First- and second-generation integrated process for bioethanol production: Fermentation of molasses diluted with hemicellulose hydrolysate by recombinant Saccharomyces cerevisiae.

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.

Enhancing acetone production from H2 and CO2 using supplemental electron acceptors in an engineered Moorella thermoacetica.

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.

Prospecting and engineering yeasts for ethanol production under inhibitory conditions: an experimental design analysis.

The recently discovered wild yeast Wickerhamomyces sp. UFFS-CE-3.1.2 was analyzed through a high-throughput experimental design to improve ethanol yields in synthetic media with glucose, xylose, and cellobiose as carbon sources and acetic acid, furfural, formic acid, and NaCl as fermentation inhibitors. After Plackett-Burman (PB) and central composite design (CCD), the optimized condition was used in a fermentation kinetic analysis to compare this yeast's performance with an industrial Saccharomyces cerevisiae strain (JDY-01) genetically engineered to achieve a higher xylose fermentation capacity and fermentation inhibitors tolerance by overexpressing the genes XYL1, XYL2, XKS1, and TAL1. Our results show that furfural and NaCl had no significant effect on sugar consumption by UFFS-CE-3.1.2. Surprisingly, acetic acid negatively affected glucose but not xylose and cellobiose consumption. In contrast, the pH positively affected all the analyzed responses, indicating a cell's preference for alkaline environments. In the CCD, sugar concentration negatively affected the yields of ethanol, xylitol, and cellular biomass. Therefore, fermentation kinetics were carried out with the average concentrations of sugars and fermentation inhibitors and the highest tested pH value (8.0). Although UFFS-CE-3.1.2 fermented glucose efficiently, xylose and cellobiose were mainly used for cellular growth. Interestingly, the genetically engineered strain JDY-01 consumed ~ 30% more xylose and produced ~ 20% more ethanol. Also, while UFFS-CE-3.1.2 only consumed 32% of the acetic acid of the medium, JDY-01 consumed > 60% of it, reducing its toxic effects. Thus, the overexpressed genes played an essential role in the inhibitors' tolerance, and the applied engineering strategy may help improve 2G ethanol production.

Reversible Hydrogenase Activity Confers Flexibility to Balance Intracellular Redox in Moorella thermoacetica.

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.

Comparison of Spathaspora passalidarum and recombinant Saccharomyces cerevisiae for integration of first- and second-generation 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 and 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.

Autotrophic growth and ethanol production enabled by diverting acetate flux in the metabolically engineered Moorella thermoacetica.

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.

The Transcription Factor Gene tclB2 Regulates Mannanolytic Enzyme Production in the Fungus Talaromyces cellulolyticus.

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 ß-mannanase, ß-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 ß-mannanase and ß-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.

Draft Genome Sequence of Klebsiella pneumoniae subsp. pneumoniae CCI2, Isolated from Leaf Soil.

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%.

Metabolic engineering of Moorella thermoacetica for thermophilic bioconversion of gaseous substrates to a volatile chemical.

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.

Isolation, draft genome sequencing and identification of Enterobacter roggenkampii CCI9.

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.

Draft Genome Sequence of Enterobacter oligotrophicus CCA3, Isolated from Leaf Soil.

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%.

Paenibacillus glycanilyticus subsp. hiroshimensis subsp. nov., isolated from leaf soil collected in Japan.

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.

Crystal structure of GH30-7 endoxylanase C from the filamentous fungus Talaromyces cellulolyticus.

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 Šresolution. 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.

Performance of Burkholderia multivorans CCA53 for ethyl red degradation.

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.

Characterization of an NAD(P)+-dependent meso-diaminopimelate dehydrogenase from Thermosyntropha lipolytica.

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.

Identification and functional characterization of NAD(P)+ -dependent meso-diaminopimelate dehydrogenase from Numidum massiliense.

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. Moreover, d-amino acid dehydrogenase (d-AADHs) derived from protein-engineered meso-DAPDH is useful for one-step synthesis of d-amino acids with high optical purity. Here, we report the identification and functional characterization of a novel NAD(P)+ -dependent meso-DAPDH from Numidum massiliense (NmDAPDH). After the gene encoding the putative NmDAPDH was expressed in recombinant Escherichia coli cells, the enzyme was purified 4.0-fold to homogeneity from the crude extract through five purification steps. Although the previously known meso-DAPDHs use only NADP+ as a coenzyme, NmDAPDH was able to use both NADP+ and NAD+ as coenzymes. When NADP+ was used as a coenzyme, NmDAPDH exhibited an approximately 2 times higher kcat /Km value toward meso-DAP than that of meso-DAPDH from Symbiobacterium thermophilum (StDAPDH). NmDAPDH also catalyzed the reductive amination of corresponding 2-oxo acids to produce acidic d-amino acids such as d-aspartate and d-glutamate. The optimum pH and temperature for the oxidative deamination of meso-DAP were about 10.5 and 75°C, respectively. Like StDAPDH, NmDAPDH exhibited high stability: it retained more than 75% of its activity after 30 min at 60°C (pH 7.2) or at pHs ranging from 5.5 to 13.0 (50°C). Alignment of the amino acid sequences of NmDAPDH and the known meso-DAPDHs suggested NmDAPDH has a hexameric structure. Given its specificity for both NADP+ and NAD+ , high stability, and a broad range of reductive amination activity toward 2-oxo acids, NmDAPDH appears to offer advantages for engineering a more effective d-AADH.

Substrate recognition by a bifunctional GH30-7 xylanase B from Talaromyces cellulolyticus.

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 ß2-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.

Deinococcus kurensis sp. nov., isolated from pond water collected in Japan.

An aerobic, oligotrophic, Gram-positive, non-sporulating, motile, rod-shaped, palladium-leaching bacterial strain, Deinococcus sp. KR-1, was previously isolated from pond water collected in Japan. This strain grew at 10 °C to 40 °C (optimum 30 °C), at pH 4.5 to 11.5 (optimum pH 8.0), and in the presence of 2.0% NaCl. Its major cellular fatty acids were C15: 1ω6 and C16 : 1ω7c. The quinone system was menaquinone 8. Multilocus sequence analysis based on partial sequences of four housekeeping genes (atpD, dnaA, gyrB and rpoB) showed that branching of Deinococcus sp. KR-1 was distant to those of Deinococcus type strains. The genome average nucleotide identity value between strain KR-1 and its closest related Deinococcus type strain was less than 95.69%. Based on its phenotypic, chemotaxonomic and phylogenetic data, strain KR-1 (= HUT-8138T = KCTC 33977T) can be considered a novel species within the genus Deinococcus with the proposed name Deinococcus kurensis sp. nov.

Draft genome sequence of Deinococcus sp. KR-1, a potential strain for palladium-leaching.

Strain KR-1 was isolated from pond water collected in Japan. Because this strain was capable of adsorbing palladium particles in sterilized water, strain KR-1 will be a useful biocatalyst for palladium-leaching from metal waste. Here we present a draft genome sequence of Deinococcus sp. KR-1, which consists of a total of 7 contigs containing 4,556,772 bp with a GC content of 70.0% and comprises 4,450 predicted coding sequences. Based on the 16S rRNA gene sequence analysis, strain KR-1 was identified as Deinococcus sp. KR-1.

IoGAS1, a GPI-Anchored Protein Derived from Issatchenkia orientalis, Confers Tolerance of Saccharomyces cerevisiae to Multiple Acids.

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.