higher butanol/acetone ratio feature in cassava-based fermentation. Traditional batch process is still the most commonly used operation mode in industrial ABE fermentations. However, it is suffered with severe butanol end-inhibition leading to a short fermentation period, so that interpreting many attractive phenomena becomes difficult. By contrast, in-situ extractive fermentation could relieve butanol inhibitory effect to improve fermentation productivity and to prolong fermentation time -. The in-situ extractive fermentation technique is not widely used in industrial ABE fermentation because of the high extractant cost and operation complexity. However, it could be used as an important prototype for investigating various characteristics of ABE fermentation, and guiding the optimal operation ways of ABE traditional fermentation. Among various in-situ fermentation extractants for butanol, oleyl alcohol has been recognized as the best one because of its non-toxicity to cell growth and high butanol extraction coefficient . In this study, ABE extractive fermentations by C. acetobutylicum ATCC 824 were conducted in a 7-L anaerobic fermentator, under the conditions of using different biomass substrate (corn or cassava). Combinational analysis of metabolic flux distribution and gene transcriptional levels were carried out to find out the variations in intracellular carbon distributions and transcriptional levels when using corn- or cassava-based substrate. All these efforts aimed to clarify the mechanism of higher butanol/acetone ratio obtained when using cassava-based medium and explore the optimal operation way for traditional ABE fermentation characterized with high butanol/acetone ratio.
C. acetobutylicum ATCC 824 was used in this study. The strain was maintained as spore suspension in 5% corn meal medium at 4°C. The methods of inoculation and pre-culture followed those described in the literatures ,.
Substrate (media) preparation and in-situ fermentative extractant pretreatment
The corn flour (raw starch content about 50% w/w) was obtained at local market and cassava powder (raw starch content about 65% to 70% w/w) was provided by Henan Tianguan Fuel Ethanol Co. Ltd., Nanyang, China. The media were pretreated by adding certain amount of α-amylase (8 U/g-corn or cassava, heated in boiling water bath for 45 min) and then glucoamylase (120 U/g-corn or cassava, heated at 62°C for 60 min). Subsequently, the viscosity-reduced media were autoclaved at 121°C for 20 min. Oleyl alcohol (Tokyo Kasei Co. Ltd., Tokyo, Japan) was used as the extractant for in-situ extractive fermentation. Oleyl alcohol was either sterilized at 121°C for 20 min or directly used without sterilization, and then added into the fermentor. When using cassava as substrate, the concentrated yeast extract solution was sterilized at 115°C for 30 min, and then pumped into the broth upon requirement since it has been revealed in the previous study that yeast extract could promote the phase shift in ABE fermentation with cassava substrate . Neutral red was dissolved in sterilized water and pumped into the broth at 60 h.
Fermentation method and condition
Seed culture was carried out in 100-mL anaerobic fermentation bottles using corn as the substrate. The initial corn or cassava meal content for extractive fermentations was 30% or 25% (w/v). The fermentations were conducted in a 7-L static fermentor (Baoxing Bioengineering Co., Shanghai, China) equipped with pH and ORP (oxidative-reductive potential) electrodes and a manual adjusted pressure unit. A temperature-controllable water bath (MP-10, Shanghai Permanent Science and Technology, Co., Shanghai, China) was used to circulate hot water into the coil pipes settled inside the fermentor to maintain broth temperature at 37°C. The fermentation medium loading volume ranged from 1.8 to 2.5 L, and equivalent volume of oleyl alcohol was added to ensure a 1:1 oil/broth volumetric ratio. N2 was sparged into the extractant reservoir for 10 min to remove residual oxygen. 10% (v/v) inoculum was transferred into the fermentor and then N2 was also sparged into broth for 10 min. The oxygen-free oleyl alcohol was poured into the fermentor using a peristaltic pump after inoculation. The initial pressure inside the fermentor was controlled at about 0.02 MPa (N2) to strictly maintain the anaerobic condition. The pressure gradually increased since fermentation started and self-generated gas began to evolve. The pressure was then controlled in a range of 0.030 to 0.055 MPa throughout fermentation. Agitation was occasionally adopted for a short time (5 min, 400 rpm) to promote butanol diffusion from aqueous phase into extractant phase.
The measurements of concentrations of solvents, organic acids and reducing sugar (glucose) were the same as those described in our previous reports ,. On account of the volume ratio of aqueous to organic phase being just 1:1 in extractive fermentation, the total concentration of butanol (or acetone) was the sum of butanol (or acetone) in broth and in extractant. H2/CO2 ratio in exhaust gas was determined using the same method reported in our previous work . The concentration of important intermediate, butyraldehyde in broth was determined by a gas chromatography (Shimadzu GC-2010, Kyoto, Japan) with flame ionization detector and DB-23 capillary column (60 m × 0.25 mm ID × 0.32 μm, Agilent, Sta. Clara, CA, USA). The condition was described as follows: nitrogen was used as the carrier gas at a velocity of 1.2 mL/min; the hydrogen and air flow rates were 47 and 400 mL/min, respectively; injector temperature was operated at 200°C, and detector temperature at 250°C; the initial temperature stayed at 40°C for 5 min, and then raised at the velocity of 10°C per min until arriving to 180°C, and finally stayed for another 5 min.
Metabolic flux analysis
As shown in Figure 1 and the Appendix, the MR model contained 19 metabolic reaction rates (k = 19). Among the rates, seven extracellular substance rates were measurable (m = 7) including rates of glucose consumption, organic acid formation or re-assimilation, solvents synthesis, and hydrogen evolution. As shown in the Appendix, there were a total of 13 substances (n = 13) covering substrates, products and intermediate metabolites, and thus 13 mass balance equations were available. Thus, this MR model is an overdetermined system (n = 13 > k-m = 12). All of the unknown reaction rates could be optimally determined using the measurable rate data and the stoichiometric coefficients of the metabolic reaction matrix with the aid of the calculation package embedded in Matlab (Ver. R2010b, MathWorks Inc., Natick, MA, USA) . The following treatments were applied in the network model calculation: (1) glucose was calculated in the model as single carbon resource since it was the most preferred for strain and highest percentage in these complex mediums; (2) glucose consumption rates were normalized as 100 mmol/(L⋅h), and the other measurable rates were recalculated using the above (glucose) normalization coefficient; (3) pseudo-steady state assumption was adopted for intracellular intermediate metabolites.
RNA purification, cDNA synthesis, and real-time fluorescence quantitative PCR analysis
Primer sequences used in the real-time fluorescence quantitative PCR
Fragment size (bp)
Fermentation performances comparison when using corn or cassava as substrate
The maximum butyrate accumulation in cassava broth was 1.2 g/L, only half of which in corn broth. Furthermore, after entering solventogenic phase, acetate and butyrate re-assimilation rates were significantly slower in cassava-based fermentation. The final solvent concentrations (including butanol and acetone in both extractive and aqueous phase. ethanol was not accounted for due to low accumulation) reached a total level of 50 g/L in both cases, in which butanol/acetone ratio was 2.87 using cassava-based substrate and 1.75 with corn. All these distinctions, particularly butanol/acetone and H2/CO2 ratios, were important in understanding the optimal regulation for ABE fermentation. Their mechanisms should be properly interpreted.
Metabolic flux analysis in ABE extractive fermentations with corn and cassava
High butanol/acetone ratio is desirable for ABE fermentation. It reached nearly 2.9 when using cassava-based substrate, a 64% enhancement compared to corn. To understand this result, metabolic flux analysis was conducted to explore the mechanisms.
Gene transcriptional analysis for ABE extractive fermentations with corn and cassava
Attempt of further butanol/acetone ratio enhancement by adding neutral red in ABE fermentation with cassava
Fermentation performance under various operation modes with corn and cassava substrates
Cassava + Neutral red
Number of experiments
Fermentation time (h)
Total butanol (g/L)
33.26 ± 2.61
37.48 ± 3.11
42.60 ± 2.02
Total acetone (g/L)
18.98 ± 1.39
13.06 ± 0.93
14.59 ± 0.60
Butanol/acetone ratio (−)
1.75 ± 0.01
2.87 ± 0.03
2.92 ± 0.02
3.20 ± 0.60
2.94 ± 0.27
2.80 ± 0.03
1.40 ± 0.22
1.24 ± 0.34
1.60 ± 0.08
2.58 ± 0.34
1.27 ± 0.16
1.44 ± 0.28
0.39 ± 0.06
0.41 ± 0.12
0.51 ± 0.15
Gas production (L/L-broth)
80.00 ± 6.13
72.37 ± 5.37
64.86 ± 0.11
Butanol productivity (g/L/h)
0.33 ± 0.02
0.37 ± 0.03
0.42 ± 0.02
The butanol/acetone ratio reached a much higher level of 2.87 in extractive fermentation with cassava substrate, a 64% increment as compared to using corn substrate (Table 2). It was close to the reported ratio obtained in fermentations by a hyper-butanol strain of C. acetobutylicum EA 2018 with corn-based medium . The preliminary analysis to fermentation performances showed that ORP and H2/CO2 ratio were both at low levels when using cassava (Figure 2). ORP could be considered as a comprehensive index reflecting pH, dissolved oxygen, reductive potential of compounds dissolved in medium . The ABE fermentation required an anaerobic environment so that dissolved oxygen in broth could be ignored. Change patterns of pH were basically similar when using different substrates. Thus, the lower ORP suggested that cassava-based medium was rich in reductive substances. On the other hand, H2 and CO2 are the two major components in the exhaust gas emitted by clostridia. H2 is generated from the electron transport shuttle system via the reaction of 2H+ + 2e− → H2 catalyzed by hydrogenase . CO2 is mainly produced in reaction of Pyruvate → Acetyl-CoA associated with formation of reductive ferredoxin, the electron donor for hydrogen or NADH generation . Therefore, lower H2/CO2 ratio implied that more electron flows were distributed to NADH production in the electron transport shuttle system.
Based on the preliminary analysis results, metabolic flux and gene transcriptional analysis were conducted to verify the assumption and to elucidate the mechanism about high butanol/acetone ratio in cassava-based fermentation. The metabolic flux analysis revealed that NADH was truly generated more under the cassava-based environment (Figure 3), which was consistent with the preliminary analysis results. It should be addressed that the genes (adhE and bdhB) regulating butanol synthesis had higher transcriptional levels under corn-based environment, but more butanol production was obtained in cassava-based fermentation. This fact demonstrated that NADH generation rate is one of dominated factors controlling butanol/acetone ratio in ABE fermentations by C. acetobutylicum. Besides, metabolic flux of butyrate closed-loop (rByH and rACE-By) in cassava-based fermentation was largely weakened after shifting into solventogenic phase. Correspondently, transcriptional levels of buk and ctfAB (responsible for butyrate formation and re-assimilation respectively) were much lower than those in corn-based fermentation. In metabolic pathway of C. acetobutylicum, butyrate formation and re-assimilation reaction constitute a closed-loop (butyrate loop) at butyryl-CoA node (Figure 1). The butyrate loop not only competes with butanol synthesis route for carbon resource, but also relates to acetone formation. Therefore, high butanol/acetone ratio in cassava-based fermentation was also attributed to weakened metabolic strength of butyrate closed-loop. It could be concluded that higher NADH generation rate and lower metabolic flux in butyrate closed-loop worked jointly, leading to the high butanol/acetone ratio feature in fermentation with cassava-based substrate.
The alteration of redox balance to promote NADH generation has been reported in many studies using corn or glucose as substrate. The methods of provision of artificial electron carriers such as neutral red , and methyl viologen -, ORP regulation , and inhibition of hydrogenase by spraying carbon monoxide ,, all of them have effect on enhancing butanol/acetone ratio. Among these approaches, adding neutral red seems to be the most appropriate one of low-cost and easy to operate. In the previous works, it has been demonstrated that adding neutral red could acquire a 63% increment in butanol/acetone ratio with corn-based substrate ,. Therefore, neutral red was added into cassava broth at 60 h when butanol production rate was in a relatively high level, in order to further enhance butanol/acetone ratio. The results indicated that final butanol concentration could slightly increase, due to the enhancements in rNADH and adhE transcriptional level after neutral red addition. However, the metabolic fluxes of organic acid formation/re-assimilation pathway and ctfAB transcription level were also enhanced after supplementing neutral red (Figures 5 and 6), which was actually beneficial for acetone formation. The simultaneous enhancement of both butanol and acetone synthesis route led to an unchanged butanol/acetone ratio in cassava-based fermentation with neutral red addition. It was speculated that under the reductive compound-enriched environment using cassava-based substrate, reductive power NADH might have been excessively produced/consumed leading to a burden on cellular metabolism . To match up relatively low fluxes of the acid loops with enhanced NADH regeneration in an appropriate way will be the key issue in obtaining further high butanol/acetone ratio while maintaining comparably high butanol productivity.
In addition to strength of the reductive power, many other approaches have been adopted to acquire high butanol/acetone ratio. Among these efforts, some modifications to metabolic pathways were obtained good effect on increasing butanol/acetone ratio. Harris et al. used metabolic engineering tools to restrain buk (encoding butyrate kinase) expression and resulted in a significant increase in butanol/acetone ratio (3.8) . Jang et al. further strengthened the butanol synthesis pathway by up-regulating adhE expression, on the basis of the weakened acid formation pathway, which achieved a rather high butanol/acetone ratio (8.8) . However, some other attempts to regulate pathways had totally different results. Lehmann et al. sought to construct a pta/ptb double knockout strain of C. acetobutylicum but failed to find any positive clones . Tummala attempted to downregulate the expression of ctfAB, but observed high organic acid accumulation in broth with low solvent production . It could be found that all these efforts to extend the butanol/acetone ratio were involved in the modifications of acid formation pathways. It is known that acetate and butyrate formation pathways are the major energy substance (ATP) production route in C. acetobutylicum. As obligate anaerobes, clostridia are rather inefficient in energy production. So an irreversible change on the major energy substance (ATP) production route would inevitably bring adverse impact on cell growth and solvent production. In this study, a 64% increment in butanol/acetone ratio was obtained by changing corn to a cheaper feedstock cassava, without irreversible damages to cell or cost increase (the additional amount of yeast extract was rather less, and the cost of cassava-added yeast extract was even much lower than that of corn). Moreover, most of the mechanism analysis researches in the past were based on concise culture environment by using a defined medium. Therefore, this mechanism research based on biomass substrate was necessary for achieving high butanol/acetone ratio under industrial ABE fermentation condition.
In addition, it was noteworthy that why higher NADH generation rate and lower metabolic flux of butyrate closed-loop appeared in cassava-based culture environment not corn? What special chemical compositions of cassava resulted in these phenomena? Aiming to illustrate the above questions, another research is now carried out by us. Currently, it is discovered that when carbon/nitrogen ratio (C/N ratio) in the substrate is increased from 46.7 to 186.7 mol/mol, acid formation is visibly restrained in the solventogenic phase, leading to a 28% reduction in acetone production, but no adverse impact on butanol production. Moreover, H2 generation dropped off rapidly, associated with C/N ratio increase, which implied that high C/N ratio could limit the electron directing to H2 synthesis and contribute to enhance NADH production. These results indicated that higher C/N ratio contained in cassava (118.8 mol/mol) compared to corn (21.9 mol/mol) may be one of the factors leading to higher butanol/acetone ratio. Besides, there are still other potential factors needed to be further confirmed. The toxic compounds contained in cassava, which may have caused the restraint of some enzyme activities such as CoA-transfer or butyrate kinase, is a notable aspect and needs to be explored deeply.
A higher butanol/acetone ratio of approximately 2.9:1 was observed in extractive fermentation on cassava-based substrate, which had a 64% increment compared to that on corn-based substrate. The results from metabolic flux and transcriptional analysis indicated that the weakened metabolic fluxes in organic acids (especially butyrate) formation/re-assimilation pathways, as well as the enhancement of NADH generation, contributed to this higher butanol/acetone ratio feature in fermentation on cassava. Moreover, neutral red added in cassava broth could not further increase butanol/acetone ratio, which demonstrated that a further higher butanol/acetone ratio could be realized only when NADH regeneration is enhanced and the metabolic fluxes in organic acid formation/reutilization routes are controlled at suitably low levels simultaneously.
Metabolic reactions in ABE fermentation by Clostridium acetobutylicum ATCC 824
rGlu(r1): Glucose → 2 Pyruvate + 2 NADH + 2 ATP
rPyr(r2): Pyruvate → Acetyl-CoA + CO2 + Reduced ferredoxin
rEtOH(r3): Acetyl-CoA + 2 NADH → Ethanol
rAcH(r4): Acetyl-CoA → Acetate + ATP
rAc-CoA(r5): 2 Acetyl-CoA → Acetoacetyl-CoA
rACE-Ac(r6): Acetoacetyl-CoA + Acetate → Acetone + CO2 + Acetyl-CoA
rACE-By(r7): Acetoacetyl-CoA + Butyrate → Acetone + CO2 + Butyryl-CoA
rBy-CoA(r8): Acetoacetyl-CoA + 2 NADH → Butyryl-CoA
rByH(r9): Butyryl-CoA → Butyrate + ATP
rBtOH(r10): Butyryl-CoA + 2 NADH → Butanol
rH2(r11): Reduced ferredoxin → H2
rNADH(r12): Reduced ferredoxin → NADH
Intercelluar enzymes in C. acetobutylicum ATCC 824
E1, pyruvate-ferredoxin oxidoreductase; E2, ferredoxin-NAD reductase; E3, hydrogenase; E4, phosphotransacetylase; E5, acetate kinase (encoded by ask); E6, acetaldehyde dehydrogenase; E7, ethanol dehydrogenase; E8. thiolase; E9, CoA-transferase (encoded by ctfAB); E10, acetoacetate decarboxylase; E11, β-hydroxybutyryl-CoA dehydrogenase; E12, crotonase; E13, butyryl-CoA dehydrogenase; E14, phosphotrans butyrylase; E15, butyrate kinase (encoded by buk); E16, butyraldehyde dehydrogenase (encoded by adhE); E17, butanol dehydrogenase (encoded by bdhB).
The study was supported by the National Natural Science Foundation Program (#20976072) and Major State Basic Research Development Program (#2007CB714303) of China. The authors also appreciated the assistance from Mr. Kevin Ding in refining the English of the manuscript.
- Jones DT, Woods DR: Acetone-butanol fermentation revisited. Microbiol Rev 1986,50(4):484–524.Google Scholar
- Lee SY, Park JH, Jang SH, Nielsen LK, Kim J, Jung KS: Fermentative butanol production by clostridia. Biotechnol Bioeng 2008,101(2):209–228. 10.1002/bit.22003View ArticleGoogle Scholar
- Pfromm PH, Amanor-Boadu V, Nelson R, Vadlani P, Madl R: Bio-butanol vs. bio-ethanol: a technical and economic assessment for corn and switchgrass fermented by yeast or Clostridium acetobutylicum . Biomass Bioenergy 2010,34(4):515–524. 10.1016/j.biombioe.2009.12.017View ArticleGoogle Scholar
- Liu Z, Ying Y, Li F, Ma C, Xu P: Butanol production by Clostridium beijerinckii ATCC 55025 from wheat bran. J Ind Microbiol Biotechnol 2010,37(5):495–501. 10.1007/s10295-010-0695-8View ArticleGoogle Scholar
- Qureshi N, Ezeji TC, Ebener J, Dien BS, Cotta MA, Blaschek HP: Butanol production by Clostridium beijerinckii . Part I: use of acid and enzyme hydrolyzed corn fiber. Bioresour Technol 2008,99(13):5915–5922. 10.1016/j.biortech.2007.09.087View ArticleGoogle Scholar
- Qureshi N, Saha BC, Dien B, Hector RE, Cotta MA: Production of butanol (a biofuel) from agricultural residues: Part I - use of barley straw hydrolysate. Biomass Bioenergy 2010,34(4):559–565. 10.1016/j.biombioe.2009.12.024View ArticleGoogle Scholar
- Qureshi N, Saha BC, Hector RE, Dien B, Hughes S, Liu S, Iten L, Bowman MJ, Sarath G, Cotta MA: Production of butanol (a biofuel) from agricultural residues: Part II - use of corn stover and switchgrass hydrolysates. Biomass Bioenergy 2010,34(4):566–571. 10.1016/j.biombioe.2009.12.023View ArticleGoogle Scholar
- Lu C, Zhao J, Yang ST, Wei D: Fed-batch fermentation for n-butanol production from cassava bagasse hydrolysate in a fibrous bed bioreactor with continuous gas stripping. Bioresour Technol 2012, 104: 380–387. 10.1016/j.biortech.2011.10.089View ArticleGoogle Scholar
- Li X, Li Z, Zheng J, Shi Z, Li L: Yeast extract promotes phase shift of bio-butanol fermentation by Clostridium acetobutylicum ATCC824 using cassava as substrate. Bioresour Technol 2012, 125: 43–51. 10.1016/j.biortech.2012.08.056View ArticleGoogle Scholar
- Harris LM, Blank L, Desai RP, Welker NE, Papoutsakis ET: Fermentation characterization and flux analysis of recombinant strains of Clostridium acetobutylicum with an inactivated solR gene. J Ind Microbiol Biotechnol 2001,27(5):322–328. 10.1038/sj.jim.7000191View ArticleGoogle Scholar
- Desai RP, Harris LM, Welker NE, Papoutsakis ET: Metabolic flux analysis elucidates the importance of the acid-formation pathways in regulating solvent production by Clostridium acetobutylicum . Metab Eng 1999,1(3):206–213. 10.1006/mben.1999.0118View ArticleGoogle Scholar
- Hoenicke D, Janssen H, Grimmler C, Ehrenreich A, Luetke-Eversloh T: Global transcriptional changes of Clostridium acetobutylicum cultures with increased butanol:acetone ratios. New Biotechnol 2012,29(4):485–493. 10.1016/j.nbt.2012.01.001View ArticleGoogle Scholar
- Bankar SB, Survase SA, Singhal RS, Granstrom T: Continuous two stage acetone-butanol-ethanol fermentation with integrated solvent removal using Clostridium acetobutylicum B 5313. Bioresour Technol 2012, 106: 110–116. 10.1016/j.biortech.2011.12.005View ArticleGoogle Scholar
- Dhamole PB, Wang Z, Liu Y, Wang B, Feng H: Extractive fermentation with non-ionic surfactants to enhance butanol production. Biomass Bioenergy 2012, 40: 112–119. 10.1016/j.biombioe.2012.02.007View ArticleGoogle Scholar
- Roffler SR, Blanch HW, Wilke CR: In-situ recovery of butanol during fermentation. Bioprocess Biosyst Eng 1987,2(1):1–12. 10.1007/BF00369221View ArticleGoogle Scholar
- Evans PJ, Wang HY: Enhancement of butanol formation by Clostridium acetobutylicum in the presence of decanol-oleyl alcohol mixed extractants. Appl Environ Microbiol 1988,54(7):1662–1667.Google Scholar
- Zhang L, Yang Y, Shi Z: Performance optimization of property-improved biodiesel manufacturing process coupled with butanol extractive fermentation. Chin J Biotechnol 2008,24(11):1943–1948.Google Scholar
- Li Z, Li X, Zheng J, Zhang S, Shi Z: Butanol extractive fermentation to simultaneously produce “properties improved” biodiesel and butanol in a water and energy-saving operation way. J Biobased Mater Bioenergy 2011,5(3):312–318. 10.1166/jbmb.2011.1150View ArticleGoogle Scholar
- Papoutsakis ET: Equations and calculations for fermentations of butyric acid bacteria. Biotechnol Bioeng 1984,26(2):174–187. 10.1002/bit.260260210View ArticleGoogle Scholar
- Meyer CL, Papoutsakis ET: Increased levels of ATP and NADH are associated with increased solvent production in continuous cultures of Clostridium acetobutylicum . Appl Microbiol Biotechnol 1989,30(5):450–459. 10.1007/BF00263849View ArticleGoogle Scholar
- Takiguchi N, Shimizu H, Shioya S: An on-line physiological state recognition system for the lysine fermentation process based on a metabolic reaction model. Biotechnol Bioeng 1997,55(1):170–181. 10.1002/(SICI)1097-0290(19970705)55:1<170::AID-BIT18>3.0.CO;2-QView ArticleGoogle Scholar
- Gu Y, Hu S, Chen J, Shao L, He H, Yang Y, Yang S, Jiang W: Ammonium acetate enhances solvent production by Clostridium acetobutylicum EA 2018 using cassava as a fermentation medium. J Ind Microbiol Biotechnol 2009,36(9):1225–1232. 10.1007/s10295-009-0604-1View ArticleGoogle Scholar
- Ishizaki A, Snibai H, Hirose Y: Basic aspects of electrode potential change in submerged fermentation. Agric Biol Chem 1974, 38: 2399–2405. 10.1271/bbb1961.38.2399View ArticleGoogle Scholar
- Demuez M, Cournac L, Guerrini O, Soucaille P, Girbal L: Complete activity profile of Clostridium acetobutylicum FeFe -hydrogenase and kinetic parameters for endogenous redox partners. FEMS Microbiol Lett 2007,275(1):113–121. 10.1111/j.1574-6968.2007.00868.xView ArticleGoogle Scholar
- Gheshlaghi R, Scharer JM, Moo-Young M, Chou CP: Metabolic pathways of clostridia for producing butanol. Biotechnol Adv 2009,27(6):764–781. 10.1016/j.biotechadv.2009.06.002View ArticleGoogle Scholar
- Girbal L, Vasconcelos I, Sant-Amans S, Soucaille P: How neutral red modified carbon and electron flow in Clostridium acetobutylicum grown in chemostat culture. FEMS Microbiol Rev 1995, 16: 151–162. 10.1111/j.1574-6976.1995.tb00163.xView ArticleGoogle Scholar
- Peguin S, Goma G, Delorme P, Soucaille P: Metabolic flexibility of Clostridium acetobutylicum in response to methyl viologen addition. Appl Microbiol Biotechnol 1994, 42: 611–616. 10.1007/BF00173928View ArticleGoogle Scholar
- Rao G, Mutharasan R: Altered electron flow in continuous cultures of Clostridium acetobutylicum induced by viologen dyes. Appl Environ Microbiol 1987,53(6):1232–1235.Google Scholar
- Rao G, Mutharasan R: Alcohol production by Clostridium acetobutylicum induced by methyl viologen. Biotechnol Lett 1986,8(12):893–896. 10.1007/BF01078655View ArticleGoogle Scholar
- Wang S, Zhu Y, Zhang Y, Li Y: Controlling the oxidoreduction potential of the culture of Clostridium acetobutylicum leads to an earlier initiation of solventogenesis, thus increasing solvent productivity. Appl Microbiol Biotechnol 2012,93(3):1021–1030. 10.1007/s00253-011-3570-2View ArticleGoogle Scholar
- Kim BH, Bellows P, Datta R, Zeikus JG: Control of carbon and electron flow in Clostridium acetobutylicum fermentations: utilization of carbon monoxide to inhibit hydrogen production and to enhance butanol yields. Appl Environ Microbiol 1984,48(4):764–770.Google Scholar
- Meyer CL, Roose JW, Papoutsakis ET: Carbon monoxide gasing leads to alcohol production and butyrate uptake without acetone formation in continuous cultures of Clostridium acetobutylicum . Appl Microbiol Biotechnol 1986, 24: 159–167. 10.1007/BF01982561Google Scholar
- Savinell JM, Palsson BO: Network analysis of intermediary metabolism using linear optimization. I. Development of mathematical formalism. J Theor Biol 1992,154(4):421–454. 10.1016/S0022-5193(05)80161-4View ArticleGoogle Scholar
- Harris LM, Desai RP, Welker NE, Papoutsakis ET: Characterization of recombinant strains of the Clostridium acetobutylicum butyrate kinase inactivation mutant: need for new phenomenological models for solventogenesis and butanol inhibition? Biotechnol Bioeng 2000,67(1):1–11. 10.1002/(SICI)1097-0290(20000105)67:1<1::AID-BIT1>3.0.CO;2-GView ArticleGoogle Scholar
- Jang YS, Lee JY, Lee J, Park JH, Im JA, Eom MH, Lee J, Lee SH, Song H, Cho JH, Seung DY, Lee SY: Enhanced butanol production obtained by reinforcing the direct butanol-forming route in Clostridium acetobutylicum . Mbio 2012,3(5):e00314–12. 10.1128/mBio.00314-12View ArticleGoogle Scholar
- Lehmann D, Radomski N, Luetke-Eversloh T: New insights into the butyric acid metabolism of Clostridium acetobutylicum . Appl Microbiol Biotechnol 2012,96(5):1325–1339. 10.1007/s00253-012-4109-xView ArticleGoogle Scholar
- Tummala SB, Junne SG, Papoutsakis ET: Antisense RNA downregulation of coenzyme A transferase combined with alcohol-aldehyde dehydrogenase overexpression leads to predominantly alcohologenic Clostridium acetobutylicum fermentations. J Bacteriol 2003,185(12):3644–3653. 10.1128/JB.185.12.3644-3653.2003View ArticleGoogle Scholar
This article is published under license to BioMed Central Ltd. This is an open access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/4.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly credited.