Acetone-butanol-ethanol Fermentation Research Articles

Integrated kinetic modeling of acetone-butanol-ethanol fermentation by Clostridium saccharoperbutilacetonicum N1-4: Co-utilization strategy with cane molasses, biomass-derived sugars, and furaldehydes

Sugar-based byproducts such as molasses and bagasse are abundant resources for large-scale biobutanol commercialization. This study presents a comprehensive kinetic model to analyze ABE (acetone-butanol-ethanol) fermentation by C. saccharoperbutilacetonicum N1-4, emphasizing diverse carbon sources and furaldehyde co-utilization. By leveraging sensitivity analysis against models in the literature and the proposed model as well as parameter optimization using Scilab®, the potential for the simultaneous utilization of sugarcane molasses and bagasse-derived sugars alongside furfural and HMF for butanol synthesis was assessed. These findings revealed that despite the microbial preference for hexose sugars, the incorporation of up to 25% pentose sugars did not significantly hinder butanol production. However, furaldehydes perturbed butyric acid assimilation and acetyl-CoA consumption while enhancing acetone-butanol-ethanol synthesis. The simulation highlighted the peak concentrations of furfural and HMF (0.33 mmol L−1 and 0.03 mmol L−1, respectively), underscoring their conversion to less toxic alcohols, thereby augmenting metabolism. Sensitivity analysis underscores the necessity of enhancing butyric acid assimilation, providing critical insights for optimizing ABE fermentation and advancing biobutanol production from sugar-based byproducts.

Superstructure optimization of hydrothermal liquefaction for microalgae biorefinery considering environmental impacts and economics

Microalgae biorefinery superstructure connections from algae to muti-products are addressed. The superstructure connections affect eCO2 emissions, product variety, and profits. Through the superstructure optimization algorithm for the illustrated four scenarios within the same lipid content of 25% and 200 kg weight of microalgae, (i) Scenario-1 for maximizing the net profit, the best net profit of 32.54 USD is achieved due to producing the green electricity and biodiesel, (ii) Scenario-2 for minimizing total eCO2 emissions, the lowest total eCO2 emissions with 78.28 kg eCO2 is guaranteed if the power generation from biogas is assumed to fully cover load demands of the process units but the corresponding net profit is down to 10.84 USD, (iii) Scenario-3 for balancing net profit and eCO2 emissions, the net profit is returned to 17.65 USD since the acetone/butanol/ethanol by the ABE fermentation and biooil/green diesel are added, (iv) Scenario-4 for maximizing biooil production, the total revenue is higher than Scenarios 1-3 by 16∼164% but the corresponding eCO2 emissions is also higher than Scenarios 1-3 by 65∼160%. Although the superstructure optimization problem induces the trade-off results, it is validated that the combination of ABE fermentation and HTL is superior to the combination of transesterification and anaerobic digestion.

Efficient butanol production from sweet sorghum stem juice by a co-culture system at an optimum temperature: Insights from oxidation-reduction potential monitoring and pilot scale validation

A two-stage co-culture approach was employed in an acetone-butanol-ethanol (ABE) fermentation. An obligate aerobic bacterium, Arthrobacter sp., was first grown for 6 h at 30 °C to create anaerobic conditions. Subsequently, Clostridium beijerinckii TISTR 1461 was inoculated and a fermentation was performed at 37 °C. To identify an intermediate temperature suitable for both microorganisms, their growth was examined at 30, 34, and 37 °C. C.beijerinckii exhibited the highest specific growth rate at 37 °C, while Arthrobacter sp. displayed similar growth rates at all tested temperatures. Butanol production from a synthetic medium (P2 medium) by C. beijerinckii at different temperatures using oxygen-free nitrogen (OFN) gas flushing as a control treatment revealed that fermentation at 37 °C gave the highest butanol concentration (PB, 9.98 g/L). Consequently, 37 °C was chosen for butanol production from sweet sorghum stem juice (SSJ) by co-culture of these two microorganisms in 1-L screw–capped bottles. Compared to the control treatment, higher PB (11.38 g/L), yield (YB/S, 0.37 g/g) and productivity (QB, 0.24 g/L·h) were achieved using the co-culture system. These results were further confirmed by monitoring the oxidation–reduction potential (ORP) during ABE fermentation in a 2-L stirred-tank bioreactor (STR). Moreover, when the co-culture fermentation at 37 °C was scaled up in a 30-L STR, the PB, YB/S and QB values were comparable to those obtained in the 2-L STR. Therefore, co-culture fermentation of Arthrobacter sp. and C.beijerinckii TISTR 1461 at 37 °C represents a promising method for large-scale butanol production.

The Effect of Technological Conditions on ABE Fermentation and Butanol Production of Rye Straw and the Composition of Volatile Compounds.

The objective of this study was to evaluate the effect of pretreatment and different technological conditions on the course of ABE fermentation of rye straw (RS) and the composition of volatile compounds in the distillates obtained. The highest concentration of ABE and butanol was obtained from the fermentation of pretreated rye straw by alkaline hydrolysis followed by detoxification and enzymatic hydrolysis. After 72 h of fermentation, the maximum butanol concentration, productivity, and yield from RS were 16.11 g/L, 0.224 g/L/h, and 0.402 g/g, respectively. Three different methods to produce butanol were tested: the two-step process (SHF), the simultaneous process (SSF), and simultaneous saccharification with ABE fermentation (consolidation SHF/SSF). The SHF/SSF process observed that ABE concentration (21.28 g/L) was higher than in the SSF (20.03 g/L) and lower compared with the SHF (22.21 g/L). The effect of the detoxification process and various ABE fermentation technologies on the composition of volatile compounds formed during fermentation and distillation were analyzed.

Application of fed-batch strategy to fully eliminate the negative effect of lignocellulose-derived inhibitors in ABE fermentation

BackgroundInhibitors that are released from lignocellulose biomass during its treatment represent one of the major bottlenecks hindering its massive utilization in the biotechnological production of chemicals. This study demonstrates that negative effect of inhibitors can be mitigated by proper feeding strategy. Both, crude undetoxified lignocellulose hydrolysate and complex medium supplemented with corresponding inhibitors were tested in acetone–butanol–ethanol (ABE) fermentation using Clostridium beijerinckii NRRL B-598 as the producer strain.ResultsFirst, it was found that the sensitivity of C. beijerinckii to inhibitors varied with different growth stages, being the most significant during the early acidogenic phase and less pronounced during late acidogenesis and early solventogenesis. Thus, a fed-batch regime with three feeding schemes was tested for toxic hydrolysate (no growth in batch mode was observed). The best results were obtained when the feeding of an otherwise toxic hydrolysate was initiated close to the metabolic switch, resulting in stable and high ABE production. Complete utilization of glucose, and up to 88% of xylose, were obtained. The most abundant inhibitors present in the alkaline wheat straw hydrolysate were ferulic and coumaric acids; both phenolic acids were efficiently detoxified by the intrinsic metabolic activity of clostridia during the early stages of cultivation as well as during the feeding period, thus preventing their accumulation. Finally, the best feeding strategy was verified using a TYA culture medium supplemented with both inhibitors, resulting in 500% increase in butanol titer over control batch cultivation in which inhibitors were added prior to inoculation.ConclusionProperly timed sequential feeding effectively prevented acid-crash and enabled utilization of otherwise toxic substrate. This study unequivocally demonstrates that an appropriate biotechnological process control strategy can fully eliminate the negative effects of lignocellulose-derived inhibitors.Graphical

Optimizing dilute acid pretreatment for enhanced recovery and co-fermentation of hexose and pentose sugars for ethanol and butanol production

A systematic study of dilute acid pretreatment of sugarcane bagasse was performed to optimize the recovery of hexose-rich solid and pentose-rich liquid while minimizing fermentation inhibitors. Pretreatment experiments evaluated the effects of pretreatment time (10–90 min) and acid concentration (0.5–3.0 % w/w). The optimized pretreatment (1.4 % w/w sulfuric acid, 56.4 min at 121 °C) led to a solid fraction with 60.4 % cellulose and a liquid stream rich in pentose, in which 92.7 % of sugars was recovered as xylose (17.8 g/L). Besides that, low concentrations of by-products (3 g/L – the sum of acetic and formic acid, furfural, and HMF) were identified in the liquid fraction. Both fractions were integrated into enzymatic processes for further co-fermentation of C5- and C6- sugars. Two fermentative routes were evaluated: simultaneous isomerization of xylose and co-fermentation of glucose and xylulose (SIcF) for 2G ethanol production and acetone-butanol-ethanol (ABE) fermentation of glucose and xylose for biobutanol, utilizing Saccharomyces cerevisiae and Clostridium acetobutylicum, respectively. SIcF yielded 0.48 gethanol/gsugars (24 g/L ethanol) with complete glucose consumption and 58.2 % xylose conversion. ABE fermentation produced 0.36 gABE/gsugars (15.7 g/L ABE and 9.5 g/L butanol), with 96 % glucose consumption and 29.6 % xylose conversion. The proof-of-concept demonstrated that the hydrolysates were satisfactorily fermentable by microorganisms, thus validating the pretreatment optimization for fermentation applications.

Molecular Markers and Regulatory Networks in Solventogenic Clostridium Species: Metabolic Engineering Conundrum

Solventogenic Clostridium species are important for establishing the sustainable industrial bioproduction of fuels and important chemicals such as acetone and butanol. The inherent versatility of these species in substrate utilization and the range of solvents produced during acetone butanol–ethanol (ABE) fermentation make solventogenic Clostridium an attractive choice for biotechnological applications such as the production of fuels and chemicals. The functional qualities of these microbes have thus been identified to be related to complex regulatory networks that play essential roles in modulating the metabolism of this group of bacteria. Yet, solventogenic Clostridium species still struggle to consistently achieve butanol concentrations exceeding 20 g/L in batch fermentation, primarily due to the toxic effects of butanol on the culture. Genomes of solventogenic Clostridium species have a relatively greater prevalence of genes that are intricately controlled by various regulatory molecules than most other species. Consequently, the use of genetic or metabolic engineering strategies that do not consider the underlying regulatory mechanisms will not be effective. Several regulatory factors involved in substrate uptake/utilization, sporulation, solvent production, and stress responses (Carbon Catabolite Protein A, Spo0A, AbrB, Rex, CsrA) have been identified and characterized. In this review, the focus is on newly identified regulatory factors in solventogenic Clostridium species, the interaction of these factors with previously identified molecules, and potential implications for substrate utilization, solvent production, and resistance/tolerance to lignocellulose-derived microbial inhibitory compounds. Taken together, this review is anticipated to highlight the challenges impeding the re-industrialization of ABE fermentation, and inspire researchers to generate innovative strategies for overcoming these obstacles.

Integrated catalytic approach for advanced biofuel production from renewable ABE fermentation

This study focuses on advancing the production of sustainable aviation biofuels by employing a one-pot integrated catalytic approach to convert Clostridium beijerinckii strain SR-44 ABE fermentation products into higher-value compounds, specifically ketones, using Pd/Ni@BNNS bimetallic catalysts. The influence of various parameters, such as salting-out agents, temperature, catalyst loading, and reaction time, significantly improved the ABE conversion to 98% with 86% higher ketone (C5–C11) selectivity. Furthermore, the heterogeneity and recyclability of the Pd/Ni @BNNSs catalyst were investigated, confirming its suitability for industrial-scale applications. By advancing biofuel synthesis technology and overcoming the drawbacks of conventional biofuels, this study contributes to the mitigation of the environmental and energy challenges facing the aviation industry.

Understanding the dewatering of fermentation-based 1,3-propanediol with acetone before cyclohexanone synthesis

Acetone can be produced by microbial fermentation using Clostridium acetobutylicum (acetone-n-butanol-ethanol fermentation, ABE fermentation), but it provides a mixture of acetone, 1-butanol, and ethanol. N-butanol and ethanol can be used as biofuels, but high-value applications of acetone generally require upgrading. Bio-based 1,3-propanediol is more readily produced by fermentation and separated at higher titers and has been used industrially. Therefore, the coupled upgrading of the two fermentation products can provide another avenue for high-value utilization of acetone. In this paper, salting-out extraction of 1,3-propanediol with acetone was carried out, and 1,3-propanediol and acetone would spontaneously form an organic phase, thus reducing the energy consumption in the 1,3-propanediol separation process. As the double alkylation reaction of acetone with equivalent 1,3-propanediol would generate cyclohexanone, the extraction of 1,3-propanediol with acetone can provide new insight into the process intensification (removing water, salt and water concentrated in the aqueous phase) for the 1,3-propanediol separation and conversion.

Acetone-Butanol-Ethanol (ABE) fermentation with clostridial co-cultures for enhanced biobutanol production

This study has addressed the issue of enhanced biobutanol production through Consolidated Bioprocessing, with the use of clostridial co-cultures combining C. acetobutylicum (Cac) and C. pasteurianum (Cpa). To begin with, the total Acetone-Butanol-Ethanol (ABE) solvent production and butanol selectivity of individual clostridial cultures grown on different carbon sources present in lignocellulosic hydrolysates. Thereafter, statistical optimization of ABE fermentation with co-culture system was carried out using Box-Behnken design. The optimization variables were Cac to Cpa inoculum ratio (X1 in mL mL−1), sodium concentration in the medium (X2 g L−1), and xylose/glucose ratio (X3 g g−1 L L−1), whereas response variables were butanol titre (Y1 in g L−1), biomass growth (Y2 OD600), total ABE titre (Y3 in g L−1). Maximum values of the response variables with the corresponding set of optimization parameters were as follows: Y1, max = 12.1 ± 0.45 (for X1 = 0.30, X2 = 5.90, X3 = 0), Y2, max = 4.15 ± 0.03 (for X1 = 0.3, X2 = 2.42, X3 = 0.14), Y3, max = 23.1 ± 0.55 (for X1 = 0.46, X2 = 6.36, X3 = 0). The study demonstrated a substantial ≈ 22% and 61% increment in butanol titre in co-culture system compared to individual fermentations with Cac and Cpa grown on pure glucose, respectively.

Pilot-scale acetone-butanol-ethanol fermentation from corn stover

Biobutanol is an advanced biofuel that can be produced from excess lignocellulose via acetone-butanol-ethanol (ABE) fermentation. Although significant technological progress has been made in this field, attempts at large-scale lignocellulosic ABE production remain scarce. In this study, 1 m3 scale ABE fermentation was investigated using high inhibitor tolerance Clostridium acetobutylicum ABE-P1201 and steam-exploded corn stover hydrolysate (SECSH). Before expanding the fermentation scale, the detoxification process for SECSH was simplified by process engineering. Results revealed that appropriate pH management during the fed-batch cultivation could largely decrease the inhibition of the toxic components in undetoxified SECSH to the solventogenesis phase of the ABE-P1201 strains, avoiding “acid crash”. Therefore, after naturalizing the pH by Ca(OH)2, the undetoxified SECSH, without removal of the solid components, reached 17.68 ± 1.30 g/L of ABE production with 0.34 ± 0.01 g/g of yield in 1 L scale bioreactor. Based on this strategy, the fermentation scale gradually expanded from laboratory-scale apparatus to pilot-scale bioreactors. Finally, 17.05 ± 1.20 g/L of ABE titer and 0.32 ± 0.01 g/g of ABE yield were realized in 1 m3 bioreactor, corresponding to approximately 145 kg of ABE production from 1 t of dry corn stover. The pilot-scale ABE fermentation demonstrated excellent stability during repeated operations. This study provided a simplified ABE fermentation strategy and verified the feasibility of the pilot process, providing tremendous significance and a solid foundation for the future industrialization of second-generation ABE plants.

Decoupling acidogenic cascade via bio-electrogenic induced ABE pathway for enhanced n-butanol synthesis in Clostridium acetobutylicum ATCC-824: Bioenergetics and gene expression analysis

This investigation scrutinized the quantitative aspects of biobutanol production in conventional and bioelectrogenic induced ABE fermentation using Clostridium acetobutylicum ATCC-824. The primary objective of the study was to investigate how alterations in the extracellular redox potential (-0.4 V vs. Ag/AgCl (3.5 M KCl)) affect the hetero-fermentation towards the production of acetone, butanol, and ethanol during the bi-phasic fermentation, utilizing different glucose concentrations from 20 g/L − 60 g/L. The study showed significant results with 68.86 % increased butanol titer (6.67 g/L) compared to conventional fermentation (3.95 g/L butanol). Additionally, the acetone production also increased to 2.34 g/L as compared to conventional fermentation (1.96 g/L). Furthermore, gene expression and network analysis showed that various ABE pathway genes were significantly up or down regulated during the bi-phasic fermentation, indicating a difference between the conventional and EF reactors. The external potential influenced the overexpression of genes like pta, crt, bcd, ask, adh (CA_C1574), and hbd (CA_C3375), while simultaneously downregulation of buk gene, suggesting the acidogenic decoupling and transition from cold channel (butyric acid) towards hot channel pathway (directly from acetyl CoA through butyryl-CoA) for improved butanol production. Moreover, the study also revealed that entropy and enthalpy changes played a significant role in butanol production and ABE fermentation. The EF showed more negative free energy (-3.33 × 104 kJ/mol) when compared with conventional fermentation (-2.8 × 104 kJ/mol) suggesting the mechanism to be more spontaneous and viable. Overall, this study provided evidence of metabolic rerouting with non-genetic approach by regulating electron flow, culminating in an impact on the bi-phasic fermentation towards specific metabolites.

Sustainability and life cycle analyzes of different biofuel from municipal solid waste processes: an effective environmental guidance

Abstract The refining of biowaste into biofuels, particularly focusing on the organic fraction-municipal solid waste (OF-MSW), remains nascent and is influenced by factors such as energy requirements, microbial effectiveness, and structural design. This article presents a sustainable and thorough framework for evaluating the environmental behavior associated with diverse biofuel from OF-MSW conversion methodologies. The evaluation considers three different pre-treatment methods (acetone organosolv, hot water, and acidic pre-treatment), several fermentation techniques (including ethanol fermentation and ABE-F (acetone/butanol/ethanol fermentation)), and acidic or enzymatic hydrolysis approaches. Furthermore, the environmental analysis utilizes the life cycle analysis (LCA) approach. Within this framework, a consequential LCA is implemented, which includes process development to address the issue of multi-functionality and the use of marginal processes for designing foundational processes. The biofuels produced, ethanol and butanol, are analyzed for their environmental impact. To discern the varying and combined effects, methodologies for sensitivity analysis and single score evaluations have been established. Research outcomes suggest that the acetone–ethanol–butanol fermentation scenario does not provide an optimal environmental outcome due to its inability to offset the environmental impacts through the benefits derived from the byproducts. Among the scenarios examined, Scenario SC-IV emerged as the most environmentally beneficial, showing significant net environmental savings including decrements of −854.55 PDF m−2 (potentially disappeared fraction, annually), −253.74 kg CO2.eq per 1000 kg of OF-MSW, and − 3290 MJ per 1000 kg of OF-MSW treated.

Effects of Temperature, pH, and Agitation on Growth and Butanol Production of Clostridium acetobutylicum, Clostridium beijerinckii, and Clostridium saccharoperbutylacetonicum

Abstract Butanol is a promising alternative to fossil-derived fuels. Clostridium genus bacteria are known for their ability to produce butanol as one of the metabolites, however, at the moment this solution is not economically viable. To solve it, the process of butanol production should be optimized. While ABE fermentation has been extensively studied, information about the optimal growth conditions for specific microorganisms often differs from one study to another. Therefore, this study aims to search for optimal growth conditions in sealed serum bottle tests for three widely used strains in ABE fermentation. In this study effects of temperature, pH, and agitation were tested on Clostridium acetobutylicum, Clostridium beijerinckii, and Clostridium saccharoperbutylacetonicum. The optimal temperature for C. beijerinckii growth and butanol production was 32 °C, the optimal agitation speed for growth was 0 rpm, but for butanol production, it was 200 rpm. For C. saccharoperbutylacetonicum growth and butanol production pH 7.5, 30 °C temperature and an agitation rate of 100 rpm were optimal, however, this effect was slight. For C. acetobutylicum cultivation optimal temperature, pH, and agitation rate were respectively 37 °C, 6.5, and 200 rpm.

Waste valorization through acetone-butanol-ethanol (ABE) fermentation

BackgroundBiobutanol, produced through acetone-butanol-ethanol (ABE) fermentation, has been proposed for use as a transportation fuel and for the development of butanol-based materials. However, the economic viability of ABE fermentation is heavily dependent on the cost of raw materials. MethodsThis study assesses various carbon and nitrogen sources for ABE fermentation. Carbon sources examined include local molasses (M1), Thai molasses (M2), Taiwan sugar agricultural molasses (M3), and Taiwan sugar edible molasses (M4). Nitrogen sources considered are corn steep liquor (CSL), acid-hydrolyzed black soldier fly larval meal (IA), and enzyme-hydrolyzed black soldier fly larval meal (IE). Significant findingsOur findings reveal that M2CSL, a combination of Thai molasses and corn steep liquor, serves as a cost-effective and efficient medium for ABE fermentation, resulting in a butanol concentration of 7.4 ± 3.5 g/L. Furthermore, our research identifies variations in molasses and their impact on sucrose consumption inhibition. Notably, this study underscores the potential of insect peptone derived from enzyme-hydrolyzed black soldier fly larval meal (IE) as an alternative nitrogen source, while cautioning against the use of insect peptone obtained from acid-hydrolyzed black soldier fly larval meal (IA) due to its inhibitory properties.

Developing a high-rate ABE fermentation system for rice straw: CSTR with immobilization on granular-activated carbon with ex situ pervaporation

This study assessed the performance of two continuous stirred tank reactors (CSTRs) to immobilize Clostridium acetobutylicum DSM 792 and Clostridium beijerinckii DSM 6422 on granular activated carbon. Dilution rates (D) from 0.05 to 0.60 h−1 were tested using a sugar mixture to mimic rice straw hydrolysate. Immobilization was shown to be a highly effective technique for processing high flows without cell washout. Both CSTRs demonstrated significantly higher butanol productivity than their free-cell counterparts, achieving the remarkable value of 2.29 g L−1 h−1 with C. beijerinckii at D = 0.60 h−1. Rice straw hydrolysate was fed to the high-rate CSTR, reaching a butanol productivity of 2.07 g L−1 h−1 at D = 0.30 h−1. A novel downstream configuration of ex situ gas stripping followed by two pervaporation cycles operated under rough vacuum was explored in discontinuous mode, that reduced the energy demand by 63 % of conventional distillation methods. This configuration holds great promise for the advance of the lignocellulosic biorefinery process.

Trifluoroethyl Acrylate-Substituted Polymethylsiloxane—a Promising Membrane Material for Separating an ABE Fermentation Mixture

Trifluoroethyl Acrylate-Substituted Polymethylsiloxane—a Promising Membrane Material for Separating an ABE Fermentation Mixture

NADH-based kinetic model for acetone-butanol-ethanol production by Clostridium

We present in this work a kinetic model of the acetone-butanol-ethanol (ABE) fermentation based on enzyme kinetics expressions. The model includes the effect of the co-substrate NADH as a modulating factor of cellular metabolism. The simulations obtained with the model showed an adequate fit to the experimental data reported by several authors, matching or improving the results observed with previous models. In addition, this model does not require artificial mathematical strategies such as on-off functions to achieve a satisfactory fit of the ABE fermentation dynamics. The parametric sensitivity allowed to identify the direct glucose → acetyl-CoA → butyryl-CoA pathway as being more significant for butanol production than the acid re-assimilation pathway. Likewise, model simulations showed that the increase in NADH, due to glucose concentration, favors butanol production and selectivity, finding a maximum selectivity of 3.6, at NADH concentrations above 55 mM and glucose concentration of 126 mM. The introduction of NADH in the model would allow its use for the analysis of electrofermentation processes with Clostridium, since the model establishes a basis for representing changes in the intracellular redox potential from extracellular variables.

Optimising microalgae-derived butanol yield

Rapid global urbanisation emphasises the necessity to explore sustainable energy resources to fulfill escalating energy demands. Biobutanol emerges as a promising biofuel due to heightened energy density and molecular similarity to petrol. Microalgae, rich in carbohydrates, offer a potential glucose source for biobutanol fermentation. The current study shows that varying CO2 concentrations affect carbohydrate content in the biomass of P. kessleri bh-2 and Scenedesmus sp.k-7. The introduction of 1% CO2 significantly improved carbohydrate productivity, reaching 74.5% for P. kessleribh-2 and 71.0% for Scenedesmus sp.k-7. Enzymatic hydrolysis was found to be most effective for ABE fermentation, with optimal results obtained at enzyme loads of 8 mg g−1 cellulase and 2 mg g−1 amylase for both strains. When C. acetobutylicum cells were cultivated with pretreated P. kessleribh-2 biomass, the biobutanol yield amounted to 4.8 gL-1 at a glucose concentration of 5.30 gL-1, demonstrating strain's superior performance compared to Scenedesmus sp.k-7.

Lignocellulosic ethanol and butanol production by Saccharomyces cerevisiae and Clostridium beijerinckii co-culture using non-detoxified corn stover hydrolysate

Considering global economic and environmental –benefits, green renewable biofuels such as ethanol and butanol are considered as sustainable alternatives to fossil fuels. Thus, developing a co-culture strategy for ethanol and butanol production by Saccharomyces cerevisiae and Clostridium beijerinckii has emerged as a promising approach for biofuel production from lignocellulosic biomass. This study developed a co-culture of S. cerevisiae and C. beijerinckii for ethanol and butanol production from non-detoxified corn stover hydrolysate. By firstly inoculating 3 % S. cerevisiae and then 7 % C. beijerinckii with 8–10 h time intervals, the optimized co-culture process gave 24.0 g/L ABE (20.8 g/L ethanol and 2.4 g/L butanol), obtaining ABE yield and productivity of 0.421 g/g and 0.55 g/L/h. The demonstrated co-culture strategy made full use of hexose and pentose in hydrolysate and contributed to total yield and efficiency compared to conventional ethanol or ABE fermentation, indicating its great potential for developing economically feasible and sustainable bioalcohols production.