Isobutanol Biosynthesis Research Articles

Electro-controlled distribution of reducing equivalents to boost isobutanol biosynthesis in microbial electro-fermentation of S. oneidensis

Electro-controlled distribution of reducing equivalents to boost isobutanol biosynthesis in microbial electro-fermentation of S. oneidensis

Efficient production of isobutanol from glycerol in Klebsiella pneumoniae: Regulation of acetohydroxyacid synthase, a rate-limiting enzyme in isobutanol biosynthesis

Glycerol is an abundant and inexpensive resource that can be used to produce valuable industrial products. Isobutanol is an important industrial chemical that has been studied for biosynthesis from various carbon sources and microorganisms. So far, isobutanol production by Klebsiella pneumoniae has mainly been studied using glucose. In this study, we produced isobutanol from glycerol based on the K. pneumoniae ΔldhAΔbudA mutant harboring pBR-iBO, which was used in a previous study with K. pneumoniae. We investigated the effect of different acetohydroxyacid synthase (AHAS) isoenzymes (rate-limiting enzymes in isobutanol biosynthesis), plasmid copy number, and different promoters as a method to increase isobutanol production through regulation at gene expression level. The K. pneumoniae Cu ΔldhAΔbudA, pUC-tac-BN-ISO strain produced 2.56-fold more isobutanol than reported previously for glycerol-derived isobutanol production. Additionally, the in vitro enzyme activity of AHAS I (ilvBN) was greater than that of the other two isoenzymes (ilvIH and ilvGM). The evaluation of process factors indicated that an agitation speed of 200 rpm with the culture maintained at pH 6.0 was a favorable condition for isobutanol production (1.02 g/L). Our results demonstrated enhanced production of isobutanol from glycerol and provide insights for future research on isobutanol production from renewable feedstock.

Increased production of isobutanol from xylose through metabolic engineering of Saccharomyces cerevisiae overexpressing transcription factor Znf1 and exogenous genes.

Only trace amount of isobutanol is produced by the native Saccharomyces cerevisiae via degradation of amino acids. Despite several attempts using engineered yeast strains expressing exogenous genes, catabolite repression of glucose must be maintained together with high activity of downstream enzymes, involving iron-sulfur assimilation and isobutanol production. Here, we examined novel roles of nonfermentable carbon transcription factor Znf1 in isobutanol production during xylose utilization. RNA-seq analysis showed that Znf1 activates genes in valine biosynthesis, Ehrlich pathway and iron-sulfur assimilation while coupled deletion or downregulated expression of BUD21 further increased isobutanol biosynthesis from xylose. Overexpression of ZNF1 and xylose-reductase/dehydrogenase (XR-XDH) variants, a xylose-specific sugar transporter, xylulokinase, and enzymes of isobutanol pathway in the engineered S. cerevisiae pho13gre3Δ strain resulted in the superb ZNXISO strain, capable of producing high levels of isobutanol from xylose. The isobutanol titer of 14.809±0.400g/L was achieved, following addition of 0.05g/L FeSO4.7H2O in 5L bioreactor. It corresponded to 155.88mg/g xylose consumed and+264.75% improvement in isobutanol yield. This work highlights a new regulatory control of alternative carbon sources by Znf1 on various metabolic pathways. Importantly, we provide a foundational step toward more sustainable production of advanced biofuels from the second most abundant carbon source xylose.

Establishment of a resource recycling strategy by optimizing isobutanol production in engineered cyanobacteria using high salinity stress

BackgroundIsobutanol is an attractive biofuel with many advantages. Third-generation biorefineries that convert CO2 into bio-based fuels have drawn considerable attention due to their lower feedstock cost and more ecofriendly refining process. Although autotrophic cyanobacteria have been genetically modified for isobutanol biosynthesis, there is a lack of stable and convenient strategies to improve their production.ResultsIn this study, we first engineered Synechococcus elongatus for isobutanol biosynthesis by introducing five exogenous enzymes, reaching a production titer of 0.126 g/L at day 20. It was then discovered that high salinity stress could result in a whopping fivefold increase in isobutanol production, with a maximal in-flask titer of 0.637 g/L at day 20. Metabolomics analysis revealed that high salinity stress substantially altered the metabolic profiles of the engineered S. elongatus. A major reason for the enhanced isobutanol production is the acceleration of lipid degradation under high salinity stress, which increases NADH. The NADH then participates in the engineered isobutanol-producing pathway. In addition, increased membrane permeability also contributed to the isobutanol production titer. A cultivation system was subsequently developed by mixing synthetic wastewater with seawater to grow the engineered cyanobacteria, reaching a similar isobutanol production titer as cultivation in the medium.ConclusionsHigh salinity stress on engineered cyanobacteria is a practical and feasible biotechnology to optimize isobutanol production. This biotechnology provides a cost-effective approach to biofuel production, and simultaneously recycles chemical nutrients from wastewater and seawater.

Co-Production of Isobutanol and Ethanol from Prairie Grain Starch Using Engineered Saccharomyces cerevisiae

Isobutanol is an important and valuable platform chemical and an appealing biofuel that is compatible with contemporary combustion engines and existing fuel distribution infrastructure. The present study aimed to compare the potential of triticale, wheat and barley starch as feedstock for isobutanol production using an engineered strain of Saccharomyces cerevisiae. A simultaneous saccharification and fermentation (SSF) approach showed that all three starches were viable feedstock for co-production of isobutanol and ethanol and could produce titres similar to that produced using purified sugar as feedstock. A fed-batch process using triticale starch yielded 0.006 g isobutanol and 0.28 g ethanol/g starch. Additionally, it is demonstrated that Fusarium graminearum infected grain starch contaminated with mycotoxin can be used as an effective feedstock for isobutanol and ethanol co-production. These findings demonstrate the potential for triticale as a purpose grown energy crop and show that mycotoxin-contaminated grain starch can be used as feedstock for isobutanol biosynthesis, thus adding value to a grain that would otherwise be of limited use.

Modulating redox metabolism to improve isobutanol production in Shimwellia blattae

BackgroundIsobutanol is a candidate to replace gasoline from fossil resources. This higher alcohol can be produced from sugars using genetically modified microorganisms. Shimwellia blattae (p424IbPSO) is a robust strain resistant to high concentration of isobutanol that can achieve a high production rate of this alcohol. Nevertheless, this strain, like most strains developed for isobutanol production, has some limitations in its metabolic pathway. Isobutanol production under anaerobic conditions leads to a depletion of NADPH, which is necessary for two enzymes in the metabolic pathway. In this work, two independent approaches have been studied to mitigate the co-substrates imbalance: (i) using a NADH-dependent alcohol dehydrogenase to reduce the NADPH dependence of the pathway and (ii) using a transhydrogenase to increase NADPH level.ResultsThe addition of the NADH-dependent alcohol dehydrogenase from Lactococcus lactis (AdhA) to S. blattae (p424IbPSO) resulted in a 19.3% higher isobutanol production. The recombinant strain S. blattae (p424IbPSO, pIZpntAB) harboring the PntAB transhydrogenase produced 39.0% more isobutanol than the original strain, reaching 5.98 g L−1 of isobutanol. In both strains, we observed a significant decrease in the yields of by-products such as lactic acid or ethanol.ConclusionsThe isobutanol biosynthesis pathway in S. blattae (p424IbPSO) uses the endogenous NADPH-dependent alcohol dehydrogenase YqhD to complete the pathway. The addition of NADH-dependent AdhA leads to a reduction in the consumption of NADPH that is a bottleneck of the pathway. The higher consumption of NADH by AdhA reduces the availability of NADH required for the transformation of pyruvate into lactic acid and ethanol. On the other hand, the expression of PntAB from E. coli increases the availability of NADPH for IlvC and YqhD and at the same time reduces the availability of NADH and thus, the production of lactic acid and ethanol. In this work it is shown how the expression of AdhA and PntAB enzymes in Shimwellia blattae increases yield from 11.9% to 14.4% and 16.4%, respectively.

Metabolic engineering of Zymomonas mobilis for anaerobic isobutanol production

BackgroundBiofuels and value-added biochemicals derived from renewable biomass via biochemical conversion have attracted considerable attention to meet global sustainable energy and environmental goals. Isobutanol is a four-carbon alcohol with many advantages that make it attractive as a fossil-fuel alternative. Zymomonas mobilis is a highly efficient, anaerobic, ethanologenic bacterium making it a promising industrial platform for use in a biorefinery.ResultsIn this study, the effect of isobutanol on Z. mobilis was investigated, and various isobutanol-producing recombinant strains were constructed. The results showed that the Z. mobilis parental strain was able to grow in the presence of isobutanol below 12 g/L while concentrations greater than 16 g/L inhibited cell growth. Integration of the heterologous gene encoding 2-ketoisovalerate decarboxylase such as kdcA from Lactococcus lactis is required for isobutanol production in Z. mobilis. Moreover, isobutanol production increased from nearly zero to 100–150 mg/L in recombinant strains containing the kdcA gene driven by the tetracycline-inducible promoter Ptet. In addition, we determined that overexpression of a heterologous als gene and two native genes (ilvC and ilvD) involved in valine metabolism in a recombinant Z. mobilis strain expressing kdcA can divert pyruvate from ethanol production to isobutanol biosynthesis. This engineering improved isobutanol production to above 1 g/L. Finally, recombinant strains containing both a synthetic operon, als-ilvC-ilvD, driven by Ptet and the kdcA gene driven by the constitutive strong promoter, Pgap, were determined to greatly enhance isobutanol production with a maximum titer about 4.0 g/L. Finally, isobutanol production was negatively affected by aeration with more isobutanol being produced in more poorly aerated flasks.ConclusionsThis study demonstrated that overexpression of kdcA in combination with a synthetic heterologous operon, als-ilvC-ilvD, is crucial for diverting pyruvate from ethanol production for enhanced isobutanol biosynthesis. Moreover, this study also provides a strategy for harnessing the valine metabolic pathway for future production of other pyruvate-derived biochemicals in Z. mobilis.

Xylose assimilation enhances the production of isobutanol in engineered Saccharomyces cerevisiae.

Bioconversion of xylose-the second most abundant sugar in nature-into high-value fuels and chemicals by engineered Saccharomyces cerevisiae has been a long-term goal of the metabolic engineering community. Although most efforts have heavily focused on the production of ethanol by engineered S. cerevisiae, yields and productivities of ethanol produced from xylose have remained inferior as compared with ethanol produced from glucose. However, this entrenched focus on ethanol has concealed the fact that many aspects of xylose metabolism favor the production of nonethanol products. Through reduced overall metabolic flux, a more respiratory nature of consumption, and evading glucose signaling pathways, the bioconversion of xylose can be more amenable to redirecting flux away from ethanol towards the desired target product. In this report, we show that coupling xylose consumption via the oxidoreductive pathway with a mitochondrially-targeted isobutanol biosynthesis pathway leads to enhanced product yields and titers as compared to cultures utilizing glucose or galactose as a carbon source. Through the optimization of culture conditions, we achieve 2.6 g/L of isobutanol in the fed-batch flask and bioreactor fermentations. These results suggest that there may be synergistic benefits of coupling xylose assimilation with the production of nonethanol value-added products.

Enhancement of photosynthetic isobutanol production in engineered cells of Synechocystis PCC 6803

BackgroundCyanobacteria, oxygenic photoautotrophic prokaryotes, can be engineered to produce various valuable chemicals from solar energy and CO2 in direct processes. The concept of photosynthetic production of isobutanol, a promising chemical and drop-in biofuel, has so far been demonstrated for Synechocystis PCC 6803 and Synechococcus elongatus PCC 7942. In Synechocystis PCC 6803, a heterologous expression of α-ketoisovalerate decarboxylase (Kivd) from Lactococcus lactis resulted in an isobutanol and 3-methyl-1-butanol producing strain. Kivd was identified as a bottleneck in the metabolic pathway and its activity was further improved by reducing the size of its substrate-binding pocket with a single replacement of serine-286 to threonine (KivdS286T). However, isobutanol production still remained low.ResultsIn the present study, we report on how cultivation conditions significantly affect the isobutanol production in Synechocystis PCC 6803. A HCl-titrated culture grown under medium light (50 μmol photons m−2 s−1) showed the highest isobutanol production with an in-flask titer of 194 mg l−1 after 10 days and 435 mg l−1 at day 40. This corresponds to a cumulative isobutanol production of 911 mg l−1, with a maximal production rate of 43.6 mg l−1 day−1 observed between days 4 and 6. Additional metabolic bottlenecks in the isobutanol biosynthesis pathway were further addressed. The expression level of KivdS286T was significantly affected when co-expressed with another gene downstream in a single operon and in a convergent oriented operon. Moreover, the expression of the ADH encoded by codon-optimized slr1192 and co-expression of IlvC and IlvD were identified as potential approaches to further enhance isobutanol production in Synechocystis PCC 6803.ConclusionThe present study demonstrates the importance of a suitable cultivation condition to enhance isobutanol production in Synechocystis PCC 6803. Chemostat should be used to further increase both the total titer as well as the rate of production. Furthermore, identified bottleneck, Kivd, should be expressed at the highest level to further enhance isobutanol production.

Elimination of biosynthetic pathways for l-valine and l-isoleucine in mitochondria enhances isobutanol production in engineered Saccharomyces cerevisiae

Saccharomyces cerevisiae has a natural ability to produce higher alcohols, making it a promising candidate for production of isobutanol. However, the several pathways competing with isobutanol biosynthesis lead to production of substantial amounts of l-valine and l-isoleucine in mitochondria and isobutyrate, l-leucine, and ethanol in cytosol. To increase flux to isobutanol by removing by-product formation, the genes associated with formation of l-valine (BAT1), l-isoleucine (ILV1), isobutyrate (ALD6), l-leucine (LEU1), and ethanol (ADH1) were disrupted to construct the S. cerevisiae WΔGBIALA1_2vec strain. This strain showed 8.9 and 8.6 folds increases in isobutanol concentration and yield, respectively, relative the corresponding values of the background strain on glucose medium. In a bioreactor fermentation with a gas trapping system, the WΔGBIALA1_2vec strain produced 662 mg/L isobutanol concentration with a yield of 6.71 mgisobutanol/gglucose. With elimination of the competing pathways, the WΔGBIALA1_2vec strain would serve as a platform strain for isobutanol production.

Improving isobutanol titers in Saccharomyces cerevisiae with over-expressing NADPH-specific glucose-6-phosphate dehydrogenase (Zwf1)

Isobutanol is a more promising biofuel than ethanol due to its higher energy density and lower hygroscopicity. Saccharomyces cerevisiae, as a model eukaryote, has the potential advantage to produce isobutanol because of its greater tolerance to higher alcohols. NADPH is a key cofactor for isobutanol synthesis, and glucose-6-phosphate dehydrogenase (Zwf1) is one of the main NADPH-supplying sources in S. cerevisiae. In this study, we investigated the effects of over-expressing ZWF1 on isobutanol titers. Our results showed that engineered strain HZAL-7023 produced 6.22 mg isobutanol per g glucose, which increased by 6.64-fold compared with the parent strain, while engineered strain HZAL-7023 22-ZWF1 produced 11.46 mg isobutanol per g glucose, which increased by 1.82-fold compared with engineered strain HZAL-7023. These results suggested that improvement of NADPH supply through over-expressing ZWF1 contributed to isobutanol biosynthesis in S. cerevisiae. These results also verified the proposed concept of increasing isobutanol titers in S. cerevisiae by resolving cofactor imbalance. Finally, this study provides a new strategy for enhancing isobutanol biosynthesis.

Heterologous expression of bacterial phosphoenol pyruvate carboxylase and Entner–Doudoroff pathway in Saccharomyces cerevisiae for improvement of isobutanol production

Bacterial phosphoenol pyruvate carboxylase (PPC) and enzymes in the Entner-Doudoroff (ED) pathway were heterologously expressed in Saccharomyces cerevisiae to improve the NADPH supply required for the bio-production of chemicals such as isobutanol. The heterologous expression of PPC from Synechocystis sp. PCC6803 increased in the isobutabol titer 1.45-fold (93.2±1.6mg/L) in metabolically engineered S.cerevisiae strains producing isobutanol. This result suggested that the pyruvate and NADPH supply for isobutanol biosynthesis was activated by PPC overexpression. On the other hand, the expression of two enzymes organizing the ED pathway (6-phosphogluconate dehydratase [6PGD] and 2-dehydro-3-deoxy-phosphogluconate aldolase [KDPGA]) had no effect to isobutabol bio-production. Further analysis, however, revealed that additional expression of 6PGD and KDPGA improved the growth rate of S.cerevisiae strain BY4742 gnd1Δ. A 13C-labeling experiment using [1-13C] glucose also suggested that metabolic flow levels in the ED pathway increased slightly with the additional expression. These results showed that the ED pathway was successfully constructed in S.cerevisiae, even though activity of the pathway was too weak to improve isobutanol biosynthesis.

Secretion of 2,3-dihydroxyisovalerate as a limiting factor for isobutanol production in Saccharomyces cerevisiae.

Isobutanol is a superior biofuel compared to ethanol, and it is naturally produced by yeasts. Previously, Saccharomyces cerevisiae has been genetically engineered to improve isobutanol production. We found that yeast cells engineered for a cytosolic isobutanol biosynthesis secrete large amounts of the intermediate 2,3-dihydroxyisovalerate (DIV). This indicates that the enzyme dihydroxyacid dehydratase (Ilv3) is limiting the isobutanol pathway and/or yeast exhibit effective transport systems for the secretion of the intermediate, competing with isobutanol synthesis. Moreover, we found that DIV cannot be taken up by the cells again. To identify the responsible transporters, microarray analysis was performed with a DIV producing strain compared to a wild type. Altogether, 19 genes encoding putative transporters were upregulated under DIV-producing conditions. Thirteen of these were deleted together with five homologous genes. A yro2 mrh1 deletion strain showed reduced DIV secretion, while a hxt5 deletion mutant showed increased isobutanol production. However, a strain deleted for all the 18 genes secreted even slightly increased amounts of the intermediates and less isobutanol. The lactate transporter Jen1 turned out to transport the intermediate 2-ketoisovalerate, but not DIV. The results suggest that the transport of DIV is a rather complex process and several unspecific transporters seem to be involved.

Engineering the leucine biosynthetic pathway for isoamyl alcohol overproduction in Saccharomyces cerevisiae.

Isoamyl alcohol can be used not only as a biofuel, but also as a precursor for various chemicals. Saccharomyces cerevisiae inherently produces a small amount of isoamyl alcohol via the leucine degradation pathway, but the yield is very low. In the current study, several strategies were devised to overproduce isoamyl alcohol in budding yeast. The engineered yeast cells with the cytosolic isoamyl alcohol biosynthetic pathway produced significantly higher amounts of isobutanol over isoamyl alcohol, suggesting that the majority of the metabolic flux was diverted to the isobutanol biosynthesis due to the broad substrate specificity of Ehrlich pathway enzymes. To channel the key intermediate 2-ketosiovalerate (KIV) towards α-IPM biosynthesis, we introduced an artificial protein scaffold to pull dihydroxyacid dehydratase and α-IPM synthase into the close proximity, and the resulting strain yielded more than twofold improvement of isoamyl alcohol. The best isoamyl alcohol producer yielded 522.76±38.88mg/L isoamyl alcohol, together with 540.30±48.26mg/L isobutanol and 82.56±8.22mg/L 2-methyl-1-butanol. To our best knowledge, our work represents the first study to bypass the native compartmentalized α-IPM biosynthesis pathway for the isoamyl alcohol overproduction in budding yeast. More importantly, artificial protein scaffold based on the feature of quaternary structure of enzymes would be useful in improving the catalytic efficiency and the product specificity of other enzymatic reactions.

Effect of GPD2 and PDC6 Deletion on Isobutanol Titer in Saccharomyces Cerevisiae

Objectives: Isobutanol is regarded as a next-generation biofuel for its higher octane number and higher energy density than ethanol. However, during isobutanol biosynthesis, ethanol and glycerol are major unwanted byproducts. In order to improve isobutanol production in Saccharomyces cerevisiae, we used molecular biology and genetic recombination technologies to eliminate ethanol and glycerol titers. Methods: In this study, GPD2 and PDC6 were deleted to increase isobutanol production in microaerobic fermentation of Saccharomyces cerevisiae. Engineered strain HZAL–13 (PGK1p–BAT2 gpd2Δ::RYUR) was constructed by overexpressing of BAT2 (which encodes a branched-chain amino-acid aminotransferase) and deleting GPD2 (which encodes glycerol-3-phosphate dehydrogenase). Engineered strain HZAL–14 (PGK1p–BAT2 pdc6Δ::R gpd2Δ::RYUR) was obtained by further deleting PDC6 (which encodes pyruvate decarboxylase) in HZAL– 13 pILV2. Then we tested the fermentation performances of engineered strains and control strain. During microaerobic fermentation, cultures were performed at 30°C in the unbaffled shake flasks kept at constant stirring speed of 100 rev/min with 100 ml medium for 48 hours. Results: The maximum isobutanol titers of control strain, HZAL–13 pILV2 and HZAL–14 pILV2 were 29.8 mg/l, 162.3 mg/l and 309.3 mg/l, respectively. These results demonstrate that decreasing glycerol formation and ethanol biosynthesis in combination through deletion of PDC6 and GPD2 could increase dramatically the isobutanol titer in S. cerevisiae. Conclusion: Overexpression of related genes in isobutanol biosynthesis pathway and deletion of key genes that encode glycerol and ethanol biosynthesis is a promising strategy to increase isobutanol titer in Saccharomyces cerevisiae.

Eliminating the isoleucine biosynthetic pathway to reduce competitive carbon outflow during isobutanol production by Saccharomyces cerevisiae.

BackgroundIsobutanol is an important biorefinery target alcohol that can be used as a fuel, fuel additive, or commodity chemical. Baker’s yeast, Saccharomyces cerevisiae, is a promising organism for the industrial manufacture of isobutanol because of its tolerance for low pH and resistance to autolysis. It has been reported that gene deletion of the pyruvate dehydrogenase complex, which is directly involved in pyruvate metabolism, improved isobutanol production by S. cerevisiae. However, the engineering strategies available for S. cerevisiae are immature compared to those available for bacterial hosts such as Escherichia coli, and several pathways in addition to pyruvate metabolism compete with isobutanol production.ResultsThe isobutyrate, pantothenate or isoleucine biosynthetic pathways were deleted to reduce the outflow of carbon competing with isobutanol biosynthesis in S. cerevisiae. The judicious elimination of these competing pathways increased isobutanol production. ILV1 encodes threonine ammonia-lyase, the enzyme that converts threonine to 2-ketobutanoate, a precursor for isoleucine biosynthesis. S. cerevisiae mutants in which ILV1 had been deleted displayed 3.5-fold increased isobutanol productivity. The ΔILV1 strategy was further combined with two previously established engineering strategies (activation of two steps of the Ehrlich pathway and the transhydrogenase-like shunt), providing 11-fold higher isobutanol productivity as compared to the parent strain. The titer and yield of this engineered strain was 224 ± 5 mg/L and 12.04 ± 0.23 mg/g glucose, respectively.ConclusionsThe deletion of competitive pathways to reduce the outflow of carbon, including ILV1 deletion, is an important strategy for increasing isobutanol production by S. cerevisiae.

Identification and optimization of a novel thermo- and solvent stable ketol-acid reductoisomerase for cell free isobutanol biosynthesis.

Due to its enhanced energy content and hydrophobicity, isobutanol is flagged as a next generation biofuel and chemical building block. For cellular and cell-free isobutanol production, NADH dependent (over NADPH dependent) enzyme systems are desired. To improve cell-free isobutanol processes, we characterized and catalytically optimized a NADH dependent, thermo- and solvent stable ketol-acid reductoisomerase (KARI) derived from the bacterium Meiothermus ruber (Mr). The wild type Mr-KARI has the most temperature tolerant KARI specific activity reported to date. The KARI screening procedure developed in this study allows accelerated molecular optimization. Thus, a KARI variant with a 350% improved activity and enhanced NADH cofactor specificity was identified. Other KARI variants gave insights into Mr-KARI structure-function relationships.

Genome tailoring powered production of isobutanol in continuous CO2/H2 blend fermentation using engineered acetogen biocatalyst

The cell energy fraction that powered maintenance and expression of genes encoding pro-phage elements, pta-ack cluster, early sporulation, sugar ABC transporter periplasmic proteins, 6-phosphofructokinase, pyruvate kinase, and fructose-1,6-disphosphatase in acetogen Clostridium sp. MT871 was re-directed to power synthetic operon encoding isobutanol biosynthesis at the expense of these genes achieved via their elimination. Genome tailoring decreased cell duplication time by 7.0 ± 0.1 min (p < 0.05) compared to the parental strain, with intact genome and cell duplication time of 68 ± 1 min (p < 0.05). Clostridium sp. MT871 with tailored genome was UVC-mutated to withstand 6.1 % isobutanol in fermentation broth to prevent product inhibition in an engineered commercial biocatalyst producing 5 % (674.5 mM) isobutanol during two-step continuous fermentation of CO2/H2 gas blend. Biocatalyst Clostridium sp. MT871RG- 11IBR6 was engineered to express six copies of synthetic operon comprising optimized synthetic format dehydrogenase, pyruvate formate lyase, acetolactate synthase, acetohydroxyacid reductoisomerase, 2,3-dihydroxy-isovalerate dehydratase, branched-chain alpha-ketoacid decarboxylase gene, aldehyde dehydrogenase, and alcohol dehydrogenase, regaining cell duplication time of 68 ± 1 min (p < 0.05) for the parental strain. This is the first report on isobutanol production by an engineered acetogen biocatalyst suitable for commercial manufacturing of this chemical/fuel using continuous fermentation of CO2/H2 blend thus contributing to the reversal of global warming.

Model-Driven Redox Pathway Manipulation for Improved Isobutanol Production in Bacillus subtilis Complemented with Experimental Validation and Metabolic Profiling Analysis

To rationally guide the improvement of isobutanol production, metabolic network and metabolic profiling analysis were performed to provide global and profound insights into cell metabolism of isobutanol-producing Bacillus subtilis. The metabolic flux distribution of strains with different isobutanol production capacity (BSUL03, BSUL04 and BSUL05) drops a hint of the importance of NADPH on isobutanol biosynthesis. Therefore, the redox pathways were redesigned in this study. To increase NADPH concentration, glucose-6-phosphate isomerase was inactivated (BSUL06) and glucose-6-phosphate dehydrogenase was overexpressed (BSUL07) successively. As expected, NADPH pool size in BSUL07 was 4.4-fold higher than that in parental strain BSUL05. However, cell growth, isobutanol yield and production were decreased by 46%, 22%, and 80%, respectively. Metabolic profiling analysis suggested that the severely imbalanced redox status might be the primary reason. To solve this problem, gene udhA of Escherichia coli encoding transhydrogenase was further overexpressed (BSUL08), which not only well balanced the cellular ratio of NAD(P)H/NAD(P)+, but also increased NADH and ATP concentration. In addition, a straightforward engineering approach for improving NADPH concentrations was employed in BSUL05 by overexpressing exogenous gene pntAB and obtained BSUL09. The performance for isobutanol production by BSUL09 was poorer than BSUL08 but better than other engineered strains. Furthermore, in fed-batch fermentation the isobutanol production and yield of BSUL08 increased by 11% and 19%, up to the value of 6.12 g/L and 0.37 C-mol isobutanol/C-mol glucose (63% of the theoretical value), respectively, compared with parental strain BSUL05. These results demonstrated that model-driven complemented with metabolic profiling analysis could serve as a useful approach in the strain improvement for higher bio-productivity in further application.

Isobutanol production as an alternative metabolic sink to rescue the growth deficiency of the glycogen mutant of Synechococcus elongatus PCC 7942

Glycogen synthesis initiated by glucose-1-phosphate adenylyltransferase (glgC) represents a major carbon storage route in cyanobacteria which could divert a significant portion of assimilated carbon. Significant growth retardation in cyanobacteria with glgC knocked out (ΔglgC) has been reported in high light conditions. Here, we knocked out the glgC gene and analyzed its effects on carbon distribution in an isobutanol-producing strain of Synechococcus elongatus PCC7942 and its parental wild-type strain. We showed that isobutanol production was able to partially rescue the growth of ΔglgC mutant where the growth rescue effect positively correlated with the rate of isobutanol production. Using NaH(14)CO3 incorporation analysis, we observed a 28% loss of total carbon fixation rate in the ΔglgC mutant compared to the wild-type. Upon expression of the isobutanol production pathway in ΔglgC mutant, the total carbon fixation rate was restored to the wild-type level. Furthermore, we showed that 52% of the total carbon fixed was redirected into isobutanol biosynthesis in the ΔglgC mutant expressing enzymes for isobutanol production, which is 2.5 times higher than that of the wild-type expressing the same enzymes. These results suggest that biosynthesis of non-native product such as isobutanol can serve as a metabolic sink for replacing glycogen to rescue growth and restore carbon fixation rate. The rescue effect may further serve as a platform for cyanobacteria energy and carbon metabolism study.