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Cellulosic n-butanol from renewable lignocellulosic biomass has gained increased interest. Previously, we have engineered Clostridium cellulovorans, a cellulolytic acidogen, to overexpress the bifunctional butyraldehyde/butanol dehydrogenase gene adhE2 from C. acetobutylicum for n-butanol production from crystalline cellulose. However, butanol production by this engineered strain had a relatively low yield of approximately 0.22 g/g cellulose due to the coproduction of ethanol and acids. We hypothesized that strengthening the carbon flux through the central butyryl-CoA biosynthesis pathway and increasing intracellular NADH availability in C. cellulovorans adhE2 would enhance n-butanol production. In this study, thiolase (thlA CA ) from C. acetobutylicum and 3-hydroxybutyryl-CoA dehydrogenase (hbd CT ) from C. tyrobutyricum were overexpressed in C. cellulovorans adhE2 to increase the flux from acetyl-CoA to butyryl-CoA. In addition, ferredoxin-NAD(P) + oxidoreductase (fnr), which can regenerate the intracellular NAD(P)H and thus increase butanol biosynthesis, was also overexpressed. Metabolic flux analyses showed that mutants overexpressing these genes had a significantly increased carbon flux toward butyryl-CoA, which resulted in increased production of butyrate and butanol. The addition of methyl viologen as an electron carrier in batch fermentation further directed more carbon flux towards n-butanol biosynthesis due to increased reducing equivalent or NADH. The engineered strain C. cellulovorans adhE2-fnr CA -thlA CA -hbd CT produced n-butanol from cellulose at a 50% higher yield (0.34 g/g), the highest ever obtained in batch fermentation by any known bacterial strain. The engineered C. cellulovorans is thus a promising host for n-butanol production from cellulosic biomass in consolidated bioprocessing., (© 2021 Wiley Periodicals LLC.)

Clostridia are Gram-positive, spore-forming, obligate anaerobic bacteria that can produce solvents such as acetone, ethanol, and butanol, which can be used as biofuels or building block chemicals. Many successful attempts have been made to improve solvent yield and titer from sugars through metabolic engineering of solventogenic and acidogenic clostridia. More recently, cellulolytic and acetogenic clostridia have also attracted high interests for their ability to utilize low-cost renewable substrates such as cellulose and syngas. Process engineering such as in situ butanol recovery and consolidated bioprocessing (CBP) has been developed for improved solvent titer and productivity. This review focuses on metabolic and process engineering strategies for solvent production from sugars, lignocellulosic biomass, and syngas by various clostridia, including conventional solventogenic Clostridium acetobutylicum, engineered acidogens such as C. tyrobutyricum and C. cellulovorans, and carboxydotrophic acetogens such as C. carboxidivorans and C. ljungdahlii.

Clostridium cellulovorans capable of producing large amounts of acetate and butyrate from cellulose is a promising candidate for biofuels and biochemicals production from lignocellulosic biomass. However, the restriction modification (RM) systems of C. cellulovorans hindered the application of existing shuttle plasmids for metabolic engineering of this organism. To overcome the hurdle of plasmid digestion by host, a new shuttle plasmid (pYL001) was developed to remove all restriction sites of two major RM systems of C. cellulovorans, Cce743I and Cce743II. The pYL001 plasmid remained intact after challenge by C. cellulovorans cell extract. Post-electroporation treatments and culturing conditions were also modified to improve cell growth and colony formation on agar plates. With the improvements, the pYL001 plasmid, without in vivo methylation, was readily transformed into C. cellulovorans with colonies of recombinant cells formed on agar plates within 24 h. Three pYL001-derived recombinant plasmids free of Cce743I/Cce743II restriction sites, after synonymous mutation of the heterologous genes, were constructed and transformed into C. cellulovorans. Functional expression of these genes was confirmed with butanol and ethanol production from glucose in batch fermentations by the transformants. The pYL001 plasmid and improved transformation method can facilitate further metabolic engineering of C. cellulovorans for cellulosic butanol production.

Clostridium carboxidivorans can convert CO 2 , CO and H 2 to ethanol and n-butanol; however, its industrial application is limited by the lack of tools for metabolic pathway engineering. In this study, C. carboxidivorans was successfully engineered to overexpress aor, adhE2, and fnr together with adhE2 or aor. In glucose fermentation, all engineered strains showed higher alcohol yields compared to the wild-type. Strains overexpressing aor showed CO 2 re-assimilation during heterotrophic growth. In syngas fermentation, compared to the wild-type, the strain overexpressing adhE2 produced ∼50% more ethanol and the strain overexpressing adhE2 and fnr produced ∼18% more butanol and ∼22% more ethanol. Interestingly, both strains showed obvious acid re-assimilation, with <0.15 g/L total acid remaining at the end of fermentation. Overexpressing fnr with adhE2 enhanced butanol production compared to only adhE2. This is the first report of overexpressing homologous and heterologous genes in C. carboxidivorans for enhancing alcohols production from syngas and glucose., (Copyright © 2019 Elsevier Ltd. All rights reserved.)

Butyric acid is an important C4 organic acid with broad applications. It is currently produced by chemosynthesis from petroleum-based feedstocks. However, the fermentative production of butyric acid from renewable feedstocks has received growing attention because of consumer demand for green products and natural ingredients in foods, pharmaceuticals, animal feed supplements, and cosmetics. In this review, strategies for improving microbial butyric acid production, including strain engineering and novel fermentation process development are discussed and compared regarding product yield, titer, purity and productivity. Future perspectives on strain and process improvements for butyric acid production are also discussed., (Copyright © 2018 Elsevier Inc. All rights reserved.)

Acetoin and 2,3-butanediol (2,3-BD) have a large number of industrial applications. The production of acetoin and 2,3-BD has traditionally relied on oil supplies. Microbial production of acetoin and 2,3-BD will alleviate the dependence on oil. Acetoin and 2,3-BD are neighboring metabolites in the 2,3-BD metabolic pathway of bacteria. This review summarizes metabolic engineering strategies for improvement of microbial acetoin and 2,3-BD production. We also propose enhancements to current acetoin and 2,3-BD production strategies, by offering a metabolic engineering approach that is guided by systems biology and synthetic biology.

Clostridium tyrobutyricum is a promising organism for butyrate and n-butanol production, but cannot grow on sucrose. Three genes (scrA, scrB, and scrK) involved in the sucrose catabolic pathway, along with an aldehyde/alcohol dehydrogenase gene, were cloned from Clostridium acetobutylicum and introduced into C. tyrobutyricum (Δack) with acetate kinase knockout. In batch fermentation, the engineered strain Ct(Δack)-pscrBAK produced 14.8-18.8 g/L butanol, with a high butanol/total solvent ratio of ∼0.94 (w/w), from sucrose and sugarcane juice. Moreover, stable high butanol production with a high butanol yield of 0.25 g/g and productivity of 0.28 g/L∙h was obtained in batch fermentation without using antibiotics for selection pressure, suggesting that Ct(Δack)-pscrBAK is genetically stable. Furthermore, sucrose utilization by Ct(Δack)-pscrBAK was not inhibited by glucose, which would usually cause carbon catabolite repression on solventogenic clostridia. Ct(Δack)-pscrBAK is thus advantageous for use in biobutanol production from sugarcane juice and other sucrose-rich feedstocks.

Butanol as an advanced biofuel has gained great attention due to its environmental benefits and superior properties compared to ethanol. However, the cost of biobutanol production via conventional acetone-butanol-ethanol (ABE) fermentation by Clostridium acetobutylicum is not economically competitive, which has hampered its industrial application. The strain performance and downstream process greatly impact the economics of biobutanol production. Although various engineered strains with carefully orchestrated metabolic and sporulation-specific pathways have been developed, none of them is ideal for industrial biobutanol production. For further strain improvement, it is necessary to develop advanced genome editing tools and a deep understanding of cellular functioning of genes in metabolic and regulatory pathways. Processes with integrated product recovery can increase fermentation productivity by continuously removing inhibitory products while generating butanol (ABE) in a concentrated solution. In this review, we provide an overview of recent advances in C. acetobutylicum strain engineering and process development focusing on in situ product recovery. With deep understanding of systematic cellular bioinformatics, the exploration of state-of-the-art genome editing tools such as CRISPR-Cas for targeted gene knock-out and knock-in would play a vital role in Clostridium cell engineering for biobutanol production. Developing advanced hybrid separation processes for in situ butanol recovery, which will be discussed with a detailed comparison of advantages and disadvantages of various recovery techniques, is also imperative to the economical development of biobutanol., (Copyright © 2017 Elsevier Inc. All rights reserved.)

Clostridium tyrobutyricum is a promising microorganism for butyric acid production. However, its ability to utilize xylose, the second most abundant sugar found in lignocellulosic biomass, is severely impaired by glucose-mediated carbon catabolite repression (CCR). In this study, CCR in C. tyrobutyricum was eliminated by overexpressing three heterologous xylose catabolism genes (xylT, xylA and xlyB) cloned from C. acetobutylicum. Compared to the parental strain, the engineered strain Ct-pTBA produced more butyric acid (37.8g/L vs. 19.4g/L) from glucose and xylose simultaneously, at a higher xylose utilization rate (1.28g/L·h vs. 0.16g/L·h) and efficiency (94.3% vs. 13.8%), resulting in a higher butyrate productivity (0.53g/L·h vs. 0.26g/L·h) and yield (0.32g/g vs. 0.28g/g). When the initial total sugar concentration was ~120g/L, both glucose and xylose utilization rates increased with increasing their respective concentration or ratio in the co-substrates but the total sugar utilization rate remained almost unchanged in the fermentation at pH 6.0. Decreasing the pH to 5.0 significantly decreased sugar utilization rates and butyrate productivity, but the effect was more pronounced for xylose than glucose. The addition of benzyl viologen (BV) as an artificial electron carrier facilitated the re-assimilation of acetate and increased butyrate production to a final titer of 46.4g/L, yield of 0.43g/g sugar consumed, productivity of 0.87g/L·h, and acid purity of 98.3% in free-cell batch fermentation, which were the highest ever reported for butyric acid fermentation. The engineered strain with BV addition thus can provide an economical process for butyric acid production from lignocellulosic biomass., (Copyright © 2017 International Metabolic Engineering Society. Published by Elsevier Inc. All rights reserved.)

Propionibacterium freudenreichii cannot use xylose, the second most abundant sugar in lignocellulosic biomass. Although Propionibacterium acidipropionici can use xylose as a carbon source, it is difficult to genetically modify, impeding further improvement through metabolic engineering. This study identified three xylose catabolic pathway genes encoding for xylose isomerase (xylA), xylose transporter (xylT), and xylulokinase (xylB) in P. acidipropionici and overexpressed them in P. freudenreichii subsp. shermanii via an expression plasmid pKHEM01, enabling the mutant to utilize xylose efficiently even in the presence of glucose without glucose-induced carbon catabolite repression. The mutant showed similar fermentation kinetics with glucose, xylose, and the mixture of glucose and xylose, respectively, as carbon source, and with or without the addition of antibiotic for selection pressure. The engineered P. shermanii thus can provide a novel cell factory for industrial production of propionic acid and other value-added products from lignocellulosic biomass., (Copyright © 2016 Elsevier Ltd. All rights reserved.)

1,3-Propanediol (1,3-PDO) production from crude glycerol, a byproduct from biodiesel manufacturing, by Clostridium beijerinckii DSM 791 was studied with corn steep liquor as an inexpensive nitrogen source replacing yeast extract in the fermentation medium. A stable, long-term 1,3-PDO production from glycerol was demonstrated with cells immobilized in a fibrous bed bioreactor operated in a repeated batch mode, which partially circumvented the 1,3-PDO inhibition problem. The strain was then engineered to overexpress Escherichia coli gldA encoding glycerol dehydrogenase (GDH) and dhaKLM encoding dihydroxyacetone kinase (DHAK), which increased 1,3-PDO productivity by 26.8-37.5% compared to the wild type, because of greatly increased specific growth rate (0.25-0.40h(-1) vs. 0.13-0.20h(-1) for the wild type). The engineered strain gave a high 1,3-PDO titer (26.1g/L), yield (0.55g/g) and productivity (0.99g/L·h) in fed-batch fermentation. Overexpressing GDH and DHAK was thus effective in increasing 1,3-PDO production from glycerol., (Copyright © 2016 Elsevier Ltd. All rights reserved.)

Production of cellulosic biofuels has drawn increasing attention. However, currently no microorganism can produce biofuels, particularly butanol, directly from cellulosic biomass efficiently. Here we engineered a cellulolytic bacterium, Clostridium cellulovorans, for n-butanol and ethanol production directly from cellulose by introducing an aldehyde/alcohol dehydrogenase (adhE2), which converts butyryl-CoA to n-butanol and acetyl-CoA to ethanol. The engineered strain was able to produce 1.42 g/L n-butanol and 1.60 g/L ethanol directly from cellulose. Moreover, the addition of methyl viologen as an artificial electron carrier shifted the metabolic flux from acid production to alcohol production, resulting in a high biofuel yield of 0.39 g/g from cellulose, comparable to ethanol yield from corn dextrose by yeast fermentation. This study is the first metabolic engineering of C. cellulovorans for n-butanol and ethanol production directly from cellulose with significant titers and yields, providing a promising consolidated bioprocessing (CBP) platform for biofuel production from cellulosic biomass., (Copyright © 2015 International Metabolic Engineering Society. Published by Elsevier Inc. All rights reserved.)

The glucose-mediated carbon catabolite repression (CCR) in Clostridium tyrobutyricum impedes efficient utilization of xylose present in lignocellulosic biomass hydrolysates. In order to relieve the CCR and enhance xylose utilization, three genes (xylT, xylA, and xylB) encoding a xylose proton-symporter, a xylose isomerase and a xylulokinase, respectively, from Clostridium acetobutylicum ATCC 824 were co-overexpressed with aldehyde/alcohol dehydrogenase (adhE2) in C. tyrobutyricum (Δack). Compared to the strain Ct(Δack)-pM2 expressing only adhE2, the mutant Ct(Δack)-pTBA had a higher xylose uptake rate and was able to simultaneously consume glucose and xylose at comparable rates for butanol production. Ct(Δack)-pTBA produced more butanol (12.0 vs. 3.2 g/L) with a higher butanol yield (0.12 vs. 0.07 g/g) and productivity (0.17 vs. 0.07 g/L · h) from both glucose and xylose, while Ct(Δack)-pM2 consumed little xylose in the fermentation. The results confirmed that the CCR in C. tyrobutyricum could be overcome through overexpressing xylT, xylA, and xylB. The mutant was also able to co-utilize glucose and xylose present in soybean hull hydrolysate (SHH) for butanol production, achieving a high butanol titer of 15.7 g/L, butanol yield of 0.24 g/g, and productivity of 0.29 g/L · h. This study demonstrated the potential application of Ct(Δack)-pTBA for industrial biobutanol production from lignocellulosic biomass., (© 2015 Wiley Periodicals, Inc.)

Clostridium tyrobutyricum does not have the enzymes needed for using maltose or starch. Two extracellular α-glucosidases encoded by agluI and agluII from Clostridium acetobutylicum ATCC 824 catalyzing the hydrolysis of α-1,4-glycosidic bonds in maltose and starch from the non-reducing end were cloned and expressed in C. tyrobutyricum (Δack, adhE2), and their effects on n-butanol production from maltose and soluble starch in batch fermentations were studied. Compared to the parental strain grown on glucose, mutants expressing agluI showed robust activity in breaking down maltose and produced more butanol (17.2 vs. 9.5 g/L) with a higher butanol yield (0.20 vs. 0.10 g/g) and productivity (0.29 vs. 0.16 g/L h). The mutant was also able to use soluble starch as substrate, although at a slower rate compared to maltose. Compared to C. acetobutylicum ATCC 824, the mutant produced more butanol from maltose (17.2 vs. 11.2 g/L) and soluble starch (16.2 vs. 8.8 g/L) in batch fermentations. The mutant was stable in batch fermentation without adding antibiotics, achieving a high butanol productivity of 0.40 g/L h. This mutant strain thus can be used in industrial production of n-butanol from maltose and soluble starch.

The overexpression of CoA transferase (ctfAB), which catalyzes the reaction: acetate/butyrate + acetoacetyl-CoA → acetyl/butyryl-CoA + acetoacetate, was studied for its effects on acid reassimilation and butanol biosynthesis in Clostridium tyrobutyricum (Δack, adhE2). The plasmid pMTL007 was used to co-express adhE2 and ctfAB from Clostridium acetobutylicum ATCC 824. In addition, the sol operon containing ctfAB, adc (acetoacetate decarboxylase), and ald (aldehyde dehydrogenase) was also cloned from Clostridium beijerinckii NCIMB 8052 and expressed in C. tyrobutyricum (Δack, adhE2). Mutants expressing these genes were evaluated for their ability to produce butanol from glucose in batch fermentations at pH 5.0 and 6.0. Compared to C. tyrobutyricum (Δack, adhE2) without expressing ctfAB, all mutants with ctfAB overexpression produced more butanol, with butanol yield increased to 0.22 - 0.26 g/g (vs. 0.10 - 0.13 g/g) and productivity to 0.35 g/l h (vs. 0.13 g/l h) because of the reduced acetate and butyrate production. The expression of ctfAB also resulted in acetone production from acetoacetate through a non-enzymatic decarboxylation.

Butanol biosynthesis through aldehyde/alcohol dehydrogenase (adhE2) is usually limited by NADH availability, resulting in low butanol titer, yield, and productivity. To alleviate this limitation and improve n-butanol production by Clostridium tyrobutyricum Δack-adhE2 overexpressing adhE2, the NADH availability was increased by using methyl viologen (MV) as an artificial electron carrier to divert electrons from ferredoxin normally used for H2 production. In the batch fermentation with the addition of 500 μM MV, H2 , acetate, and butyrate production was reduced by more than 80-90%, while butanol production increased more than 40% to 14.5 g/L. Metabolic flux analysis revealed that butanol production increased in the fermentation with MV because of increased NADH availability as a result of reduced H2 production. Furthermore, continuous butanol production of ∼55 g/L with a high yield of ∼0.33 g/g glucose and extremely low ethanol, acetate, and butyrate production was obtained in fed-batch fermentation with gas stripping for in situ butanol recovery. This study demonstrated a stable and reliable process for high-yield and high-titer n-butanol production by metabolically engineered C. tyrobutyricum by applying MV as an electron carrier to increase butanol biosynthesis., (© 2014 Wiley Periodicals, Inc.)

Clostridium acetobutylicum JB200, a mutant strain of C. acetobutylicum ATCC 55025 obtained through strain evolution in a fibrous bed bioreactor, had high butanol tolerance and produced up to ~21 g/L butanol from glucose in batch fermentation, an improvement of ~67 % over the parental strain (~12.6 g/L). Comparative genomic analysis revealed a single-base deletion in the cac3319 gene leading to C-terminal truncation in its encoding histidine kinase (HK) in JB200. To study the effects of cac3319 mutation on cell growth and fermentation, the cac3319 gene in ATCC 55025 was disrupted using the ClosTron group II intron-based gene inactivation system. Compared to ATCC 55025, the cac3319 HK knockout mutant, HKKO, produced 44.4 % more butanol (18.2 ± 1.3 vs. 12.6 ± 0.2 g/L) with a 90 % higher productivity (0.38 ± 0.03 vs. 0.20 ± 0.02 g/L h) due to increased butanol tolerance, confirming, for the first time, that cac3319 plays an important role in regulating solvent production and tolerance in C. acetobutylicum. This work also provides a novel metabolic engineering strategy for generating high-butanol-tolerant and high-butanol-producing strains for industrial applications.

Propionibacterium freudenreichii subsp. shermanii naturally forms propionic acid as the main fermentation product with acetate and succinate as two major by-products. In this study, overexpressing the native propionyl-CoA:succinate CoA transferase (CoAT) in P. shermanii was investigated to evaluate its effects on propionic acid fermentation with glucose, glycerol, and their mixtures as carbon source. In general, the mutant produced more propionic acid, with up to 10% increase in yield (0.62 vs. 0.56g/g) and 46% increase in productivity (0.41 vs. 0.28g/Lh), depending on the fermentation conditions. The mutant also produced less acetate and succinate, with the ratios of propionate to acetate (P/A) and succinate (P/S) in the final product increased 50% and 23%, respectively, in the co-fermentation of glucose/glycerol. Metabolic flux analysis elucidated that CoAT overexpression diverted more carbon fluxes toward propionic acid, resulting in higher propionic acid purity and a preference for glycerol over glucose as carbon source., (Copyright © 2014 International Metabolic Engineering Society. Published by Elsevier Inc. All rights reserved.)

Propionic acid is currently produced mainly via petrochemicals, but there is increasing interest in its fermentative production from renewable biomass. However, the current propionic acid fermentation process suffers from low product yield and productivity. In this work, the gene encoding phosphoenolpyruvate carboxylase (PPC) was cloned from Escherichia coli and expressed in Propionibacterium freudenreichii. PPC catalyzes the conversion of phosphoenolpyruvate to oxaloacetate with the fixation of one CO2. Its expression in P. freudenreichii showed profound effects on propionic acid fermentation. Compared to the wild type, the mutant expressing the ppc gene grew significantly faster, consumed more glycerol, and produced propionate to a higher final titer at a faster rate. The mutant also produced significantly more propionate from glucose under elevated CO2 partial pressure. These effects could be attributed to increased CO2 fixation and resulting changes in the flux distributions in the dicarboxylic acid pathway.

Fumaric acid, a dicarboxylic acid used as a food acidulant and in manufacturing synthetic resins, can be produced from glucose in fermentation by Rhizopus oryzae. However, the fumaric acid yield is limited by the co-production of ethanol and other byproducts. To increase fumaric acid production, overexpressing endogenous pyruvate carboxylase (PYC) and exogenous phosphoenolpyruvate carboxylase (PEPC) to increase the carbon flux toward oxaloacetate were investigated. Compared to the wild type, the PYC activity in the pyc transformants increased 56%-83%, whereas pepc transformants exhibited significant PEPC activity (3-6 mU/mg) that was absent in the wild type. Fumaric acid production by the pepc transformant increased 26% (0.78 g/g glucose vs. 0.62 g/g for the wild type). However, the pyc transformants grew poorly and had low fumaric acid yields (<0.05 g/g glucose) due to the formation of large cell pellets that limited oxygen supply and resulted in the accumulation of ethanol with a high yield of 0.13-0.36 g/g glucose. This study is the first attempt to use metabolic engineering to modify the fumaric acid biosynthesis pathway to increase fumaric acid production in R. oryzae., (Copyright © 2012 Elsevier Inc. All rights reserved.)

Polymalic acid (PMA), a homopolymer of L-malic acid (MA) generated from a yeast-like fungus Aureobasidium pullulans, has unique properties and many applications in food, biomedical, and environmental fields. Acid hydrolysis of PMA, releasing the monomer MA, has become a novel process for the production of bio-based MA, which currently is produced by chemical synthesis using petroleum-derived feedstocks. Recently, current researches attempted to develop economically competitive process for PMA and MA production from renewable biomass feedstocks. Compared to lignocellulosic biomass, PMA and MA production from low-value food processing wastes or by-products, generated from corn, sugarcane, or soybean refinery industries, showed more economical and sustainable for developing a MA derivatives platform from biomass biorefinery to chemical conversion. In the review, we compared the process feasibility for PMA fermentation with lignocellulosic biomass and food process wastes. Some useful strategies for metabolic engineering are summarized. Its changeable applicability and future prospects in food and biomedical fields are also discussed. [ABSTRACT FROM AUTHOR]

Some microorganisms naturally produce β-poly(L-malic acid) (PMA), which has excellent water solubility, biodegradability, and biocompatibility properties. PMA has broad prospective applications as novel biopolymeric materials and carriers in the drug, food, and biomedical fields. Malic acid, a four-carbon dicarboxylic acid, is widely used in foods and pharmaceuticals, as a platform chemical. Currently, malic acid produced through chemical synthesis and is available as a racemic mixture of L- and D-forms. The D-form malic acid exhibits safety concerns for human consumption. There is extensive interest to develop economical bioprocesses for L-malic acid and PMA production from renewable biomass feedstocks. In this review, we focus on PMA biosynthesis by Aureobasidium pullulans, a black yeast with a large genome containing genes encoding many hydrolases capable of degrading various plant materials. The metabolic and regulatory pathways for PMA biosynthesis, metabolic engineering strategies for strain development, process factors affecting fermentation kinetics and PMA production, and downstream processing for PMA recovery and purification are discussed. Prospects of microbial PMA and malic acid production are also considered. [ABSTRACT FROM AUTHOR]

Abstract: Fumaric acid is a dicarboxylic acid used extensively in synthetic resins, food acidulants, and other applications, including oil field fluids and esters. The filamentous fungus Rhizopus oryzae is known for its ability to produce and accumulate high levels of fumaric acid under aerobic conditions. In this work, the overexpression of native fumarase encoded by fumR and its effect on fumaric acid production in R. oryzae were investigated. Three plasmids containing the endogenous fumR gene were constructed and used to transform R. oryzae, and all transformants showed significantly increased fumarase activity during both the seed culture (growth) and fermentation (fumaric acid production) stages. However, fumarase overexpression in R. oryzae yielded more malic acid, instead of fumaric acid, in the fermentation because the overexpressed fumarase also catalyzed the hydration of fumaric acid to malic acid. The results suggested that the overexpressed fumarase, encoded by fumR, by itself was not responsible for the over-production of fumaric acid in R. oryzae. [Copyright &y& Elsevier]

Abstract: Large amounts of crude glycerol produced in the biodiesel industry can be used as a low-cost renewable feedstock to produce chemicals and fuels. Compared to sugars (sucrose, glucose, xylose, etc.), glycerol has a lower reducing level, which is of benefit to the production of reduced chemicals. In this work, glycerol as the sole carbon source in propionic acid fermentation by metabolically engineered Propionibacterium acidipropionici (ACK-Tet) was studied. It was found that the adapted ACK-Tet mutant could use glycerol for its growth and produced propionic acid at a high yield of 0.54–0.71g/g, which was much higher than that from glucose (∼0.35g/g). In addition, the production of acetic acid in glycerol fermentation was much less than that from glucose. Thus, glycerol fermentation produced a high purity propionic acid with a high propionic acid to acetic acid ratio of 22.4 (vs. ∼5 for glucose fermentation), facilitating the recovery and purification of propionic acid from the fermentation broth. The highest propionic acid concentration obtained from glycerol fermentation was ∼106g/L, which was 2.5 times of the highest concentration (∼42g/L) previously reported in the literature. [Copyright &y& Elsevier]

The production of n -butanol from sugarcane juice by metabolically engineered Clostridium tyrobutyricum Ct(Δack)-pscrBAK overexpressing scr operon genes ( scrB , scrA , and scrK ) for sucrose catabolism and an aldehyde/alcohol dehydrogenase gene ( adhE2 ) for butanol biosynthesis was studied with corn steep liquor (CSL) as a low-cost nitrogen source. In free cell fermentation, butanol production of ∼16 g/L at a yield of 0.31 ± 0.02 g/g and productivity of 0.33 ± 0.02 g/L·h was obtained from sucrose and yield of 0.24 ± 0.02 g/g and productivity of 0.30 ± 0.01 g/L·h from sugarcane juice containing sucrose, glucose and fructose. The fermentation was also studied in a fibrous bed bioreactor (FBB) operated in a repeated batch mode for 10 consecutive cycles in 10 days, achieving an average butanol yield of 0.21 ± 0.02 g/g and productivity of 0.53 ± 0.05 g/L·h from sugarcane juice, demonstrating its long-term stability without applying the antibiotic selection pressure. [ABSTRACT FROM AUTHOR]

Aureobasidium pullulans is a yeast-like fungus used for producing biopolymers e.g. polymalic acid (PMA) and pullulan. A high PMA producing strain, A. pullulans CCTCC M2012223, was isolated and sequenced in our previous study. To understand its metabolic performance, a genome-scale metabolic model, i ZX637, consisting of 637 genes, 1347 reactions and 1133 metabolites, was reconstructed based on genome annotation and literature mining studies. The i ZX637 model was validated by simulating cell growth, utilization of carbon and nitrogen sources, and gene essentiality analysis in A. pullulans . We further validated our model, designed a simulation program for the prediction of PMA production using experimental data, and further analyzed the carbon flux distribution and change with increasing PMA synthesis rates. Through the calculated flux distribution, NADPH- and NADH-dependent methylenetetrahydrofolate dehydrogenase (MTHFD) were found to be associated with the transfer of reducing equivalents from NADPH to NADH for supplementing NADH in the metabolic network. Furthermore, under the high PMA synthesis rate, a large amount of carbon flux was through pyruvate into malic acid via the reductive TCA cycle. Thus, pyruvate carboxylase, which can convert pyruvate to oxaloacetate with CO 2 fixation, may also be an important target for PMA synthesis. These results illustrated that the model i ZX637 was a powerful tool for optimization of A. pullulans metabolism and identification of targets for guiding metabolic engineering. [ABSTRACT FROM AUTHOR]

Bio-based propionic acid production by propionibacteria is increasingly attractive because of its potential to replace petroleum-based chemical synthesis processes. Metabolic engineering of Propionibacterium freudenreichii subsp. shermanii DSM 4902 for enhanced propionic acid fermentation is made possible by the recently available whole genome sequence and genetic engineering tools. Pyruvate carboxylase (PYC), methylmalonyl-CoA decarboxylase (MMD), and methylmalonyl-CoA carboxyltransferase (MMC) are three biotin-dependent carboxylases in the dicarboxylic acid pathway controlling the carbon flux in the Wood–Werkman cycle. These carboxylases were overexpressed in P. shermanii to study their effects on propionic acid fermentation in serum bottles with glucose and glycerol as substrates. Compared to the wild-type, the mutants overexpressing MMC and MMD showed a significant increase in the metabolic fluxes toward the biosynthesis of propionic acid, against acetic and succinic acids, with significantly increased yield (up to 14% increase) and productivity (up to 17% increase), especially in the co-fermentation of glycerol and glucose. On the other hand, the mutant overexpressing PYC grew slower, produced more succinate, and had a lower production of propionate (up to 12% decrease in productivity). This is the first study demonstrating enhanced propionic acid production by overexpressing MMC and MMD in propionibacteria. [ABSTRACT FROM AUTHOR]

Abstract: Clostridium tyrobutyricum ATCC 25755, a butyric acid producing bacterium, has been engineered to overexpress aldehyde/alcohol dehydrogenase 2 (adhE2, Genebank no. AF321779) from Clostridium acetobutylicum ATCC 824, which converts butyryl-CoA to butanol, under the control of native thiolase (thl) promoter. Butanol titer of 1.1g/L was obtained in C. tyrobutyricum overexpressing adhE2. The effects of inactivating acetate kinase (ack) and phosphotransbutyrylase (ptb) genes in the host on butanol production were then studied. A high C4/C2 product ratio of 10.6 (mol/mol) was obtained in ack knockout mutant, whereas a low C4/C2 product ratio of 1.4 (mol/mol) was obtained in ptb knockout mutant, confirming that ack and ptb genes play important roles in controlling metabolic flux distribution in C. tyrobutyricum. The highest butanol titer of 10.0g/L and butanol yield of 27.0% (w/w, 66% of theoretical yield) were achieved from glucose in the ack knockout mutant overexpressing adhE2. When a more reduced substrate mannitol was used, the butanol titer reached 16.0g/L with 30.6% (w/w) yield (75% theoretical yield). Moreover, C. tyrobutyricum showed good butanol tolerance, with >80% and ∼60% relative growth rate at 1.0% and 1.5% (v/v) butanol. These results suggest that C. tyrobutyricum is a promising heterologous host for n-butanol production from renewable biomass. [Copyright &y& Elsevier]

• Different aldehyde/alcohol dehydrogenases were expressed in C. cellulovorans. • Strain overexpressing adh E2 produced 4 g/L n -butanol with a high yield of 0.22 g/g. • Co-expressing bdh B with adh E2 decreased overall butanol production. • Co-expressing adh E1 and bdh B had the highest selectivity for butanol over ethanol. With high cellulolytic and acetic/butyric acids production abilities, Clostridium cellulovorans is promising for use to produce cellulosic n -butanol. Here, we introduced three different aldehyde/alcohol dehydrogenases encoded by bdh B, adh E1, and adh E2 from Clostridium acetobutylicum into C. cellulovorans and studied their effects on ethanol and n -butanol production. Compared to AdhE2, AdhE1 was more specific for n -butanol biosynthesis over ethanol. Co-expressing adh E1 with bdh B produced a comparable amount of butanol but significantly less ethanol, leading to a high butanol/ethanol ratio of 7.0 and 5.6 (g/g) in glucose and cellulose fermentation, respectively. Co-expressing adh E1 or adh E2 with bdh B did not increase butanol production because the activity of BdhB was limited by the NADPH availability in C. cellulovorans. Overall, the strain overexpressing adh E2 alone produced the most n -butanol (4.0 g/L, yield: 0.22 ± 0.01 g/g). Based on the insights from this study, further metabolic engineering of C. cellulovorans for cellulosic n -butanol production is suggested. [ABSTRACT FROM AUTHOR]