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Specific Growth Rate (μ MAX , h -1 ) calculated for each different moment of the log phase. The maximum value was obtained between 36 and 60 hours (0,1028 h -1 ). The slowest growth rate was observed between 60 and 108 hours (0.0102 h -1 ). Dashed line means the average value (0.0369 h -1 ) 

Specific Growth Rate (μ MAX , h -1 ) calculated for each different moment of the log phase. The maximum value was obtained between 36 and 60 hours (0,1028 h -1 ). The slowest growth rate was observed between 60 and 108 hours (0.0102 h -1 ). Dashed line means the average value (0.0369 h -1 ) 

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A wild-type yeast that could ferment D-xylose was isolated from the abdominal content of Nasutitermes sp. collected in the Central Amazon rainforest using sugarcane bagasse hemicellulosic hydrolyzate (SBHH) as selective medium. The yeast was identified as Meyerozyma guilliermondii. Its ability to ferment D-xylose was assessed using liquid medium co...

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... as previously described (Matos et al., 2012). D-xylose assimilation was verified using the replica-plating method in Petri dishes containing D- xylose (50 mM) and YNB wa (6.7 g.L -1 ). Ability to ferment D-xylose was assessed by culturing the isolates in liquid medium composed of D-xylose (40 g.L -1 ) and YNB wa (6.7 g.L -1 ), pH 7.0, containing a Durham tube to identify gas production, as described by Barnett et al. (1990). D-xylose fermentation yield was estimated using a fermentometer assay. Theoretical ethanol production was measured by stoichiometric calculation, as described by Dijck et al. (2000). Taxonomic identification was assessed by molecular and biochemical methods. For molecular identification, genomic DNA was amplified by PCR using an ITS1 primer (5’ TCCGTAGGTGAACCTGCGG 3’). The PCR products were sequenced, and the obtained DNA sequence was submitted to non-redundant nucleotide GenBank database using BLAST (), as described by Zhang et al. (2000). The biochemical profile was verified using the ID32C kit for biochemical tests developed by Biomerieux®. The results were plotted using the online application ApiWeb (Biomerieux ®). A D-xylose-fermenting strain was selected for cultivation in liquid medium using SBHH (TRS = 42.6 g.L -1 ) as the carbon source, supplemented with yeast extract (1.5 g.L -1 ), urea (1.25 g.L -1 ) and KH 2 PO 4 (1.1 g.L -1 ) during 120 hours (120 rpm, pH 5.0). The initial inoculum was 0.125 g.L -1 (wet weight). Saccharification and sugar intake were monitored using the DNS method (Zhao et al., 2010). Cell growth was measured using optical density at 600 nm (OD 600 ) as described by Heer and Sauer (2008). Specific growth rate (μ MAX , h -1 ) was calculated using linear regression by natural logarithm of optical density / initial optical density (ln OD/ODi ) versus time during the log phase, obtaining the equation [ln OD/ODi = μ MAX .t + a] as described by Duarte et al. (2008). Yield biomass (Y X , g.g -1 ) was calculated by evaluating final biomass produced (wet weight) per gram of consumed sugar (DUARTE et al., 2008). Thermotolerance was assessed using lethal heat-shock. The yeast was cultured in Erlenmeyer flasks of 125 mL containing 50 mL of YPD medium composed of yeast extract (10 g.L -1 ), peptone (20 g.L -1 ) and dextrose (20 g.L -1 ) (30 oC, 120 rpm, pH 5.5). After 72 h, the flasks were incubated in a water-bath at 52 oC for 9 minutes and cell viability was measured. Ethanol tolerance was verified through ethanol shock. The yeast was cultivated in YPD (30 oC, 120 rpm). After 72 hours, ethanol was added aseptically at final concentrations of 10% and 20%. The flasks were maintained at 30 oC and 120 rpm for 9 minutes, and cell viability was measured. In both assays, cell viability was quantified using methylene blue staining, as described by Vianna et al. (2008). Ability to grow in the presence of ethanol was assessed by culturing 1.0 mL of cell suspension (OD 600 = 1.0) in YPD containing ethanol 10% (v/v). The control group was composed of Erlenmeyer flasks containing YPD without ethanol. This assay was performed in duplicate. A total of 54 yeast colonies were isolated, with 12 colonies able to assimilate D-xylose and one able to ferment it. This D-xylose-fermenting strain was named LC27. The other isolates were stored in sterilized distilled water for future research. The fermentometer assay lasted a total of 120 hours. The maximum theoretical ethanol yield was estimated to be 3.8 g.L -1 , obtained after 108 hours. The ITS1 sequence, deposited in GenBank with accession number JN974905, corresponds to Pichia guilliermondii , with a maximum identity of 100%. The biochemical profile of LC27 (Table 1) has 95.9% similarity with Candida guilliermondii . According to Lopes et al. (2009), this species is the asexual phase (anamorphous) of P. guilliermondii . Currently, this species has been repositioned in a new genus named Meyerozyma (Kurtzman and Suzuki, 2010). Cell viability after lethal heat-shock and ethanol shock was 39.8% and 56.0%, respectively. Despite its ethanol tolerance, M. guilliermondii LC27 was unable to grow in YPD containing 10% Cultivation of M. guilliermondii LC27 in SBHH had a lag phase of 36 hours. After this time, exponential growth (log phase) was observed until 84 hours, after which a slow cell growth occurred. The stationary phase was observed after 108 hours. The growth curve is presented in Figure 2. Because of the heterogeneous log phase, the μ MAX was calculated for each different time-point of this stage. The maximum value (0.1028 h -1 ) was obtained between36 and 60 hours, and the lowest ethanol. Control flasks reached the log phase after 8 hours of cultivation. The stationary phase was observed after 32 hours, as shown in Figure 1. rate of cell growth (0.0102 h ) was observed between 60 and 108 hours of cultivation. If μ MAX is considered during the entire log phase, the value would be 0.0369 h -1 . Linear regressions are presented in Figure 3. TRS concentration increased 42.6% during the lag phase, obtaining the highest saccharification of SBHH after 4 hours of cultivation. Sugar intake was calculated based on the highest TRS concentration (61,0 g.L -1 ) resulting in 79.5% consumption. Saccharification and subsequent sugar intake are presented in Figure 4. Final biomass produced was 25.26 g.L -1 with Y =0.52 g of biomass produced per gram of consumed sugar. The final pH in SBHH was of 7.6 and final cell viability was of 90.3%. The D-xylose-fermenting strain isolated from termites is a member of the Pichia guilliermondii species (anamorphous Candida guilliermondii ). According to Kurtzman and Suzuki (2010), the genus Pichia is a polyphyletic group. They suggest that P. guilliermondii and P. caribica must be repositioned in a new genus named Meyerozyma based on phylogenetic analysis. Because this proposal has been largely accepted by mycologists, LC27 is referred to as Meyerozyma guilliermondii . There are no reports of this species being associated with termites in Amazonian habitats. The estimated amount of ethanol produced corresponds to 18.6% of the maximum theoretical yield, meaning a low ability for ethanol production under the assessed conditions. Despite its capability to ferment D-xylose, optimal conditions are yet to be established. The cell viability value obtained after lethal heat-shock implies a low tolerance of M. guilliermondii LC27 to high-temperature conditions. This characteristic can reduce its employability in ethanol industries. However, M. guilliermondii LC27 shows the same thermotolerance of some Saccharomyces cerevisiae strains employed in wine production, as demonstrated by Vianna et al. (2008). Furthermore, this isolate has shown ethanol tolerance, meaning that the use of M. guilliermondii LC27 cannot be discarded in industrial processes. The extensive lag phase and slow cell growth during log phase obtained in this work may be closely related to the low mass of inoculated cells, because there is a positive relationship between inoculum size and cell growth/biomass production (GORRET et al., 2004). When saccharification is performed by microorganisms, it is referred to as biosaccharification. The increase of TRS obtained in this work was higher than that obtained by Hernandez-Salas et al. (2009) using commercial enzymatic kits for saccharification of SBHH. Commonly, biosaccharification of SBHH is obtained by releasing xylanases into fermented broth (KUMAR et al., 2012). The pattern observed of sugar intake by M. guilliermondii LC27 is similar to that obtained by Converti et al. (1999) in Pachysolen tannophilus when cultivated in SBHH medium, with 78.6% of sugar consumed. Zhao et al. (2010) and Zou et al. (2010) achieved 85% of sugar intake when cultivating P. tannophilus and Pichia guilliermondii for alcoholic fermentation of D-xylose in synthetic medium. Biomass yield obtained in this work was higher than the values obtained by Nigam (2000) using Candida langeronii for single-cell protein production in SBHH. The increase of pH (from 5.0 to 7.6) and high final cell viability allows us to conclude that M. guilliermondii LC27 was able to perform neutralization of SBHH and presents a high tolerance against microbial growth inhibitors. According to Parawira and Tekere (2011), the anamorphous Candida guilliermondii is able to perform biodetoxification of SBHH and is able to neutralize inhibitor compounds of this substrate. These results agree with Breznak (1982), who in the early eighties predicted that investigations about microbial content of termites' guts would provide new tools for bioconversion of lignocelluloses to fuels and other added-value chemicals. This paper is the first to report Meyerozyma guilliermondii associated with Nasutitermes sp . in the Central Amazon rainforest. The LC27 strain is a D-xylose-fermenting wild-type Meyerozyma guilliermondii , with a biochemical profile corresponding to the anamorphous Candida guilliermondii . It is associated with Nasutitermes sp ., ratifying some early predictions about the biotechnological potential of the microbial community associated with termites. M. guilliermondii LC27 presents the ability to neutralize sugar cane bagasse hemicellulosic hydrolysate and has a high potential for biomass production using this substrate as a carbon source, with higher biomass yields than some industrial strains. The ethanol tolerance, thermotolerance and ability to perform saccharification allow an estimation for biotechnological applications. This work was supported by Fundação de Amparo a Pesquisa do Estado do Amazonas (FAPEAM), Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) and Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq). Special thanks to the Programa de Pós-Graduação em Diversidade Biológica of the Universidade Federal do Amazonas ...

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