Physiological response of Clostridium carboxidivorans during conversion of synthesis gas to solvents in a gas-fed bioreactor

Clostridium carboxidivorans P7 is one of three microbial catalysts capable of fermenting synthesis gas (mainly CO, CO₂, and H₂) to produce the liquid biofuels ethanol and butanol. Gasification of feedstocks to produce synthesis gas (syngas), followed by microbial conversion to solvents, greatly expands the diversity of suitable feedstocks that can be used for biofuel production beyond commonly used food and energy crops to include agricultural, industrial, and municipal waste streams. C. carboxidivorans P7 uses a variation of the classic Wood–Ljungdahl pathway, identified through genome sequence‐enabled approaches but only limited direct metabolic analyses. As a result, little is known about gene expression and enzyme activities during solvent production. In this study, we measured cell growth, gene expression, enzyme activity, and product formation in autotrophic batch cultures continuously fed a synthetic syngas mixture. These cultures exhibited an initial phase of growth, followed by acidogenesis that resulted in a reduction in pH. After cessation of growth, solventogenesis occurred, pH increased and maximum concentrations of acetate (41 mM), butyrate (1.4 mM), ethanol (61 mM), and butanol (7.1 mM) were achieved. Enzyme activities were highest during the growth phase, but expression of carbon monoxide dehydrogenase (CODH), Fe‐only hydrogenases and two tandem bi‐functional acetaldehyde/alcohol dehydrogenases were highest during specific stages of solventogenesis. Several amino acid substitutions between the tandem acetaldehyde/alcohol dehydrogenases and the differential expression of their genes suggest that they may have different roles during solvent formation. The data presented here provide a link between the expression of key enzymes, their measured activities and solvent production by C. carboxidivorans P7. This research also identifies potential targets for metabolic engineering efforts designed to produce higher amounts of ethanol or butanol from syngas. Biotechnol. Bioeng. 2012; 109: 2720–2728. © 2012 Wiley Periodicals, Inc.     

Genomic analysis of carbon monoxide utilization and butanol production by Clostridium carboxidivorans strain P7

Increasing demand for the production of renewable fuels has recently generated a particular interest in microbial production of butanol. Anaerobic bacteria, such as Clostridium spp., can naturally convert carbohydrates into a variety of primary products, including alcohols like butanol. The genetics of microorganisms like Clostridium acetobutylicum have been well studied and their solvent-producing metabolic pathways characterized. In contrast, less is known about the genetics of Clostridium spp. capable of converting syngas or its individual components into solvents. In this study, the type of strain of a new solventogenic Clostridium species, C. carboxidivorans, was genetically characterized by genome sequencing. C. carboxidivorans strain P7(T) possessed a complete Wood-Ljungdahl pathway gene cluster, involving CO and CO(2) fixation and conversion to acetyl-CoA. Moreover, with the exception of an acetone production pathway, all the genetic determinants of canonical ABE metabolic pathways for acetate, butyrate, ethanol and butanol production were present in the P7(T) chromosome. The functionality of these pathways was also confirmed by growth of P7(T) on CO and production of CO(2) as well as volatile fatty acids (acetate and butyrate) and solvents (ethanol and butanol). P7(T) was also found to harbour a 19 Kbp plasmid, which did not include essential or butanol production related genes. This study has generated in depth knowledge of the P7(T) genome, which will be helpful in developing metabolic engineering strategies to improve C. carboxidivorans's natural capacity to produce potential biofuels from syngas.     

Genome Sequence of the Solvent-Producing Bacterium Clostridium carboxidivorans Strain P7T

Clostridium carboxidivorans strain P7^T is a strictly anaerobic acetogenic bacterium that produces acetate, ethanol, butanol, and butyrate. The C. carboxidivorans genome contains all the genes for the carbonyl branch of the Wood-Ljungdahl pathway for CO₂ fixation, and it encodes enzymes for conversion of acetyl coenzyme A into butanol and butyrate.Clostridium carboxidivorans strain P7^T (equivalent to ATCC BAA-624^T and DSM 15243^T) is an obligate anaerobe that can grow autotrophically with H₂ and CO₂ or CO (fixing carbon via the Wood-Ljungdahl pathway), or it can grow chemoorganotrophically with simple sugars (1). Acetate, ethanol, butanol, and butyrate are end products of metabolism.For slow-growing strict anaerobes such as Clostridium carboxidivorans, genome sequencing provides a rapid theoretical characterization of its metabolism compared to traditional methods. We isolated and amplified genomic C. carboxidivorans DNA using the Wizard genomic DNA purification kit (Promega, Madison, WI) and the REPLI-g kit (Qiagen). A single shotgun pyrosequencing run using a Genome Sequencer FLX system (454 Life Sciences, Branford, CT) resulted in 429,680 high-quality reads (mean read length, 231.6 bp) that were assembled using Newbler software (454 Life Sciences) into 225 contigs >500 bp long. Paired-end sequencing produced 111,154 reads (mean read length, 256.3 bp). Assembly of the paired-end and shotgun reads produced 73 scaffolds containing 216 large contigs with a mean sequence depth of 16.33 reads. PCR amplification and Sanger sequencing were conducted, followed by scaffold assembly using Sequencher (Gene Codes, Ann Arbor, MI). The 4.4-Mb final assembly has 33 scaffolds containing 69 contigs with a Phred-equivalent quality score of 40 or above (accuracy, >99.99%) (GenBank accession no. {"type":"entrez-nucleotide","attrs":{"text":"ADEK00000000","term_id":"295883218","term_text":"ADEK00000000"}}ADEK00000000).The sequence was annotated using Annotation Engine (J. Craig Venter Institute) and manually curated using Manatee (http://manatee.sourceforge.net/). The genome has 29.7% G+C content and contains 4,174 protein-coding sequences, 3 rRNA operons, 1 tmRNA (dual tRNA-like and mRNA-like nature), 6 noncoding RNAs (ncRNAs), and 48 tRNA genes. (6). Comparison of 16S rRNA genes showed that C. carboxidivorans is closely related to Clostridium scatologenes ATCC 25775^T (97% sequence identity) and Clostridium drakei type strain SL1^T (99% sequence identity). C. carboxidivorans shares 94% 16S rRNA sequence identity with Clostridium ljungdahlii (4.6 Mb), another solventogenic species.Pathway analyses indicated that C. carboxidivorans is similar to other anaerobic acetogens, such as Moorella thermoacetica (8), in having an incomplete reductive tricarboxylic acid (TCA) cycle where fumarate reductase is absent. Like other acetogenic clostridia, C. carboxidivorans uses the Wood-Ljungdahl pathway for fixing carbon dioxide to organic carbon via acetyl coenzyme A (acetyl-CoA) (5). Two of these genes encode carbon monoxide dehydrogenase (CODH) and acetyl-CoA synthase (ACS), which form a complex to catalyze the carbonyl branch of the pathway for carbon fixation and acetyl-CoA production. C. carboxidivorans has genes that encode phosphotransacetylase and acetate kinase for converting acetyl-CoA into acetate, yielding ATP (2).C. carboxidivorans is unique among other known acetogenic clostridia because it can fix carbon via the Wood-Ljungdahl pathway and convert acetyl-CoA into butanol, which is more energy dense than ethanol. Both C. carboxidivorans and Clostridium acetobutylicum encode NADPH-dependent butanol dehydrogenase (74% identity) to convert acetyl-CoA into butanol (3, 4), but C. acetobutylicum cannot fix CO₂ or CO into acetyl-CoA. Conversely, C. ljungdahlii can fix CO and CO₂, but it lacks butanol dehydrogenase and cannot convert acetyl-CoA into butanol. Therefore, P7 includes beneficial properties of both these industrially important strains. The genome sequence of C. carboxidivorans P7 could potentially accelerate research allowing its industrial application for biofuel production or to enable some of its pathways to be used directly in synthetic biology for biofuel production.     

Deciphering mixotrophic Clostridium formicoaceticum metabolism and energy conservation: Genomic analysis and experimental studies

Clostridium formicoaceticum, a Gram-negative mixotrophic homoacetogen, produces acetic acid as the sole metabolic product from various carbon sources, including fructose, glycerol, formate, and CO₂. Its genome of 4.59-Mbp contains a highly conserved Wood-Ljungdahl pathway gene cluster with the same layout as that in other mixotrophic acetogens, including Clostridium aceticum, Clostridium carboxidivorans, and Clostridium ljungdahlii. For energy conservation, C. formicoaceticum does not have all the genes required for the synthesis of cytochrome or quinone used for generating proton gradient in H⁺-dependent acetogens such as Moorella thermoacetica; instead, it has the Rnf system and a Na⁺-translocating ATPase similar to the one in Acetobacterium woodii. Its growth in both heterotrophic and autotrophic media were dependent on the sodium concentration. C. formicoaceticum has genes encoding acetaldehyde dehydrogenases, alcohol dehydrogenases, and aldehyde oxidoreductases, which could convert acetyl-CoA and acetate to ethanol and butyrate to butanol under excessive reducing equivalent conditions.     

Intracellular metabolite profiling and the evaluation of metabolite extraction solvents for Clostridium carboxidivorans fermenting carbon monoxide

Clostridium carboxidivorans ferments CO, CO₂, and H₂ via the Wood-Ljungdahl pathway. CO, CO_2, and H₂ are unique substrates, unlike other carbon sources like glucose, so it is necessary to analyze intracellular metabolite profiles for gas fermentation by C. carboxidivorans for metabolic engineering. Moreover, it is necessary to optimize the metabolite extraction solvent specifically for C. carboxidivorans fermenting syngas. In comparison with glucose media, the gas media allowed significant abundance changes of 38 and 34 metabolites in the exponential and stationary phases, respectively. Especially, C. carboxidivorans cultivated in the gas media showed changes of fatty acid metabolism and higher levels of intracellular fatty acid synthesis possibly due to cofactor imbalance and slow metabolism. Meanwhile, the evaluation of extraction solvents revealed the mixture of water-isopropanol-methanol (2:2:5, v/v/v) to be the best extraction solvent, which showed a higher extraction capability and reproducibility than pure methanol, the conventional extraction solvent. This is the first metabolomic study to demonstrate the unique intracellular metabolite profiles of the gas fermentation compared to glucose fermentation, and to evaluate water-isopropanol-methanol as the optimal metabolite extraction solvent for C. carboxidivorans on gas fermentation.     

Effects of zinc on the production of alcohol by <Emphasis Type="Italic">Clostridium carboxidivorans</Emphasis> P7 using model syngas

Renewable energy, including biofuels such as ethanol and butanol from syngas bioconversed by Clostridium carboxidivorans P7, has been drawing extensive attention due to the fossil energy depletion and global eco-environmental issues. Effects of zinc on the growth and metabolites of C. carboxidivorans P7 were investigated with model syngas as the carbon source. The cell concentration was doubled, the ethanol content increased 3.02-fold and the butanol content increased 7.60-fold, the hexanol content increased 44.00-fold in the medium with 280 μM Zn²⁺, when comparing with those in the control medium [Zn²⁺, (7 μM)]. Studies of the genes expression involved in the carbon fixation as well as acid and alcohol production in the medium with 280 μM Zn²⁺ indicated that fdhII was up-regulated on the second day, acs A, fdhII, bdh35 and bdh50 were up-regulated on the third day and bdh35, acsB, fdhI, fdhIII, fdhIV, buk, bdh10, bdh35, bdh40 and bdh50 were up-regulated on the fourth day. The results indicated that the increased Zn²⁺ content increased the alcohol production through increase in the gene expression of the carbon fixation and alcohol dehydrogenase.     

Production of biofuels from C1-gases with Clostridium and related bacteria—Recent advances

Clostridium spp. are suitable for the bioconversion of C₁-gases (e.g., CO₂, CO and syngas) into different bioproducts. These products can be used as biofuels and are reviewed here, focusing on ethanol, butanol and hexanol, mainly. The production of higher alcohols (e.g., butanol and hexanol) has hardly been reviewed. Parameters affecting the optimization of the bioconversion process and bioreactor performance are addressed as well as the pathways involved in these bioconversions. New aspects, such as mixotrophy and sugar versus gas fermentation, are also reviewed. In addition, Clostridia can also produce higher alcohols from the integration of the Wood-Ljungdahl pathway and the reverse ß-oxidation pathway, which has also not yet been comprehensively reviewed. In the latter process, the acetogen uses the reducing power of CO/syngas to reduce C₄ or C₆ fatty acids, previously produced by a chain elongating microorganism (commonly Clostridium kluyveri), into the corresponding bioalcohol.     

In silico metabolic engineering of Clostridium ljungdahlii for synthesis gas fermentation

Synthesis gas fermentation is one of the most promising routes to convert synthesis gas (syngas; mainly comprised of H₂ and CO) to renewable liquid fuels and chemicals by specialized bacteria. The most commonly studied syngas fermenting bacterium is Clostridium ljungdahlii, which produces acetate and ethanol as its primary metabolic byproducts. Engineering of C. ljungdahlii metabolism to overproduce ethanol, enhance the synthesize of the native byproducts lactate and 2,3-butanediol, and introduce the synthesis of non-native products such as butanol and butyrate has substantial commercial value. We performed in silico metabolic engineering studies using a genome-scale reconstruction of C. ljungdahlii metabolism and the OptKnock computational framework to identify gene knockouts that were predicted to enhance the synthesis of these native products and non-native products, introduced through insertion of the necessary heterologous pathways. The OptKnock derived strategies were often difficult to assess because increase product synthesis was invariably accompanied by decreased growth. Therefore, the OptKnock strategies were further evaluated using a spatiotemporal metabolic model of a syngas bubble column reactor, a popular technology for large-scale gas fermentation. Unlike flux balance analysis, the bubble column model accounted for the complex tradeoffs between increased product synthesis and reduced growth rates of engineered mutants within the spatially varying column environment. The two-stage methodology for deriving and evaluating metabolic engineering strategies was shown to yield new C. ljungdahlii gene targets that offer the potential for increased product synthesis under realistic syngas fermentation conditions.     

In situ hydrogen utilization for high fraction acetate production in mixed culture hollow-fiber membrane biofilm reactor

Syngas fermentation is a promising route for resource recovery. Acetate is an important industrial chemical product and also an attractive precursor for liquid biofuels production. This study demonstrated high fraction acetate production from syngas (H₂ and CO₂) in a hollow-fiber membrane biofilm reactor, in which the hydrogen utilizing efficiency reached 100 % during the operational period. The maximum concentration of acetate in batch mode was 12.5 g/L, while the acetate concentration in continuous mode with a hydraulic retention time of 9 days was 3.6?±?0.1 g/L. Since butyrate concentration was rather low and below 0.1 g/L, the acetate fraction was higher than 99 % in both batch and continuous modes. Microbial community analysis showed that the biofilm was dominated by Clostridium spp., such as Clostridium ljungdahlii and Clostridium drakei, the percentage of which was 70.5 %. This study demonstrates a potential technology for the in situ utilization of syngas and valuable chemical production.     

Mevalonate production by engineered acetogen biocatalyst during continuous fermentation of syngas or CO2/H2 blend

Naturally mevalonate-resistant acetogen Clostridium sp. MT1243 produced only 425 mM acetate during syngas fermentation. Using Clostridium sp. MT1243 we engineered biocatalyst selectively producing mevalonate from synthesis gas or CO₂/H₂ blend. Acetate production and spore formation were eliminated from Clostridium sp. MT1243 using Cre-lox66/lox71-system. Cell energy released via elimination of phosphotransacetylase, acetate kinase and early stage sporulation genes powered mevalonate accumulation in fermentation broth due to expression of synthetic thiolase, HMG-synthase, and HMG-reductase, three copies of each, integrated using Tn7-approach. Recombinants produced 145 mM mevalonate in five independent single-step fermentation runs 25 days each in five repeats using syngas blend 60 % CO and 40 % H₂ (v/v) (p < 0.005). Mevalonate production was 97 mM if only CO₂/H₂ blend was fed instead of syngas (p < 0.005). Mevalonate from CO₂/H₂ blend might serve as a commercial route to mitigate global warming in proportion to CO₂ fermentation scale worldwide.     

Improvement of butanol production in <Emphasis Type="Italic">Clostridium acetobutylicum</Emphasis> through enhancement of NAD(P)H availability

Clostridium acetobutylicum is a natural producer of butanol, butyrate, acetone and ethanol. The pattern of metabolites reflects the partitioning of redox equivalents between hydrogen and carbon metabolites. Here the exogenous genes of ferredoxin-NAD(P)⁺ oxidoreductase (FdNR) and trans-enoyl-coenzyme reductase (TER) are introduced to three different Clostridium acetobutylicum strains to investigate the distribution of redox equivalents and butanol productivity. The FdNR improves NAD(P)H availability by capturing reducing power from ferredoxin. A butanol production of 9.01 g/L (36.9% higher than the control), and the highest ratios of butanol/acetate (7.02) and C₄/C₂ (3.17) derived metabolites were obtained in the C acetobutylicum buk^- strain expressing FdNR. While the TER functions as an NAD(P)H oxidase, butanol production was decreased in the C. acetobutylicum strains containing TER. The results illustrate that metabolic flux can be significantly changed and directed into butanol or butyrate due to enhancement of NAD(P)H availability by controlling electron flow through the ferredoxin node.     

Control of Carbon and Electron Flow in Clostridium acetobutylicum Fermentations: Utilization of Carbon Monoxide to Inhibit Hydrogen Production and to Enhance Butanol Yields

Extracts prepared from non-solvent-producing cells of Clostridium acetobutylicum contained methyl viologen-linked hydrogenase activity (20 U/mg of protein at 37°C) but did not display carbon monoxide dehydrogenase activity. CO addition readily inhibited the hydrogenase activity of cell extracts or of viable metabolizing cells. Increasing the partial pressure of CO (2 to 10%) in unshaken anaerobic culture tube headspaces significantly inhibited (90% inhibition at 10% CO) both growth and hydrogen production by C. acetobutylicum. Growth was not sensitive to low partial pressures of CO (i.e., up to 15%) in pH-controlled fermentors (pH 4.5) that were continuously gassed and mixed. CO addition dramatically altered the glucose fermentation balance of C. acetobutylicum by diverting carbon and electrons away from H₂, CO₂, acetate, and butyrate production and towards production of ethanol and butanol. The butanol concentration was increased from 65 to 106 mM and the butanol productivity (i.e., the ratio of butanol produced/total acids and solvents produced) was increased by 31% when glucose fermentations maintained at pH 4.5 were continuously gassed with 85% N₂-15% CO versus N₂ alone. The results are discussed in terms of metabolic regulation of C. acetobutylicum saccharide fermentations to achieve maximal butanol or solvent yield.     

In silico analysis of <Emphasis Type="Italic">Clostridium acetobutylicum</Emphasis> ATCC 824 metabolic response to an external electron supply

The biological production of butanol has become an important research field and thanks to genome sequencing and annotation; genome-scale metabolic reconstructions have been developed for several Clostridium species. This work makes use of the iCAC490 model of Clostridium acetobutylicum ATCC 824 to analyze its metabolic capabilities and response to an external electron supply through a constraint-based approach using the Constraint-Based Reconstruction Analysis Toolbox. Several analyses were conducted, which included sensitivity, production envelope, and phenotypic phase planes. The model showed that the use of an external electron supply, which acts as co-reducing agent along with glucose-derived reducing power (electrofermentation), results in an increase in the butanol-specific productivity. However, a proportional increase in the butyrate uptake flux is required. Besides, the uptake of external butyrate leads to the coupling of butanol production and growth, which coincides with results reported in literature. Phenotypic phase planes showed that the reducing capacity becomes more limiting for growth at high butyrate uptake fluxes. An electron uptake flux allows the metabolism to reach the growth optimality line. Although the maximum butanol flux does not coincide with the growth optimality line, a butyrate uptake combined with an electron uptake flux would result in an increased butanol volumetric productivity, being a potential strategy to optimize the production of butanol by C. acetobutylicum ATCC 824.     

乙、丁酸添加条件下丁醇发酵图论模型的构建

有机酸代谢途径在丁醇发酵过程中具有重要的作用,对细胞内碳流的分配和产物的合成影响显著。在7 L厌氧发酵罐中,进行了间歇添加乙酸或丁酸的发酵实验。结果表明,乙、丁酸的添加显著提高了总溶剂的生产效率,分别提高了47.1%和39.2%;此外,丁醇/丙酮比在添加丁酸的批次中提高了21.7%,在添加乙酸的批次中降低了16.2%;厌氧瓶中的发酵实验也证实了以上结果。有机酸代谢计算的结果表明,乙、丁酸的添加基本上阻断了相应有机酸闭环的吸收途径。基于相关报道和代谢计算结果,构建了针对乙、丁酸添加批次的图论模型,并利用该模型对不同发酵条件下的溶剂浓度和丁醇/丙酮比进行了计算。结果表明,该模型很好地预测了实验结果,合理地构建了乙、丁酸添加批次的信号传递线图。     

Engineering Clostridium ljungdahlii as the gas-fermenting cell factory for the production of biofuels and biochemicals

Clostridium ljungdahlii is a representative autotrophic gas-fermenting acetogen capable of converting CO₂ and CO into biomass and multiple metabolites. The carbon fixation and conversion based on C. ljungdahlii have great potential for the sustainable production of bulk biochemicals and biofuels using industrial syngas and waste gases. With substantial recent advances in genetic manipulation tools, it has become possible to study and improve the metabolic capability of C. ljungdahlii in gas fermentation. The product scope of C. ljungdahlii has been expanded through the introduction of heterologous production pathways followed by the modification of native metabolic networks. In addition, progress has been made in understanding the physiological and metabolic mechanisms of this anaerobe, contributing to strain designs for expected phenotypes. In this review, we highlight the latest research progresses regarding C. ljungdahlii and discuss the next steps to comprehensively understand and engineer this bacterium for an improved bacterial gas bioconversion platform.     

Clostridium vulturis sp. nov., isolated from the intestine of the cinereous vulture (Aegypius monachus)

A Gram-stain positive, strict anaerobe, spore-forming, motile rod-shaped bacterial strain with peritrichous flagella, designated YMB-57^T, was isolated from the intestine of a cinereous vulture (Aegypius monachus) in Korea. StrainYMB-57^T was found to show optimal growth at 37 °C, pH 7.5 and 1.0 % (w/v) NaCl. Phylogenetic analysis based on the 16S rRNA gene sequence showed that strain YMB-57^T belongs to the genus Clostridium and is most closely related to the type strains of Clostridium subterminale (96.9 % sequence similarity), Clostridium thiosulfatireducens (96.7 %) and Clostridium sulfidigenes (96.6 %). The main fermentation end-products identified following growth in PYG medium were acetate, butyrate, ethanol, propanol, carbon dioxide and hydrogen. Peptone was converted to ethanol, and butanol, whereas glucose was fermented to ethanol. The major cellular fatty acids were identified as C_16:0, C_18:1 ω9c, and C_18:1 ω9c DMA and the DNA G+C content was determined to be 34.0 mol%. Phenotypic and phylogenetic differences indicate that strain YMB-57^T is distinct from other Clostridium species. It is proposed that strain YMB-57^T be classified as the type strain of a novel species of the genus Clostridium, with the name Clostridium vulturis sp. nov. The type strain is YMB-57^T (=KCTC 15114^T = JCM 17998^T).     

Acidic Conditions Are Not Obligatory for Onset of Butanol Formation by Clostridium beijerinckii (Synonym, C. butylicum)

Factors that may initiate the metabolic transition for butanol production were investigated in batch cultures of Clostridium beijerinckii (synonym, Clostridium butylicum) VPI 13436. Cultures maintained at pH 6.8 produced nearly as much butanol as those incubated without pH control, indicating that neither a change in the culture pH nor acid conditions per se are always required to initiate solvent formation. Acetate and butyrate levels at the onset of butanol production were dependent on the pH at which the cultures were maintained. Cultures maintained at pH 6.8 could be accelerated into solvent production by artificially lowering the pH to 5.0 or by the addition of acetate plus butyrate without a pH change (but neither acid alone was effective). Solvent production was associated with slower rates of growth and general metabolism, and it did not show a requirement for mature spore formation. We speculate that a slowdown in metabolism, which may be brought about by several conditions, is mechanistically related to the onset of butanol production. Extracts of solvent-producing cells contained acetoacetate decarboxylase activity as well as higher NADP⁺-linked butanol dehydrogenase and lower hydrogenase activities than extracts of acid-producing cells. Solvent production did not appear to involve an enhanced ability to catalyze H₂ oxidation.     

Improvement of butanol fermentation by supplementation of butyric acid produced from a brown alga

This study investigated butanol fermentation using glucose and culture broth containing butyrate from the butyrate fermentation of a brown alga, Laminaria japonica. Prior to the use of the biologically-produced butyrate, the initial glucose in tryptone-yeast extract acetate (TYA) medium was first optimized for butanol fermentation using Clostridium saccharoperbutylacetonicum N1-4 ATCC 27021^T. Then, a commercially-acquired (synthetic) butyrate was supplemented to the TYA medium containing the optimal glucose concentration (around 30 and 60 g/L). According to the experimental results, the highest butanol carbon yield (0.580 C-mol/C-mol) was obtained from the fermentation of 36.65 g/L glucose and 7.29 g/L synthetic butyrate. Fermentation of a similar amount of glucose (32.28 g/L) in the absence of butyrate gave a butanol carbon yield of 0.402 C-mol/C-mol. For the experiment with fermented butyrate, a 100 g/L biomass of brown alga was fermented by Clostridium tyrobutyricum ATCC 25755 and the culture broth containing butyrate was used to prepare TYA medium after removing the bacterial cells. Fermentation using the synthetic butyrate and the biologically-produced butyrate (4.95 g/L) gave a comparable butanol concentration (13.23 g/L) and butanol carbon yield (0.513 C-mol/C-mol). Overall, this study proved that the addition of fermented butyrate from brown alga fermentation could be an effective way to improve butanol production. Furthermore, the reuse of spent medium and the absence of rigorous purification of the broth containing butyrate would lower the production cost of the fermentation.     

Comparison of carbon metabolism between chloramphenicol-treated and untreated cultures of Clostridium acetobutylicum

Summary Carbon distribution from substrates to products in Clostridium acetobutylicum ATCC 824 was investigated by adding ¹⁴C-labeled substrates as tracers. Comparison of carbon conversion between chloramphenicol (CAP)-treated and untreated cultures was also studied. The percentage of ¹⁴C recovery in butanol, acetone and ethanol from uniformly labeled [¹⁴C]glucose was increased by 17, 25 and 30%, respectively, after CAP addition. The incorporation of ¹⁴C in solvents from ¹⁴C-labeled acetate and butyrate was also increased by the antibiotic treatment. A total ¹⁴C recovery of 12% in all the products from added [¹⁴C]Na₂CO₃ indicates significant heterotrophic CO₂ fixation in this microorganism. The ratio of carbon in butanol derived from glucose, acetate and butyrate was about 71:6:18, and this ratio was unchanged by CAP treatment.This paper represents contribution No. 2685 of the Rhode Island Agricultural Experimental StationCorrespondence to: R. W. Traxler     

Metabolic engineering strategies for butanol production in Escherichia coli

The global market of butanol is increasing due to its growing applications as solvent, flavoring agent, and chemical precursor of several other compounds. Recently, the superior properties of n-butanol as a biofuel over ethanol have stimulated even more interest. (Bio)butanol is natively produced together with ethanol and acetone by Clostridium species through acetone-butanol-ethanol fermentation, at noncompetitive, low titers compared to petrochemical production. Different butanol production pathways have been expressed in Escherichia coli, a more accessible host compared to Clostridium species, to improve butanol titers and rates. The bioproduction of butanol is here reviewed from a historical and theoretical perspective. All tested rational metabolic engineering strategies in E. coli to increase butanol titers are reviewed: manipulation of central carbon metabolism, elimination of competing pathways, cofactor balancing, development of new pathways, expression of homologous enzymes, consumption of different substrates, and molecular biology strategies. The progress in the field of metabolic modeling and pathway generation algorithms and their potential application to butanol production are also summarized here. The main goals are to gather all the strategies, evaluate the respective progress obtained, identify, and exploit the outstanding challenges.