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Vol.:(0123456789) 1 3 Food and Bioprocess Technology https://doi.org/10.1007/s11947-023-03108-y RESEARCH Approaching Study ontheRelationship Between Saccharomyces cerevisiae Production ofTyrosol, Hydroxytyrosol, andMelatonin withVolatile Compounds inFermented Must MarinaGonzalez‑Ramirez1· MariaMarMarin‑Torres1· MartaGallardo‑Fernandez1· AndresPlanells‑Carcel2· RicardoBisquert2· EvaValero3· CristinaUbeda1· AnaMariaTroncoso1· MariaCarmenGarcia‑Parrilla1 Received: 30 January 2023 / Accepted: 19 April 2023 © The Author(s) 2023 Abstract Yeasts are feasible and effective bioreactors and, therefore, there is a great interest in their industrial employment for the production of a wide range of molecules. In this study, the production by Saccharomyces cerevisiae of bioactive compounds such as hydroxytyrosol (HT), tyrosol (TYR) and melatonin (MEL) vs. volatile compounds in fermented must was studied. The concentration of the bioactive compounds HT and MEL in fermented must employing different yeast strains revealed that the higher the concentrations, the lower the amount of volatile compounds determined. This inverse correlation was especially remarkable with respect to the production of higher alcohols, especially 2-phenylethanol (2-PE) and esters. Furthermore, the employment of a modified Aro4pK229L S. cerevisiae QA23 yeast strain which overproduces HT, gave rise to fermented must also higher in 2-PE and their corresponding esters but with an outstanding less presence of other important esters such as ethyl hexanoate and ethyl octanoate. Both premises could point out that S. cerevisiae might have different approaches to handling cell stress/toxicity due to their nitrogen metabolism. One detoxifying pathway could be through the production of higher alcohols and these in turn to esters and the other be more related to synthesizing antioxidant molecules such as MEL and HT. Keywords S. cerevisiae· Fermentation· Tyrosol· Hydroxytyrosol· Melatonin· Volatile compounds Introduction Currently, the industrial employment of yeast to produce a wide range of molecules is booming because they are feasible and effective bioreactors, leading to efficient production performance (Pretorius, 2020). Some of the applications include the production of biodiesel, perfume ingredients, pharmaceuticals, enzymes, pigments, plastic, lubricants, and other bio-based chemicals, etc. (Bettencourt etal., 2020; Diamantopoulou etal., 2020; Franco-Duarte etal., 2017; Huang & Demirci, 2009; Mantzouridou & Paraskevopoulou, 2013; Mata-Gómez etal., 2014; Perpetuini etal., 2020; Vandermies & Fickers, 2019; Zhang etal., 2017). The main primary metabolite from the alcoholic fermentation of a sugar substrate with Saccharomyces cerevisiae is ethanol; however, the molecules derived from the secondary metabolism of the yeast, specifically from nitrogen metabolisms such as aroma and bioactive compounds are of special interest to the industry (Cordente etal., 2019). Regarding volatile compounds, depending on the yeast employed, the volatile composition may vary in a huge extent, being one of the main factors responsible for the aroma of a wine (Garde-Cerdán & Ancín-Azpilicueta, 2006; Varela etal., 2009). Moreover, the interaction of some yeasts with other types has been described to influence on the volatile compounds production (Kosel etal., 2017). In addition, it has been demonstrated that the volatile compounds produced by the yeast are strongly linked to the amino acids * Cristina Ubeda [email protected] 1 Departamento de Nutrición, Bromatología, Toxicología y Medicina Legal, Facultad de Farmacia, Universidad de Sevilla, C/P. García González no 2, 41012Seville, Spain 2 Departamento de Biotecnología de Alimentos, Instituto de Agroquímica y Tecnología de Alimentos, IATA-CSIC, Agustín Escardino 7, Paterna46980, Valencia, Spain 3 Departamento de Biología Molecular e Ingeniería Bioquímica, Universidad Pablo de Olavide, Ctra. Utrera, km 1, 41013Seville, Spain
Food and Bioprocess Technology 1 3 composition of the substrate and to the amount of yeast available nitrogen (YAN) in the media (Rapp & Versini, 1995; Hernández-Orte etal., 2002, 2005; Garde-Cerdán & Ancín-Azpilicueta, 2008), or even the temperature of fermentation (Morakul etal., 2013) among other factors. Therefore, the elucidation of the clues to modulate yeast aromatic amino acid metabolism is the subject of several research works (Dickinson etal., 2003; Hazelwood etal., 2008). Moreover, a useful system for monitoring fermentative aromas has established a strong relationship between nitrogen sources and the higher alcohols and esters production along winemaking fermentation (Mouret etal., 2014). Apart from these volatile compounds, among the higher alcohols with importance from an organoleptic perspective is tyrosol (TYR), also produced by the yeast, being published evidence of the in-mouth sensory properties related to wine bitterness (Sáenz-Navajas etal., 2012). The origin of higher alcohols by S. cerevisiae derives from α-ketoacids generated either through the anabolic (de novo synthesis from sugar) (Fig.1a) or the catabolic (from amino acids present in the media-via Ehrlich) pathways (Fig.1b) (Mas etal., 2014). Some studies have observed that the addition of the corresponding precursor amino acid may yield the specific higher alcohol in increased concentrations (HernándezOrte etal., 2002, 2005; Garde-Cerdán & Ancín-Azpilicueta, 2008; Bordiga etal., 2016). Conversely, by using isotopically 13C-labeled amino acid precursors (Crépin etal., 2017; Rollero etal., 2017) and glucose (Nisbet etal., 2014), it has been shown that the vast majority of the higher alcohols are formed through the anabolic pathway. On the other hand, S. cerevisiae prefers ammonium and glutamine as nitrogen sources but in conditions of depletion of these nitrogen sources, the yeast can use amino acids through the Ehrlich pathway (Hazelwood etal., 2008) yielding acids, aldehydes, and higher alcohols which subsequently can give rise to esters, mainly with acetate (Cordente etal., 2021). At the same time, it has been suggested that the production of higher alcohols and their corresponding esters could be a result of a detoxifying mechanism used by the yeast to diminish aldehydes and medium-chain fatty acids (MCFAs) (Borrull etal., 2015; Boulton etal., 1995; Saerens etal., 2010). In addition to the synthesis of volatile compounds, other molecules with bioactive potential are generated by the metabolism of S. cerevisiae, among them are melatonin (MEL) and hydroxytyrosol (HT) (Álvarez-Fernández etal., 2019a). MEL has been proposed as being a signaling molecule (Fernandez-Cruz etal., 2019; Morcillo-Parra etal., 2019) and also has been shown to possess remarkable antioxidant, neuroprotective, anti-inflammatory and cardiovascular protection properties in humans (Reiter etal., 2007; Sanchez-Barcelo etal., 2012). The secondary metabolism may also yield HT, which is produced from TYR. Hence, HT may be produced by yeast following the Ehrlich pathway from the tyrosine present in the fermentation media or from glucose (anabolic pathway) (Gallardo-Fernández etal., 2022) being therefore closely related to the synthesis of higher alcohols. Certain health benefits, such as cardioprotection and neuroprotection, have been reported for its precursor TYR (Gris etal., 2011; Samuel etal., 2008), but the positive health effects of HT are much more remarkable (Gallardo-Fernández etal., 2022). The employment of yeast, both as cell factories for the production of valuable volatile and bioactive compounds and as fermentative microorganisms to produce foods with enhanced organoleptic properties as well as a convenient bioactive profile, is feasible and profitable. For this purpose, genetic engineering techniques have been employed for Fig. 1 Shikimate (A) and Ehrlich (B) pathways for the production of tyrosol, hydroxytyrosol, melatonin and 2-phenylethanol. This figure is adapted from Cordente etal. (2019) and Bisquert etal. (2022)
Food and Bioprocess Technology 1 3 example for the sobreexpresion of those genes responsible for the synthesis of HT (Bisquert etal., 2022). However, the potential for the production of these compounds from the secondary metabolism of a very common yeast such as S. cerevisiae has been scarcely explored. Several research addressing the characterization of the volatile compounds produced by different yeast strains have been published (Albanese etal., 2013; Ivanova etal., 2013; Morakul etal., 2013; Mouret etal., 2014); however, these studies do not approach simultaneous production of bioactive compounds and the influence and relationship with aromatic metabolites as the present work analyzes. Very recently, Cordente etal. (2021) have pointed out the relation between 2-PE and the production of TYR in synthetic and natural grape must, showing that those genetically modified yeast strains able to overproduce 2-PE, are also capable to generate increased concentrations of TYR. Therefore, the aims of this study were to evaluate the simultaneous production of volatile compounds and the bioactive compounds melatonin, tyrosol, and hydroxytyrosol of some commonly used S. cerevisiae yeast strains trying to ascertain the relationship between aroma and bioactive composition and also the influence of the initial must composition. At the same time, the production of these compounds by a modified S. cerevisiae HT overproductive yeast strain was tested with the purpose of ascertaining if an increased production of the alcohols TYR and HT has an impact on the aroma composition of the fermented must. Materials andMethods Chemical Standards Standards of tyrosol, hydroxytyrosol, and melatonin were purchased from Sigma Aldrich (St. Louis, MO, USA). HPLC grade methanol was supplied from Merck (Darmstadt, Germany) and formic acid was provided by Prolabo (Obregon, Mexico). 4-Methyl-2-pentanol was used as the internal standard for the gas chromatography determinations and was provided by Merck (Darmstadt Germany). An alkane standard mixture C10–C40 purchased by Fluka (Madrid, Spain) was used for calculating the Linear Retention Index (LRI) for GC–MS analysis. Fermentation Trials All the samples analyzed in this study are samples at the end of the fermentation. The first set of fermentations was performed employing different commercial S. cerevisiae Uvaferm VRB (UVR), Enoferm M2 (EM2), P23 Lallemand (P23), and a yeast from Murviedro winery (MUW). The fermentations were carried out in glass bottles and they took place as described in Table1. Each strain was inoculated from a culture grown overnight in YPD in their stationary phase. Fermentations were performed in triplicate. To control the development of the fermentations, 1.5 mL of sample was extracted at 24 h, 48 h and 120 h to measure the density using a Densito 30PX densimeter and the OD600nm with a UVmini-12 spectrophotometer. At the end of the fermentation, the amount of residual sugars and the percentage of ethanol were measured (Pérezet al., 2021). A total of 12 samples (4 yeast × 3 biological replicates) were centrifuged 5 min at 4000 rpm to separate the cells, and the supernatant was stored at −20 °C prior to the analysis. The second trial of fermentations employing a commercial wine yeast strain of S. cerevisiae Lalvin YSEO QA23 (Lallemand) and its genetically modified yeast was performed. The genetic modifications carried out on QA23 were multiple integration of HpaBC complex under the control of strong constitutive promoters TEF1p and PGK1p into the genome using Ty1Cons2 sequences as homologous recombination targets, and the single integration of allelic variant ARO4K229L under the control of GPD promoter in chromosome X-3. Such modifications were performed according to previous works (Bisquert etal., 2022; MuñizCalvo etal., 2020). Briefly, genes hpaB and hpaC and bidirectional promoter TEF1-PGK1 were PCR-amplified from plasmids p426GPD-hpaB, p425GPD-hpaC and pCfB2628 respectively (Germann etal., 2016), while ARO4K229L with GPD promoter was amplified from plasmid p423GPDARO4*. In parallel, vectors bearing the Ty1Cons2 and X-3 sequence from the EasyCloneMulti and EasyClone vector set pCfB2988 and pCfB257 (Jensen etal., 2014; Maury etal., 2016), were prepared by sequential treatment with enzymes AsiSI (SfaAI) (Thermo Fisher Scientific, Waltham, MA, USA) and BsmI (New England Biolabs, Ipswich, MA, USA). After purification, PCR products were cloned into pre-treated vectors by USERTM method (New England Biolabs). The ligation product was transformed into E. coli and successful cloning of both vectors was verified by Sanger sequencing (EUROFINS genomics, Ebersberg, Germany). Table 1 Conditions of the two different fermentation trials YAN yeast assimilable nitrogen, SM synthetic must Non-modified/commercial strains trial Modified QA23 strain trial Temperature 28 25 Agitation 150 rpm Volume 80 mL 750 mL YAN 300 mg/L 200 mg/L Cells/mL 2 × 106 cells/mL 106 cells/mL SM employed Riou etal. (1997)
Food and Bioprocess Technology 1 3 Prior to yeast transformation, the resulting integrative vectors pCfB2988, HpaBC and pCfB257 were linearized by FastDigest NotI (Thermo scientific, Vilnius, Lithuania) and the fragment containing the desired sequences to integrate were purified from agarose gel. Yeast cells were transformed with 1–1.5 µg of the linear fragment from the integrative vectors by the PEG/LiAc method according to Gietz (2014) and selected on selective agar medium according to strain auxotrophic markers. The fermentations were also carried out following Riou etal. (1997) specifications for synthetic must with some modifications as described: 10 L of SM was prepared for experiment with slight differences following RebolloRomero etal. (2020). Sugars: fructose (100 g/L) and glucose (100 g/L); NH4Cl (0.46 g/L); acids: malic acid (5 g/L), citric acid (0.5 g/L) and tartaric acid (3 g/L); the minerals added were: K2SO4 (0.5 g/L), KH2PO4 (0.75 g/L), MgSO4 7H2O (0.25 g/L), CaCl2 (0.155 g/L) and NaCl (0.2 g/L). Also it was added to the SM 1 mL of trace elements was added including 13.09 mL of an amino acids solution composed by isoleucine (2.5 g/L), tyrosine (1.5 g/L), tryptophan (13.4 g/L), threonine (5.8 g/L), aspartic acid (3.4 g/L), glutamic acid (9.2 g/L), leucine (3.7 g/L), glycine (1.4 g/L), histidine (2.6 g/L), glutamine (38.4 g/L), alanine (11.2 g/L), valine (3.4 g/L), methionine (2.4 g/L), cysteine (1.6 g/L), phenylalanine (2.9 g/L), arginine (28.3 g/L), serine (6 g/L), lysine (1.3 g/L), and proline (46.1 g/L). Finally to complete this SM 10 mL of a vitamins solution containing myoinositol (2 g/L), thiamine hydrochloride (0.025 g/L), calcium pantothenate (0.15 g/L), pyridoxine (0.025 g/L), nicotinic acid (0.2 g/L) and biotin (3 mL). The pH was adjusted to 3.31 with NaOH. The final YAN was 210 mg/L. Six replicate fermentation experiments were used for each strain with the fermentation conditions showed in Table1. The flasks were weighed daily before and after sampling, in order to monitor the fermentation. The optical density was also measured daily by (Cytoflex S, Beckman Coulter, California, EEUU). The samples of final fermented musts resulting from the fermentations were stored at −80 °C, before the analysis in UHPLC-HRMS and GC–MS. Tyrosol, Hydroxytyrosol, andMelatonin Extraction Before the analysis, samples were cleaned up using SPE C18 cartridges (Variant, Agilent). The first step was the conditioning of the cartridge using 2 mL of methanol and sequentially 2 mL of Milli-Q water. Once the cartridge is conditioned, 2 mL of the sample was passed through the cartridge. Then 2 mL of a 10% v/v methanol/water solution was used to wash it. The compounds of interest were eluted with 1 mL of methanol. A vacuum concentrator (HyperVAC-LITE, Gyrozen, Korea) was used at 2000 rpm at 30 °C for 8 h, to dry samples as previously described (Álvarez-Fernández etal., 2019b). Once the samples were dried, they were reconstituted with 200 μL of 10% v/v acetonitrile/water in the case of hydroxytyrosol and tyrosol and 10% v/v methanol/water with 0.1% formic acid for melatonin, and they were stored at −80 °C until analysis. UHPLC‑HRMS Analyses A Thermo Scientific Liquid Chromatography system consisting of a binary UHPLC Dionex Ultimate 3000 RS connected to a quadrupole-orbitrap Qexactive hybrid mass spectrometer (ThermoFisher Scientific, USA) with HESI ionization probe (HESI-II) was used for the determination of the bioactive compounds tyrosol, hydroxytyrosol and melatonin. A Zorbax SB-C18 (2.1 × 100 mm, 1.8 µm particle size) column (Agilent) with a flow of 0.4 mL/min for hydroxytyrosol and tyrosol and 0.5 mL/min for melatonin. The chromatographic conditions for melatonin consisted of two mobile phases, water (A) and methanol (B), both with 0.1% formic acid with a gradient elution programmed as follows: 95% A, 5% B (0–2 min); 0% A, 100% B (2–13 min); and 95% A, 5% B (13.1–15 min). The flow selected was 0.5 mL min−1. The gradient for hydroxytyrosol and tyrosol consists of (A) water with 0.2% of acetic acid and (B) acetonitrile. The binary gradient was used with the following profile: 0–1 min 5% B, 1–7 min from 5 to 100% B, 7–8.5 min 100% B, and 8.5–10 min 5% B. 5 μL was the volume elected for the injection. The compounds were dissolved in 10% v/v acetonitrile/water. A method of parallel reaction monitoring (PRM) was used in a negative mode with a resolution of 35,000 at m/z 200 FWHM and an isolation window of 1 m/z and the normalized collision energy was set at 40 eV. The masses were optimized as follows: tyrosol (137.06080) and hydroxytyrosol (153.05572). HESI source parameters were spray voltage, 3.0 kV; S lens level, 50; capillary temperature, 320 °C; sheath, auxiliary, and sweep gas flow, 50, 15, and 2 respectively (arbitrary units); and probe heater temperature, 425 °C. For melatonin, the positive mode was used. The following parameters were optimized to carry out the analysis: HESI source parameters were as follows: source voltage 3.5 kV; tube lens voltage 50 V; capillary temperature 230 °C; source heater temperature 440 °C; sheath, auxiliary and sweep gas flow rate (N2) 53, 14 and 3. The masses were optimized as follows for melatonin (233.12845). The data were treated with the TraceFinder 5.1 software. SPME/GC/MS Analyses Volatile compounds’ extraction was performed using Headspace Solid Phase Microextraction (HS-SPME), employing
Food and Bioprocess Technology 1 3 a triple fiber of 1 cm DVB (divinylbenzene)/C-WR (carbon wide range)/PDMS (polydimethylsiloxane) (Agilent Technologies, Switzerland). For this purpose, 4 mL of each sample was transferred into 20 mL glass vials with 0.8 g of sodium chloride and 10 µL of 4-methyl-2-pentanol (0.75 mg/L) (used as an internal standard), which were then placed in the autosampler. For the static headspace extraction, incubation lasted 40 min at 45 °C and 250 rpm agitation speed, and the fiber was then exposed to the headspace for 40 min, with a penetration into the vial of 22 mm. Once the adsorption finished, the fiber was desorbed for 180 s in the injector using the splitless mode. For the analyses of the samples, a Bruker 450 Gas Chromatograph was employed coupled to a Mass Spectrometer Bruker 300-MS. For the chomatographic analysis, the conditions followed are described in Ubeda etal. (2019). For identification purposes, linear retention indices (LRIs) were calculated after the injection of C10-C40 alkanes solution by applying the same conditions of sample analysis. The identification was made by matching the LRIs of each compound from the standards NIST library (2.0 version) Table 2 Volatile compounds determined after alcoholic fermentation of Uvaferm® VRB, Enoferm® M2, P23 Lallemand and Murviedro winery yeast of the synthetic must Values are expressed in relative areas. Values with different superscript letters indicate statistically significant differences (p < 0.05) LSDFisher test LRI linear retention index, Qion major ion employed for quantitation, ID reliability of identification: A, mass spectrum agreed with NIST mass spectral database and LRI agreed with the literature data (Pherobase: www. phero base. com; NIST Mass Spectrometry Data Center: https:// webbo ok. nist. gov/; Pubchem: https:// pubch em. ncbi. nlm. nih. gov/); B, mass spectrum agreed with NIST mass spectral database Compound LRI Qion ID Uvaferm® VRB Enoferm® M2 P23 Lallemand Murviedro winery Esters Ethyl acetate 890 43 A 70.843 ± 14.826a96.937 ± 25.443ab 120.828 ± 35.555b84.381 ± 16.648ab Isoamyl acetate 1100 43 A 3.706 ± 0.439a10.067 ± 1.305ab 13.324 ± 5.763b27.525 ± 7.412c Ethyl octanoate 1433 88 A 17.909 ± 2.494b6.947 ± 4.656a18.939 ± 3.939b18.298 ± 9.077b Ethyl nonanoate 1535 88 A 0.112 ± 0.019 0.073 ± 0.025 0.115 ± 0.046 0.139 ± 0.102 Ethyl decanoate 1638 88 A 13.151 ± 5.605a12.968 ± 3.623a14.931 ± 4.186a24.817 ± 5.844b Gamma-butyrolactone 1667 42 A 0.112 ± 0.023a0.562 ± 0.109b0.815 ± 0.279b0.859 ± 0.221b Ethy-9-decenoate 1687 55 A 0.559 ± 0.117b0.258 ± 0.202a0.606 ± 0.154b0.763 ± 0.048b 2-Phenylethyl acetate 1831 104 A 4.211 ± 1.253a13.716 ± 0.694bc 12.687 ± 1.449b15.413 ± 1.526c 2,2-Dimethyl-1-(2-hydroxy1-methylethyl)propyl 2Methylpropanoate 1884 71 A 1.057 ± 0.479 1.203 ± 0.101 1.679 ± 0.526 1.454 ± 0.129 Ethyl 3-hydroxytridecanoate 1903 117 A 0.051 ± 0.020a0.118 ± 0.014b0.191 ± 0.024c0.082 ± 0.004a Octyl octanoate 2018 55 A 0.036 ± 0.015 0.055 ± 0.004 0.062 ± 0.030 0.061 ± 0.011 Alcohols Isobutanol 1071 43 A 6.794 ± 2.672a9.513 ± 3.247a22.399 ± 4.524b18.177 ± 1.039b 3-Methyl-1-butanol 1247 55 A 76.103 ± 11.585a157.988 ± 23.123b141.778 ± 15.416b170.228 ± 30.359b 2-Nonanol 1520 45 A 0.324 ± 0.176a0.460 ± 0.104a0.488 ± 0.053a1.121 ± 0.377b 2,3-Butanediol 1568 45 A 18.966 ± 6.935a16.479 ± 7.082a37.934 ± 11.796b8.133 ± 1.591a Methionol 1743 106 A 0.082 ± 0.035a0.194 ± 0.031ab 0.321 ± 0.105c0.235 ± 0.067bc Decanol 1776 70 A 0.187 ± 0.072ab 0.129 ± 0.035a0.263 ± 0.026ab 0.324 ± 0.171b 2-Phenylethanol 1935 91 A 43.676 ± 8.136a143.284 ± 15.285b129.773 ± 18.784b118.421 ± 14.324b Dodecanol 1983 55 A 0.849 ± 0.220ab 0.764 ± 0.238a1.306 ± 0.226b1.315 ± 0.374b Acids Acetic acid 1458 43 A 49.808 ± 26.266a50.581 ± 7.305a82.482 ± 15.164b69.293 ± 3.815ab 2-Methyl propanoic acid 1589 43 A 0.514 ± 0.190a0.923 ± 0.139b0.523 ± 0.233a0.705 ± 0.100ab 4-Methyl pentanoic acid 1681 57 B 0.119 ± 0.039a0.435 ± 0.059b0.201 ± 0.064a0.403 ± 0.101b Hexanoic acid 1862 60 A 1.863 ± 0.226a4.442 ± 0.479c3.024 ± 0.301b3.762 ± 0.885bc Octanoic acid 2063 60 A 7.463 ± 1.514ab 6.162 ± 0.118a11.267 ± 0.973b10.020 ± 4.223ab Decanoic acid 2228 60 A 3.675 ± 1.183ab 2.863 ± 0.738a4.364 ± 0.851ab 5.398 ± 1.858b Aldehydes 2,4-Decadienal 1826 81 A 0.013 ± 0.002a0.015 ± 0.004ab 0.020 ± 0.001b0.019 ± 0.004ab 2,5-Dimethylbenzaldehyde 1837 134 B 0.095 ± 0.018a0.097 ± 0.022ab 0.153 ± 0.027b0.154 ± 0.047b
Food and Bioprocess Technology 1 3 Fig. 2 Total amounts of esters, alcohols, acids and aldehydes present in the fermented must produced with every Uvaferm® VRB, Enoferm® M2, P23 Lallemand and Murviedro winery yeast. Bars with different superscript letters indicate statistically significant differences (p < 0.05) by Fisher Least Significant Difference (LSD) among the samples
Food and Bioprocess Technology 1 3 found in the literature (Pherobase: www. phero base. com; NIST Mass Spectrometry Data Center: (LRI Odour database: www. odour. org. uk; accessed on March 2022). The data shown in this work were expressed as the relative area with respect to 4-methyl-2-pentanol (internal standard). The relative areas were calculated by dividing the peak area of the target ion of each compound by the peak area of the target ion of the internal standard. Statistical Analysis Data obtained were compared using ANOVA and Fisher Least Significant Difference (LSD) Method (p < 0.05) employing the InfoStat software (version 2017p, FCAUniversidad Nacional de Córdoba, Argentina). Principal component analysis (PCA) was performed using IBM SPSS Statistics 26 software (IBM, Barcelona, Spain) and Partial Fig. 3 Heatmap visualization based on the 27 volatile compounds (variables) in the fermented must produced with every Uvaferm® VRB, Enoferm® M2, P23 Lallemand and Murviedro winery yeast
Food and Bioprocess Technology 1 3 least squares-discriminant analysis (PLS-DA) with the 5.0 version of Metaboanalyst software (Quebec, Canada). Results andDiscussion Volatile Compounds, Tyrosol, Hydroxytyrosol, andMelatonin Production byYeast Samples obtained at the end of the alcoholic fermentations performed with the yeast strains UVR, EM2, P23 and MUW were analyzed for aroma composition. A total of 27 volatile compounds were determined, 11 esters, 8 alcohols, 6 acids, and 2 aldehydes (Table2). Figure2 shows tendencies related to the total sum of the relative areas corresponding to each chemical group. Strains EM2, P23 and MUW produced significantly higher amounts of alcohols. Acids and aldehydes followed a similar pattern, with UVR and EM2 reaching lower quantities at the end of fermentation vs P23 and MUW. As shown in Table2, UVR presented in general the lowest quantities of higher alcohols, especially regarding isobutanol, 3-methyl-1-butanol, and 2-PE compared to the other yeast assayed. This is in agreement with the results from Peris etal. (2016) who employed Uvaferm VRB among other yeast strains to ferment a Macabeo grape must showing a low production of higher alcohols in comparison to the quantities produced by other yeast. Our results showed that esters (ethyl and acetate) were in fact present in significantly higher quantities in P23 and MUW than in UVR trials at the end of the fermentation (Fig.2). While the production of ethyl esters during fermentation occurs via the enzymatic esterification reaction of ethanol and the carboxylic acids present in the media (Lambrechts & Pretorius, 2000), acetate esters are formed by enzymatic acetylation of alcohols, this last being mainly byproducts of the amino acid biosynthesis such as 3-methyl1-butanol or 2-PE (Sumby etal., 2010). Although samples EM2, MUW, and P23 reached higher amounts of ethyl acetate at the end of the fermentation as compared to UVR, with P23 reflecting significance (Table2). Apart from this predominant ethyl ester, the acetate esters, isoamyl acetate and 2-phenylethyl acetate, stood out among all the ester family. Interestingly, they were present in the sample at levels at least three times lower (Table2). The correlation between the formation of acetate esters and their corresponding higher alcohol has been described in wines (Cordente etal., 2012) and as can be observed, those fermented musts with a higher quantity of higher alcohols, also presented higher amounts of acetate esters. Regarding acids and aldehydes, UVR and EM2 showed similar abundance, the same happened for P23 and MUW (Fig.2). A heatmap was built with results on aroma composition and bioactive compounds (Fig.3), thus allowing a global insight of data. As can be observed, there is an inverse correlation between HT and MEL and the volatile compounds as a whole. Furthermore, it was observed that TYR concentrations from the strains EM2 and MUW were higher as compared to P23 and UVR (Table3). UVR resulted in being the lowest producer of tyrosol but the highest producer of HT, probably having a more efficient ability to hydroxylate TYR to HT. Multivariate analysis by Principal Component Analysis (PCA) was performed employing all the secondary metabolites considered (volatile compounds, TYR, HT, and MEL). Hence, six principal components (PCs) were extracted explaining 93.3% of the total variance. Figure4a shows the distribution of the samples (scores) in the plot of PC1 (Component 1) and PC2 (Component 2) accounting for 58.5% of the cumulative variance. The corresponding loadings distribution (Fig.4b) clearly showed that the strain UVR gave rise to fermented musts with a lower content of volatile compounds but higher content of MEL and HT. On the other hand, samples EM2, P23 and MUW were richer in volatile compounds but their concentrations in HT and MEL were lower than those found in UVR. As mentioned above, TYR concentrations were higher in EM2 samples (Table3); therefore, it is located in the plot closer to the fermented musts. Additionally, a Partial Least-Squares Discriminant Analysis (PLS-DA) was performed to bring out the variables that are more useful to classify the samples thus having discriminant potential. Variable importance in the projection (VIP) score plot shows the major metabolite features Table 3 Tyrosol, hydroxytyrosol and melatonin determined after alcoholic fermentation of the synthetic must by Uvaferm® VRB, Enoferm® M2, P23 Lallemand, Murviedro winery yeast and original Lalvin QA23 yeast and Lalvin QA23 modified yeast Different superscript letters indicate statistically significant differences (p < 0.05) by LSD test among the samples of non-modified strains trial and the asterisk indicates the statistically significant difference between the original QA23 and modified yeast strain trial Non-modified/commercial strains trial Modified QA23 strain trial Uvaferm® VRB Enoferm® M2 P23 Lallemand Murviedro winery Lalvin QA23™Lalvin QA23 modified Tyrosol 0.0667 ± 0.0261c0.1579 ± 0.0304ab 0.0748 ± 0.0096a0.1269 ± 0.0187bc 5.3641 ± 0.6722 37.3478 ± 3.9013* Hydroxytyrosol 0.0065 ± 0.0022b0.0026 ± 0.0006a0.0023 ± 0.0003a0.0028 ± 0.0009a0.0005 ± 0.0001 0.8793 ± 0.1315* Melatonin 0.0758 ± 0.0111 0.0598 ± 0.0067 0.0533 ± 0.0017 0.0715 ± 0.0026 - -
Food and Bioprocess Technology 1 3 (Fig.5). Among the secondary metabolites analyzed, hexanoic acid was found the best one to classify the samples. This medium-chain fatty acid (MCFA) is produced by the yeast during alcoholic fermentation and depends on several factors such as yeast strain and temperature of fermentation (Torija etal., 2003; Tronchoni etal., 2012). In general, the overpresence of MCFAs can inhibit the growth of S. cerevisiae (Baroň etal., 2017). Specifically, several works have reported the strong relation of hexanoic acid with nitrogen amount in the media both in synthetic must and wine, and also a Fig. 4 Principal Component Analysis (PCA) showing the data scores (a) and loading (b) biplot on the plane of the first two principal components (PC1 against PC2) including the 27 volatile compounds, tyrosol, hydroxytyrosol, and melatonin present in Uvaferm® VRB, Enoferm® M2, P23 Lallemand and Murviedro winery yeast