Interest in the production of bioethanol from inedible biomass is growing worldwide because of its sustainable supply and lack of competition with food supplies. Candida krusei (also known as Pichia kudriavzevii or Issatchenkia orientalis) is one of the most suitable thermotolerant yeasts used in the simultaneous saccharification and fermentation process for bioethanol production. In the production of bioethanol from lignocellulosic biomass as a feedstock, various environmental conditions occur, and the stress tolerance capacity of C. krusei, especially its low pH and tolerance to inhibitors, limits its practical application. In this study, to select a suitable second-generation bioethanol-producing strain, the tolerance capacity of five available C. krusei strains (NBRC0584, NBRC0841, NBRC1162, NBRC1395 and NBRC1664) was characterized. Spot assay and growth experiment results showed that among the five C. krusei strains, C. krusei NBRC1664 showed superior tolerance capacity for low pH and inhibitors. Furthermore, this strain efficiently produced ethanol from glucose under low pH conditions with or without sulfate. A comparative analysis of the draft genome sequences suggested that Opy2, Sln1 and Cdc24 in the HOG pathway are conserved only in C. krusei NBRC1664, which may contribute to its superior tolerance to low pH levels. Moreover, amino acid sequence alignment showed that aldehyde dehydrogenase family proteins, which catalyze the degradation of cyclic aldehydes, are commonly conserved in C. krusei. In addition, the increased transcription levels in C. krusei NBRC1664 could play a role in its higher tolerance to inhibitors. These results suggest that C. krusei NBRC1664 is a more suitable strain for application in industrial processes for second-generation bioethanol production.

As isobutanol exhibits higher energy density and lower hygroscopicity than ethanol, it is considered a better candidate biofuel. The sustainable supply of inedible biomass and lack of competition with the food supply have stimulated significant worldwide interest in the production of isobutanol from this resource. Both separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF) have been applied to isobutanol production to effectively utilize inedible biomass as a feedstock. However, both processes have various challenges, including low isobutanol yield and high production costs. This review summarizes the potential of isobutanol as a biofuel, methods for conferring isobutanol productivity, recent experimental studies, and developments in both SHF and SSF with the isobutanol-producing strains. Challenges to increasing the isobutanol yield and various suggestions for improvements to enable commercial production are also discussed.

The thermotolerant yeast Pichia kudriavzevii (previously known as Issatchenkia orientalis), can produce ethanol from a variety of carbon sources and grows at around 45 °C. Thus, this yeast is considered a useful biocatalyst for producing ethanol from lignocellulose through simultaneous saccharification and fermentation (SSF). SSF has several advantages, such as a simplified manufacturing process, ease of operation and reduced energy input. Using P. kudriavzevii NBRC1279 and NBRC1664, we previously succeeded in producing ethanol through SSF; however, the extent to which inhibitors by-produced from lignocellulose hydrolysis affect the growth and ethanol productivity of the two strains remains to be investigated. In this study, to better understand the inhibitor tolerance capacity of the two strains, spot assay, growth experiment, real-time quantitative PCR (RT-qPCR) analysis and multiple sequence alignment analysis were carried out. When P. kudriavzevii NBRC1279 and NBRC1664, as well as Saccharomyces cerevisiae BY4742 as a control, were cultured on SCD plates containing 17% ethanol, 42 mM furfural, 56 mM 5-hydroxymethylfurfural (HMF) or 10 mM vanillin, only P. kudriavzevii NBRC1664 was able to grow under all conditions. Moreover, the inhibitor tolerance capacity of P. kudriavzevii NBRC1664 was greater than those of other strains using SCD medium containing the same concentrations of various inhibitors. When an RT-qPCR analysis of seven gene sequences from aldehyde dehydrogenase and the aldehyde dehydrogenase family protein (ADHF) was performed using P. kudriavzevii NBRC1664 cultivated in the presence of 56 mM HMF, ADHF1 and ADHF2 were up-regulated in the early logarithmic growth phase. Moreover, a multiple sequence alignment of the amino acid sequences of ADHF1, ADHF2 and the known ADH suggested that ADHF1 and ADHF2 may catalyze the reversible NAD+-dependent oxidation of HMF. Our data may be useful for future studies on the metabolic engineering of more useful strains for ethanol production from lignocellulose.

Abstract The integration of first‐ (1G) and second‐generation (2G) ethanol production by adding sugarcane juice or molasses to lignocellulosic hydrolysates offers the possibility to overcome the problem of inhibitors (acetic acid, furfural, hydroxymethylfurfural and phenolic compounds), and add nutrients (such as salts, sugars and nitrogen sources) to the fermentation medium, allowing the production of higher ethanol titers. In this work, an 1G2G production process was developed with hemicellulosic hydrolysate (HH) from a diluted sulfuric acid pretreatment of sugarcane bagasse and sugarcane molasses. The industrial Saccharomyces cerevisiae CAT‐1 was genetically modified for xylose consumption and used for co‐fermentation of sucrose, fructose, glucose, and xylose. The fed‐batch fermentation with high cell density that mimics an industrial fermentation was performed at bench scale fermenter, achieved high volumetric ethanol productivity of 1.59 g L⁻¹ h⁻¹, 0.39 g g⁻¹ of ethanol yield, and 44.5 g L⁻¹ ethanol titer, and shown that the yeast was able to consume all the sugars present in must simultaneously. With the results, it was possible to establish a mass balance for the global process: from pretreatment to the co‐fermentation of molasses and HH, and it was possible to establish an effective integrated process (1G2G) with sugarcane molasses and HH co‐fermentation employing a recombinant yeast.

Acetogens grow autotrophically and use hydrogen (H2) as the energy source to fix carbon dioxide (CO2). This feature can be applied to gas fermentation, contributing to a circular economy. A challenge is the gain of cellular energy from H2 oxidation, which is substantially low, especially when acetate formation coupled with ATP production is diverted to other chemicals in engineered strains. Indeed, an engineered strain of the thermophilic acetogen Moorella thermoacetica that produces acetone lost autotrophic growth on H2 and CO2. We aimed to recover autotrophic growth and enhance acetone production, in which ATP production was assumed to be a limiting factor, by supplementing with electron acceptors. Among the four selected electron acceptors, thiosulfate and dimethyl sulfoxide (DMSO) enhanced both bacterial growth and acetone titers. DMSO was the most effective and was further analyzed. We showed that DMSO supplementation enhanced intracellular ATP levels, leading to increased acetone production. Although DMSO is an organic compound, it functions as an electron acceptor, not a carbon source. Thus, supplying electron acceptors is a potential strategy to complement the low ATP production caused by metabolic engineering and to improve chemical production from H2 and CO2.

Simultaneous saccharification and fermentation (SSF) has been investigated for the efficient production of ethanol because it has several advantages such as simplifying the manufacturing process, operating easily, and reducing energy input. Previously, using lignocellulosic biomass as source materials, we succeeded in producing ethanol by SSF with Pichia kudriavzevii NBRC1279 and NBRC1664. However, various acids that fermentation inhibitors are also produced by the hydrolysis of lignocellulosic biomass, and the extent to which these acids affect the growth and ethanol productivity of the two strains has not yet been investigated. In this study, to better understand the acid tolerance mechanism of the two strains, a spot assay, growth experiment, and transcriptome analysis were carried out using Saccharomyces cerevisiae BY4742 as a control. When the three strains were cultured in SCD medium containing 15 mM formic acid, 35 mM sulfuric acid, 60 mM hydrochloric acid, 100 mM acetic acid, or 550 mM lactic acid, only P. kudriavzevii NBRC1664 could grow well under all conditions, and it showed the fastest growth rates. The transcriptome analysis showed that “MAPK signaling pathway-yeast” was significantly enriched in P. kudriavzevii NBRC1664 cultured with 60 mM hydrochloric acid, and most genes involved in the high osmolarity glycerol (HOG) pathway were up-regulated. Therefore, the up-regulation of the HOG pathway may be important for adapting to acid stress in P. kudriavzevii. Moreover, the log2-transformed fold change value in the expression level of Gpd1 was 1.3-fold higher in P. kudriavzevii NBRC1664 than in P. kudriavzevii NBRC1279, indicating that high Gpd1 expression may be accountable for the higher acid tolerance of P. kudriavzevii NBRC1664. The transcriptome analysis performed in this study provides preliminary knowledge of the molecular mechanism of acid stress tolerance in P. kudriavzevii. Our data may be useful for future studies on methods to improve the tolerance of P. kudriavzevii to acids produced from lignocellulose hydrolysis.

Hydrogen (H2) converted to reducing equivalents is used by acetogens to fix and metabolize carbon dioxide (CO2) to acetate. The utilization of H2 enables not only autotrophic growth, but also mixotrophic metabolism in acetogens, enhancing carbon utilization. This feature seems useful, especially when the carbon utilization efficiency of organic carbon sources is lowered by metabolic engineering to produce reduced chemicals, such as ethanol. The potential advantage was tested using engineered strains of Moorella thermoacetica that produce ethanol. By adding H2 to the fructose-supplied culture, the engineered strains produced increased levels of acetate, and a slight increase in ethanol was observed. The utilization of a knockout strain of the major acetate production pathway, aimed at increasing the carbon flux to ethanol, was unexpectedly hindered by H2-mediated growth inhibition in a dose-dependent manner. Metabolomic analysis showed a significant increase in intracellular NADH levels due to H2 in the ethanol-producing strain. Higher NADH level was shown to be the cause of growth inhibition because the decrease in NADH level by dimethyl sulfoxide (DMSO) reduction recovered the growth. When H2 was not supplemented, the intracellular NADH level was balanced by the reversible electron transfer from NADH oxidation to H2 production in the ethanol-producing strain. Therefore, reversible hydrogenase activity confers the ability and flexibility to balance the intracellular redox state of M. thermoacetica. Tuning of the redox balance is required in order to benefit from H2-supplemented mixotrophy, which was confirmed by engineering to produce acetone.

Gas fermentation is a promising biological process for the conversion of CO2 or syngas into valuable chemicals. Homoacetogens are microorganisms growing autotrophically using CO2 and H2 or CO and metabolizing them to form acetate coupled with energy conservation. The challenge in the metabolic engineering of the homoacetogens is divergence of the acetate formation, whose intermediate is acetyl-CoA, to a targeted chemical with sufficient production of adenosine triphosphate (ATP). In this study, we report that an engineered strain of the thermophilic homoacetogen Moorella thermoacetica, in which a pool of acetyl-CoA is diverted to ethanol without ATP production, can maintain autotrophic growth on syngas. We estimated the ATP production in the engineered strains under different gaseous compositions by considering redox-balanced metabolism for ethanol and acetate formation. The culture test showed that the combination of retaining a level of acetate production and supplying the energy-rich CO allowed maintenance of the autotrophic growth during ethanol production. In contrast, autotrophy was collapsed by complete elimination of the acetate pathway or supplementation of H2-CO2. We showed that the intracellular level of ATP was significantly lowered on H2-CO2 in consistent with the incompetence. In the meantime, the complete disruption of the acetate pathway resulted in the redox imbalance to produce ethanol from CO, albeit a small loss in the ATP production. Thus, preservation of a fraction of acetate formation is required to maintain sufficient ATP and balanced redox in CO-containing gases for ethanol production.

First-generation ethanol (E1G) is based on the fermentation of sugars released from saccharine or starch sources, while second-generation ethanol (E2G) is focused on the fermentation of sugars released from lignocellulosic feedstocks. During the fractionation process to release sugars from hemicelluloses (mainly xylose), some inhibitor compounds are released hindering fermentation. Thus, the biggest challenge of using hemicellulosic hydrolysate is selecting strains and processes able to efficiently ferment xylose and tolerate inhibitors. With the aim of diluting inhibitors, sugarcane molasses (80% of sucrose content) can be mixed to hemicellulosic hydrolysate in an integrated E1G-E2G process. Cofermentations of xylose and sucrose were evaluated for the native xylose consumer Spathaspora passalidarum and a recombinant Saccharomyces cerevisiae strain. The industrial S. cerevisiae strain CAT-1 was modified to overexpress the XYL1, XYL2, XKS1 genes and a mutant ([4-59Δ]HXT1) version of the low-affinity HXT1 permease, generating strain MP-C5H1. Although S. passalidarum showed better results for xylose fermentation, this yeast showed intracellular sucrose hydrolysis and low sucrose consumption in microaerobic conditions. Recombinant S. cerevisiae showed the best performance for cofermentation, and a batch strategy at high cell density in bioreactor achieved unprecedented results of ethanol yield, titer and volumetric productivity in E1G-E2G production process.

Klebsiella pneumoniae subsp. pneumoniae CCI2 was isolated from leaf soil collected in Hiroshima Prefecture, Japan. The draft genome sequence comprises 78 contigs and contains 5,075,115 bp with a G+C content of 57.7%.

The filamentous fungus Talaromyces cellulolyticus is a well-characterized cellulolytic and hemicellulolytic enzyme producer. In this study, the function of the tclB2 gene, which is a homolog of the manR/clrB/clr-2 gene in other filamentous fungi, in mannanolytic enzyme production by T. cellulolyticus was investigated. When a tclB2-disrupted strain (YDTclB) was grown in the presence of glucomannan, the production of β-mannanase, β-mannosidase, and α-galactosidase was decreased at the protein and transcriptional levels when compared to the control strain. In addition, a tclB2-overexpressing strain (YHTclB) showed higher β-mannanase and β-mannosidase production. When cellulose was used as a carbon source, the expression of genes encoding mannanolytic enzymes also decreased in YDTclB. These results suggested that TclB2 contributes to mannanolytic enzyme production in T. cellulolyticus. This work is the first study to identify a transcriptional regulator of mannanolytic enzyme genes in T. cellulolyticus.

Simultaneous saccharification and fermentation (SSF) is capable of performing enzymatic saccharification and fermentation for biofuel production in a single vessel. Thus, SSF has several advantages such as simplifying the manufacturing process, operating easily, and reducing energy input. Here, we describe the application of Pichia kudriavzevii NBRC1279 and NBRC1664 to SSF for bioethanol production. When each strain was incubated for 144 h at 35 °C with Japanese cedar particles, the highest ethanol concentrations were reached 21.9 ± 0.50 g/L and 23.8 ± 3.9 g/L, respectively. In addition, 21.6 ± 0.29 g/L and 21.3 ± 0.21 g/L of bioethanol were produced from Japanese eucalyptus particles when each strain was incubated for 144 h at 30 °C. Although previous methods require pretreatment of the source material, our method does not require pretreatment, which is an advantage for industrial use. To elucidate the different characteristics of the strains, we performed genome sequencing and genome comparison. Based on the results of the eggNOG categories and the resulting Venn diagram, the functional abilities of both strains were similar. However, strain NBRC1279 showed five retrotransposon protein genes in the draft genome sequence, which indicated that the stress tolerance of both strains is slightly different.

Strain CCI5, an oligotrophic bacterium, was isolated from leaf soil collected in Japan. Strain CCI5 grew at temperatures between 25 °C and 43 °C (optimum temperature, 40 °C) and at pHs between 6.0 and 10.0 (optimum pH, 9.0). Its major fatty acids were anteiso-C15:0 and iso-C16:0, and menaquinone 7 was the only detected quinone system. In a phylogenetic analysis based on 16S rRNA gene sequences, strain CCI5 presented as a member of the genus Paenibacillus. Moreover, multilocus sequence analysis based on partial sequences of the atpD, dnaA, gmk, and infB genes showed that strain CCI5 tightly clustered with P. glycanilyticus DS-1T. The draft genome of strain CCI5 consisted of 6,864,972 bp with a G+C content of 50.7% and comprised 6,189 predicted coding sequences. The genome average nucleotide identity value (97.8%) between strain CCI5 and P. glycanilyticus DS-1T was below the cut-off value for prokaryotic subspecies delineation. Based on its phenotypic, chemotaxonomic, and phylogenetic features, strain CCI5 (= HUT-8145T = KCTC 43270T) can be considered as a novel subspecies within the genus Paenibacillus with the proposed name Paenibacillus glycanilyticus subsp. hiroshimensis subsp. nov.

Gas fermentation is one of the promising bioprocesses to convert CO2 or syngas to important chemicals. Thermophilic gas fermentation of volatile chemicals has the potential for the development of consolidated bioprocesses that can simultaneously separate products during fermentation. This study reports the production of acetone from CO2 and H2, CO, or syngas by introducing the acetone production pathway using acetyl-coenzyme A (Ac-CoA) and acetate produced via the Wood-Ljungdahl pathway in Moorella thermoacetica. Reducing the carbon flux from Ac-CoA to acetate through genetic engineering successfully enhanced acetone productivity, which varied on the basis of the gas composition. The highest acetone productivity was obtained with CO-H2, while autotrophic growth collapsed with CO2-H2. By adding H2 to CO, the acetone productivity from the same amount of carbon source increased compared to CO gas only, and the maximum specific acetone production rate also increased from 0.04 to 0.09 g-acetone/g-dry cell/h. Our development of the engineered thermophilic acetogen M. thermoacetica, which grows at a temperature higher than the boiling point of acetone (58 °C), would pave the way for developing a consolidated process with simplified and cost-effective recovery via condensation following gas fermentation.

Enterobacter oligotrophicus CCA3 was isolated from leaf soil collected in Hiroshima Prefecture, Japan. Here, we report the draft genome sequence of E. oligotrophicus CCA3. The draft genome sequence of E. oligotrophicus CCA3 consists of 29 contigs of 4,425,100 bp, with a GC content of 54.2%.

Strain CCI9, which was isolated from leaf soil collected in Japan, was capable of growth on poor-nutrient medium, at temperatures of 10°C to 45°C, at pHs of 4.5 to 10, and in the presence of 7.0% NaCl. We determined a draft genome sequence of strain CCI9, which consists of a total of 28 contigs containing 4,644,734 bp with a GC content of 56.1%. This assembly yielded 4,154 predicted coding sequences. Multilocus sequence analysis (MLSA) based on atpD, gyrB, infB, and rpoB gene sequences were performed to further identify strain CCI9. The MLSA revealed that strain CCI9 clustered tightly with Enterobacter roggenkampii EN-117T. Moreover, the average nucleotide identity value (98.6%) between genome sequences of strain CCI9 and E. roggenkampii EN-117T exceeds the cutoff value for prokaryotic subspecies delineation. Therefore, strain CCI9 was identified as E. roggenkampii CCI9. To clarify differences between E. roggenkampii EN-117T and CCI9, the coding proteins were compared against the eggNOG database.

meso-Diaminopimelate dehydrogenase (meso-DAPDH) catalyzes the reversible NADP+-dependent oxidative deamination of meso-2,6-diaminopimelate (meso-DAP) to produce l-2-amino-6-oxopimelate. meso-DAPDH is divided into two major clusters, types I and II, based on substrate specificity and structural characteristic. Here, we describe a novel type II meso-DAPDH from Thermosyntropha lipolytica (TlDAPDH). The gene encoding a putative TlDAPDH was expressed in Escherichia coli cells, and then the enzyme was purified 7.3-fold to homogeneity from the crude cell extract. The molecule of TlDAPDH seemed to form a hexamer, which is the typical structural characteristic of type II meso-DAPDHs. The purified enzyme exhibited oxidative deamination activity toward meso-DAP with both NADP+ and NAD+ as coenzymes. TlDAPDH exhibited reductive amination activity of corresponding 2-oxo acid to produce d-amino acid. In particular, the productivities for d-aspartate and d-glutamate have not been reported in the type II enzymes. The optimum pH and temperature for oxidative deamination of meso-DAP were 10.5 and 55°C, respectively. TlDAPDH retained more than 80% of its activity after incubation for 30 min at temperatures between 50°C and 65°C and in the pH range of 4.5-9.5. Moreover, the coenzyme and substrate recognition mechanisms of TlDAPDH were elucidated based on a multiple sequence alignment and the homology model. The results of these analyses suggested that the molecular mechanisms for coenzyme and substrate recognition of TlDAPDH were similar to those of meso-DAPDH from S. thermophilum, which is the representative type II enzyme. Based on the kinetic characteristics and structural comparison, TlDAPDH was considered to be a novel type II meso-DAPDH.

The discharge of industrial dyes and their breakdown products are often environmentally harmful. Here, we describe a biodegradation method using Burkholderia multivorans CCA53, which exhibits a capacity to degrade azo dyes, particularly ethyl red. Under the optimized culture conditions, 100 μM ethyl red was degraded more than 99% after incubation for 8 h. Real-time PCR analysis of azoR1 and azoR2, encoding two azoreductases, revealed that transcription level of these genes is enhanced at early phase under the optimized conditions. For a more practical approach, hydrolysates were prepared from eucalyptus or Japanese cedar chips or rice straw, and rice straw hydrolysate was used as the best medium for ethyl red biodegradation. Under those conditions, ethyl red was also degraded with high efficiency (>91%). We have thus constructed a potentially economical method for the biodegradation of ethyl red.

GH30-7 endoxylanase C from the cellulolytic fungus Talaromyces cellulolyticus (TcXyn30C) belongs to glycoside hydrolase family 30 subfamily 7, and specifically releases 22-(4-O-methyl-α-D-glucuronosyl)-xylobiose from glucuronoxylan, as well as various arabino-xylooligosaccharides from arabinoxylan. TcXyn30C has a modular structure consisting of a catalytic domain and a C-terminal cellulose-binding module 1 (CBM1). In this study, the crystal structure of a TcXyn30C mutant which lacks the CBM1 domain was determined at 1.65 Å resolution. The structure of the active site of TcXyn30C was compared with that of the bifunctional GH30-7 xylanase B from T. cellulolyticus (TcXyn30B), which exhibits glucuronoxylanase and xylobiohydrolase activities. The results revealed that TcXyn30C has a conserved structural feature for recognizing the 4-O-methyl-α-D-glucuronic acid (MeGlcA) substituent in subsite -2b. Additionally, the results demonstrated that Phe47 contributes significantly to catalysis by TcXyn30C. Phe47 is located in subsite -2b and also near the C-3 hydroxyl group of a xylose residue in subsite -2a. Substitution of Phe47 with an arginine residue caused a remarkable decrease in the catalytic efficiency towards arabinoxylan, suggesting the importance of Phe47 in arabinoxylan hydrolysis. These findings indicate that subsite -2b of TcXyn30C has unique structural features that interact with arabinofuranose and MeGlcA substituents.

Pyruvate, a potential precursor of various chemicals, is one of the fundamental chemicals produced by the fermentation process. We previously reported a pyruvate-producing Escherichia coli strain LAFCPCPt-accBC-aceE (PYR) that has the potential to be applied to the industrial production of pyruvate. In this study, the availability of the PYR strain for the production of pyruvate-derivative chemicals was evaluated using a d-lactate-producing strain (LAC) based on the PYR strain. The LAC strain expresses a d-lactate dehydrogenase-encoding gene from Lactobacillus bulgaricus under the control of a T7 expression system. The d-lactate productivity of the LAC strain was further improved by limiting aeration and changing the induction period for the expression of d-lactate dehydrogenase-encoding gene expression. Under combined conditions, the LAC strain produced d-lactate at 21.7 ± 1.4 g·L−1, which was compatible with the pyruvate production by the PYR strain (26.1 ± 0.9 g·L−1). These results suggest that we have succeeded in the effective conversion of pyruvate to d-lactate in the LAC strain, demonstrating the wide versatility of the parental PYR strain as basal strain for various chemicals production.

Xylanase B, a member of subfamily 7 of the GH30 (glycoside hydrolase family 30) from Talaromyces cellulolyticus (TcXyn30B), is a bifunctional enzyme with glucuronoxylanase and xylobiohydrolase activities. In the present study, crystal structures of the native enzyme and the enzyme-product complex of TcXyn30B expressed in Pichia pastoris were determined at resolutions of 1.60 and 1.65 Å, respectively. The enzyme complexed with 22 -(4-O-methyl-α-d-glucuronyl)-xylobiose (U4m2 X) revealed that TcXyn30B strictly recognizes both the C-6 carboxyl group and the 4-O-methyl group of the 4-O-methyl-α-d-glucuronyl side chain by the conserved residues in GH30-7 endoxylanases. The crystal structure and site-directed mutagenesis indicated that Asn-93 on the β2-α2-loop interacts with the non-reducing end of the xylose residue at subsite-2 and is likely to be involved in xylobiohydrolase activity. These findings provide structural insight into the mechanisms of substrate recognition of GH30-7 glucuronoxylanase and xylobiohydrolase.

Talaromyces cellulolyticus is a promising strain for industrial cellulase production. In this study, the thaB gene, which is a homologue of the hap2/B gene in other filamentous fungi, was isolated and characterized. When grown in the presence of cellulose, culture supernatants of a thaB-disrupted strain (YDTha) exhibited decreased cellulase and xylanase enzymatic activities compared to the control strain. Furthermore, YDTha exhibited lower expression of the genes encoding cellulases and xylanases compared to the control strain. When cellobiose and lactose (soluble carbon sources) were used as carbon sources, the expression of the genes encoding cellulases and xylanases was decreased in both the YDTha and the control strains, though the expression levels in YDTha remained lower than those in the control strain. These results suggested that thaB has a positive role in cellulase and xylanase production in T. cellulolyticus.

Glycoside hydrolase family 30 subfamily 7 (GH30-7) enzymes include various types of xylanases, such as glucuronoxylanase, endoxylanase, xylobiohydrolase, and reducing-end xylose-releasing exoxylanase. Here, we characterized the mode of action and gene expression of the GH30-7 endoxylanase from the cellulolytic fungus Talaromyces cellulolyticus (TcXyn30C). TcXyn30C has a modular structure consisting of a GH30-7 catalytic domain and a C-terminal cellulose binding module 1, whose cellulose-binding ability has been confirmed. Sequence alignment of GH30-7 xylanases exhibited that TcXyn30C has a conserved Phe residue at the position corresponding to a conserved Arg residue in GH30-7 glucuronoxylanases, which is required for the recognition of the 4-O-methyl-α-d-glucuronic acid (MeGlcA) substituent. TcXyn30C degraded both glucuronoxylan and arabinoxylan with similar kinetic constants and mainly produced linear xylooligosaccharides (XOSs) with 2 to 3 degrees of polymerization, in an endo manner. Notably, the hydrolysis of glucuronoxylan caused an accumulation of 22-(MeGlcA)-xylobiose (U4m2X). The production of this acidic XOS is likely to proceed via multistep reactions by putative glucuronoxylanase activity that produces 22-(MeGlcA)-XOSs (X n U4m2X, n ≥ 0) in the initial stages of the hydrolysis and by specific release of U4m2X from a mixture containing X n U4m2X. Our results suggest that the unique endoxylanase activity of TcXyn30C may be applicable to the production of linear and acidic XOSs. The gene xyn30C was located adjacent to the putative GH62 arabinofuranosidase gene (abf62C) in the T. cellulolyticus genome. The expression of both genes was induced by cellulose. The results suggest that TcXyn30C may be involved in xylan removal in the hydrolysis of lignocellulose by the T. cellulolyticus cellulolytic system.IMPORTANCE Xylooligosaccharides (XOSs), which are composed of xylose units with a β-1,4 linkage, have recently gained interest as prebiotics in the food and feed industry. Apart from linear XOSs, branched XOSs decorated with a substituent such as methyl glucuronic acid and arabinose also have potential applications. Endoxylanase is a promising tool in producing XOSs from xylan. The structural variety of XOSs generated depends on the substrate specificity of the enzyme as well as the distribution of the substituents in xylan. Thus, the exploration of endoxylanases with novel specificities is expected to be useful in the provision of a series of XOSs. In this study, the endoxylanase TcXyn30C from Talaromyces cellulolyticus was characterized as a unique glycoside hydrolase belonging to the family GH30-7, which specifically releases 22-(4-O-methyl-α-d-glucuronosyl)-xylobiose from hardwood xylan. This study provides new insights into the production of linear and branched XOSs by GH30-7 endoxylanase.

Construction of acid-tolerant strains of Saccharomyces cerevisiae is required for various bioproduction processes. We previously isolated the gene IoGAS1 from multiple stress-tolerant Issatchenkia orientalis as a gene conferring sulfuric acid resistance in S. cerevisiae, but its acid tolerance was only investigated using sulfuric acid. Here, we evaluated the growth and ethanol fermentation ability of the IoGAS1-expressing S. cerevisiae strain, B4-IoGAS1, by using various acidic reagents. B4-IoGAS1 exhibited faster growth than the control strain, B4-CON, when cultured aerobically with sulfuric, hydrochloric, formic, acetic, and lactic acids at pH below 2.4. However, the growth of B4-IoGAS1 was suppressed at pH above 2.48, irrespective of the type of acid reagents. Furthermore, B4-IoGAS1 exhibited higher performance of ethanol fermentation than B4-CON under 250 mM lactic acid condition at pH 2.37. These results demonstrate that IoGAS1 could facilitate the aerobic growth and anaerobic ethanol production under different acidic stressed conditions.

In this study, we characterized the mode of action of reducing-end xylose-releasing exoxylanase (Rex), which belongs to the glycoside hydrolase family 30-7 (GH30-7). GH30-7 Rex, isolated from the cellulolytic fungus Talaromyces cellulolyticus (Xyn30A), exists as a dimer. The purified Xyn30A released xylose from linear xylooligosaccharides (XOSs) 3 to 6 xylose units in length with similar kinetic constants. Hydrolysis of branched, borohydride-reduced, and p-nitrophenyl XOSs clarified that Xyn30A possesses a Rex activity. 1H nuclear magnetic resonance (1H NMR) analysis of xylotriose hydrolysate indicated that Xyn30A degraded XOSs via a retaining mechanism and without recognizing an anomeric structure at the reducing end. Hydrolysis of xylan by Xyn30A revealed that the enzyme continuously liberated both xylose and two types of acidic XOSs: 22-(4-O-methyl-α-d-glucuronyl)-xylotriose (MeGlcA2Xyl3) and 22-(MeGlcA)-xylobiose (MeGlcA2Xyl2). These acidic products were also detected during hydrolysis using a mixture of MeGlcA2Xyl n (n = 2 to 14) as the substrate. This indicates that Xyn30A can release MeGlcA2Xyl n (n = 2 and 3) in an exo manner. Comparison of subsites in Xyn30A and GH30-7 glucuronoxylanase using homology modeling suggested that the binding of the reducing-end residue at subsite +2 was partially prevented by a Gln residue conserved in GH30-7 Rex; additionally, the Arg residue at subsite -2b, which is conserved in glucuronoxylanase, was not found in Xyn30A. Our results lead us to propose that GH30-7 Rex plays a complementary role in hydrolysis of xylan by fungal cellulolytic systems.IMPORTANCE Endo- and exo-type xylanases depolymerize xylan and play crucial roles in the assimilation of xylan in bacteria and fungi. Exoxylanases release xylose from the reducing or nonreducing ends of xylooligosaccharides; this is generated by the activity of endoxylanases. β-Xylosidase, which hydrolyzes xylose residues on the nonreducing end of a substrate, is well studied. However, the function of reducing-end xylose-releasing exoxylanases (Rex), especially in fungal cellulolytic systems, remains unclear. This study revealed the mode of xylan hydrolysis by Rex from the cellulolytic fungus Talaromyces cellulolyticus (Xyn30A), which belongs to the glycoside hydrolase family 30-7 (GH30-7). A conserved residue related to Rex activity is found in the substrate-binding site of Xyn30A. These findings will enhance our understanding of the function of GH30-7 Rex in the cooperative hydrolysis of xylan by fungal enzymes.

遂行予定の研究全体像は、電気を食べる微生物（電極酸化細菌）を用いたバイオリアクターで廃棄物処理・有価物生産同時プロセス（電気発酵）の構築を目指すものである。本装置は電気化学的培養装置であり、電極還元細菌と電極酸化細菌の二種類の微生物群が電極・導線を通じ電子をやり取りして物質生産を行う。本技術の特徴は最終電子受容を行う電極酸化細菌（純菌）を陽極に隔離し、エサを電流のみに制限することで廃水（廃棄物）を原料に高付加価値物質（化学品・医薬品など）を生産しうるという点であり、本研究の目的は電気をエサに様々な有価物を生産可能な微生物触媒である電極酸化細菌を育種するために、新興ゲノム編集技術であるCRISPR/Cas9を用いて当該細菌への遺伝子導入すること及び、その導入遺伝子資源を網羅的に獲得すること、さらには遺伝子導入による新規物質生産システムを構築することの3点である。 平成30年度は(1)電極酸化物質生産システムの構築、(2)固相電気培養システムによる新規遺伝子資源の獲得及び(3)CRISPR/Cas9による組換え系の構築に取り組んだ。(1)では既知電極酸化細菌である好熱菌Moorella sp. Y72株を用いて酢酸を生産する物質生産系の構築に成功した。(2)の取り組みでは平成30年度までに固体培地上で電極酸化細菌と考えられる細菌の優占的培養に成功した。今後分離株を用いたゲノムシーケンスに取り組んでいく。(3)ではY72株を用いて、当該株のゲノム内にCas9をはじめとするゲノム編集関連遺伝子の導入に取り組み、導入及び発現に成功した。今後Cas9によるゲノム切断の効率を高めるため、最適な発現・反応条件を検討していく。

多段階His-Aspリン酸リレーに関与する典型的な環境センサーである大腸菌のArcBは細胞内代謝物であるNAD^+をシグナルとしてArcBドメイン内のPASドメインを介してシグナルを感知しているということを明らかにした。 また最近、高等植物のシロイヌナズナの擬似レギュレーターAPRRが5種類存在することを発見し、それらの転写発現が全てサーカディアンリズムを示すことを明らかにした。しかも、APRR9→APRR7→APRR5→APRR3→APRR1の順に規則正しく発現リズムを刻んだ(APRR五重奏)。さらに初発のAPRR9が光誘導性であることも明らかにした。 今回、APRRファミリーが時を刻む機構と関連しているか否かを更に検討するために、時計関連遺伝子CCA1構成的発現植物体に加え、APRR1構成的発現植物体を用いて、これらの変異植物体におけるAPRRファミリーの発現様式を詳細に解析した。その結果、得られた新規の重要な知見としては、APRRファミリーとCCA1/LHYのサーカディアン発現リズムが強く相互に影響を与えること、さらにはAPRR1がyeast two-hybridによるスクリーニングによってAPRR1と相互作用する遺伝子として取得したPIL1と共に転写活性化因子であるPIF3の機能を抑制することでAPRR9の発現を抑制していることであった。PIL1はbHLHモチーフをもつタンパク質であり、そのbHLH領域はフィトクロム相互作用因子であるPIF3のbHLH領域と非常に高い相同性を示した。以上の結果から、APRRファミリーはシロイヌナズナの概日時計と深く関わった働きをしていることが強く支持された。