2-phenylethyl Acetate Production Research Articles

Feasibility of reactive chromatography for the production of 2‐phenyl ethyl acetate

AbstractReactive chromatography is a novel process intensification option when the progress of a reaction is hampered by reversibility (e.g., esterification and acetalization). In this work, we study its feasibility for the production of 2‐phenyl ethyl acetate (PEAct) by esterification of 2‐phenyl ethyl alcohol with acetic acid using Amberlyst‐15 as a catalyst/adsorbent. The reaction kinetics is investigated in a laboratory batch reactor by varying various parameters such as agitation speed, temperature, feed molar ratio, catalyst loading, and particle size, and a Langmuir Hinshelwood kinetic model is proposed. The reaction is then studied in a fixed‐bed chromatographic reactor (FBCR). Non‐reactive binary adsorption experiments are performed in the same setup to estimate the corresponding parameters of the Langmuir adsorption isotherm. The experimentally observed reactive breakthrough curves in FBCR reveal that RC is a promising process option for the production of PEAct. Furthermore, it is shown that the FBCR model, which uses kinetics and isotherms developed in this work, explains the reactive breakthrough curves and the regeneration performance reasonably well. The work reported here forms a base for the design of a simulated moving‐bed reactor that may be used for large‐scale production.

Comparative impact of exogenous phenylalanine on oenological isolates ofKluyveromyces marxianusandSaccharomyces cerevisiae

Kluyveromyces marxianus' high production of 2-phenylethyl acetate (2-PEA) via L-phenylalanine (Phe) catabolism makes it relevant for industries relying on the production of aroma compounds through fermentation processes. This study assessed the physiological impact of exogenous supplementation of Phe on cell viability, fermentation performance, and, by extension, on lipid and amino acid metabolism in a wine isolate of this yeast. The data showed that Phe exerted cytotoxic effects on K. marxianus IWBT Y885, which were minimal on Saccharomyces cerevisiae and impacted amino acid metabolism and aroma production. We demonstrated that K. marxianus strains fermented sugars more effectively in the absence of Phe. While lipid supplementation did not mitigate any deleterious effects of Phe, it supported viability maintenance and fermentation performance in the absence of Phe. Phe supplementation succeeded in augmenting the production of 2-PE and 2-PEA. The enhanced production of 2-PEA in K. marxianus suggests that this transesterification may be, at least in part, a compensatory detoxification mechanism for this yeast.

Continuous Production of 2-Phenylethyl Acetate in a Solvent-Free System Using a Packed-Bed Reactor with Novozym® 435

2-Phenylethyl acetate (2-PEAc), a highly valued natural volatile ester, with a rose-like odor, is widely added in cosmetics, soaps, foods, and drinks to strengthen scent or flavour. Nowadays, 2-PEAc are commonly produced by chemical synthesis or extraction. Alternatively, biocatalysis is a potential method to replace chemical synthesis or extraction for the production of natural flavour. Continuous synthesis of 2-PEAc in a solvent-free system using a packed bed bioreactor through immobilized lipase-catalyzed transesterification of ethyl acetate (EA) with 2-phenethyl alcohol was studied. A Box–Behnken experimental design with three-level-three-factor, including 2-phenethyl alcohol (2-PE) concentration (100–500 mM), flow rate (1–5 mL min−1) and reaction temperature (45–65 °C), was selected to investigate their influence on the molar conversion of 2-PEAc. Then, response surface methodology and ridge max analysis were used to discuss in detail the optimal reaction conditions for the synthesis of 2-PEAc. The results indicated both 2-PE concentration and flow rate are significant factors in the molar conversion of 2-PEAc. Based on the ridge max analysis, the maximum molar conversion was 99.01 ± 0.09% under optimal conditions at a 2-PE concentration of 62.07 mM, a flow rate of 2.75 mL min−1, and a temperature of 54.03 °C, respectively. The continuous packed bed bioreactor showed good stability for 2-PEAc production, enabling operation for at least 72 h without a significant decrease of conversion.

Production of 2-phenylethyl acetate via reactive distillation

An alternative approach to 2-phenylethyl acetate production, reactive distillation process for 2-phenylethyl acetate production from 2-phenylethanol in the presence of an inert component, n-pentane, via esterification by acetic acid is presented. The main objectives of this work were shifting of the chemical equilibrium in favour of the desired product and achieving the required product purity. In the first step, graphical mapping methods were employed to evaluate reactive distillation applicability for 2-phenylethanol esterification. To describe the system phase equilibria, thermodynamic model NRTL-HOC was used. Process feasibility was evaluated using a boiling point analysis and residue curves maps, and the process operating window was estimated. Results show that the reactive distillation concept can be used for 2-phenylethyl acetate production as suitable product compositions without serious process limitations were predicted. Total equilibrium model (phase and chemical equilibria) was used for reactive distillation column calculations performed by the Aspen Plus software. Reactive distillation column parameters were calculated and optimised according to the design criteria. Finally, optimised reactive distillation column parameters were used for temperature and concentration profile evaluation. These results form a promising base for further steps in the design of 2-phenylethyl acetate production via reactive distillation.

2-Phenylethanol and 2-phenylethylacetate production by nonconventional yeasts using tequila vinasses as a substrate

Vinasses from the tequila industry are wastewaters with highly elevated organic loads. Therefore, to obtain value-added products by yeast fermentations, such as 2-phenylethanol (2-PE) and 2-phenylethylacetate (2-PEA), could be interesting for industrial applications from tequila vinasses. In this study, four yeasts species (Wickerhamomyces anomalus, Candida glabrata, Candida utilis, and Candida parapsilosis) were evaluated with two different chemically defined media and tequila vinasses. Differences in the aroma compounds production were observed depending on the medium and yeast species used. In tequila vinasses, the highest concentration (65 mg/L) of 2-PEA was reached by C. glabrata, the inhibitory compounds decreased biomass production and synthesis of 2-PEA, and biochemical and chemical oxygen demands were reduced by more than 50 %. Tequila vinasses were suitable for the production of 2-phenylethylacetate by the shikimate pathway. A metabolic network was developed to obtain a guideline to improve 2-PE and 2-PEA production using flux balance analysis (FBA).

Synergistic effect enhances 2-phenylethyl acetate production in the mixed fermentation of Hanseniaspora vineae and Saccharomyces cerevisiae

2-Phenylethyl acetate (2-PEA) is a desired aroma compound in wine due to its honey- and flowery-like characteristics. The effects of adding l-phenylalanine (Phe) during 2-PEA production were investigated in the co-fermentation of Hanseniaspora vineae (HV6) and Saccharomyces cerevisiae BDX. BDX and HV6 strains overproduced 2-phenylethyl alcohol (2-PE) and 2-PEA, respectively. The co-fermentation of BDX and HV6 achieved a 14.9 fold increase in 2-PEA odour activity value (OAV) but a 42.0 % reduction of 2-PE OAV compared to BDX fermentation; the 2-PEA concentration was significantly higher than the sum of BDX and HV6 pure fermentations. This suggests that BDX and HV6 have synergistic effects on 2-PEA formation in mixed culture. Adding 151.6 mg/L Phe enhanced the OAV of 2-PEA by 52.8 % compared to the control. The combination of Phe addition with the co-fermentation of S. cerevisiae and H. vineae is a potential way to increase 2-PEA production and improve wine aromatic quality.

Potential production of 2-phenylethanol and 2-phenylethylacetate by non-Saccharomyces yeasts from Agave durangensis

The participation of non-Saccharomyces yeasts in fermentation processes is of great importance due to their participation in the formation of esters and superior alcohols, which confer characteristic aromas to beverages such as wine and mescal. The aim of this study was identify and evaluate the potential aroma production of yeast native of Agave fermentation by the mescal production in Durango, Mexico. Isolated yeasts were molecularly identified by 5.8s ribosomal gene; the potential production of aromas was carried out in fermentations with the addition of l-phenylalanine and evaluated after 24 h of fermentation. Extraction and quantification of aromatic compounds by headspace solid-phase micro-extraction (HS-SPME) and gas chromatograph mass spectrometry (GC-MS). The isolated non-Saccharomyces yeasts could be classified into six different genera Saccharomyces cerevisiae, Clavispora lusitaniae, Torulaspora delbrueckii, Kluyveromyces dobzhanskii, Kluyveromyces marxianus, and Kluyveromyces sp. All probed strains presented a potential aroma production (ethyl acetate, isoamyl acetate, isoamyl alcohol, benzaldehyde, 2-phenylethyl butyrate, and phenylethyl propionate), particularly 2-phenylethanol and 2-phenylethylacetate; the levels found in the Kluyveromyces marxianus ITD0211 yeast have the highest 2-phenylethylacetate production at 203 mg/L and Kluyveromyces marxianus ITD0090 with a production of 2-phenylethanol at 1024 mg/L. Non-Saccharomyces yeasts were isolated from the mescal fermentation in Durango; the Kluyveromyces genus is the most predominant. For the production of aromas, highlighting two strains of Kluyveromyces marxianus produces competitive quantities of compounds of great biotechnological interest such as 2-phenylethanol and 2-phenylethylacetate, without resorting to the genetic modification of yeasts or the optimization of the culture medium.

Bioprocesses for 2-phenylethanol and 2-phenylethyl acetate production: current state and perspectives.

2-Phenylethanol (2-PE) and 2-phenethyl acetate (2-PEA) are valuable generally recognized as safe flavoring agents widely used in industry. Perfumes, pharmaceuticals, polishes, and personal care products, are some of the final products using these compounds as additives due to their rose-like odor. Also, 2-PE is used in disinfectants, pest control, and cleaning products due to its biocide capability. Although most of these additives production are derived from chemical synthesis, the current trend of consumers to prefer natural products has contributed to the development of biotechnological approaches as an alternative way to obtain natural 2-PE and 2-PEA. The most efficient route to bioproduce these compounds is through the bioconversion of L-phenylalanine via the Ehrlich pathway, and most of the advances have been focused on the development of this process. This review compiles the most recent developments in the biotechnological production of 2-PE and 2-PEA, indicating the most studied strains producing 2-PE and 2-PEA, the current advances in the in situ product recovery in liquid systems, an overview of the strain developments, and the progress in the use of residue-based systems. Future research should address the need for more sustainable and economic systems such as those using wastes as raw materials, as well as the scale-up of the proposed technologies.

Metabolic engineering of Escherichia coli for production of 2-Phenylethylacetate from L-phenylalanine.

In order to meet the need of consumer preferences for natural flavor compounds, microbial synthesis method has become a very attractive alternative to the chemical production. The 2‐phenylethanol (2‐PE) and its ester 2‐phenylethylacetate (2‐PEAc) are two extremely important flavor compounds with a rose‐like odor. In recent years, Escherichia coli and yeast have been metabolically engineered to produce 2‐PE. However, a metabolic engineering approach for 2‐PEAc production is rare. Here, we designed and expressed a 2‐PEAc biosynthetic pathway in E. coli. This pathway comprised four steps: aminotransferase (ARO8) for transamination of L‐phenylalanine to phenylpyruvate, 2‐keto acid decarboxylase KDC for the decarboxylation of the phenylpyruvate to phenylacetaldehyde, aldehyde reductase YjgB for the reduction of phenylacetaldehyde to 2‐PE, alcohol acetyltransferase ATF1 for the esterification of 2‐PE to 2‐PEAc. Using the engineered E. coli strain for shake flasks cultivation with 1 g/L L‐phenylalanine, we achieved co‐production of 268 mg/L 2‐PEAc and 277 mg/L 2‐PE. Our results suggest that approximately 65% of L‐phenylalanine was utilized toward 2‐PEAc and 2‐PE biosynthesis and thus demonstrate potential industrial applicability of this microbial platform.

Differences in Enzymatic Properties of the Saccharomyces kudriavzevii and Saccharomyces uvarum Alcohol Acetyltransferases and Their Impact on Aroma-Active Compounds Production.

Higher alcohols and acetate esters belong to the most important yeast secondary metabolites that significantly contribute to the overall flavor and aroma profile of fermented products. In Saccharomyces cerevisiae, esterification of higher alcohols is catalyzed mainly by the alcohol acetyltransferases encoded by genes ATF1 and ATF2. Previous investigation has shown other Saccharomyces species, e.g., S. kudriavzevii and S. uvarum, to vary in aroma-active higher alcohols and acetate esters formation when compared to S. cerevisiae. Here, we aimed to analyze the enzymes encoded by the ATF1 and ATF2 genes from S. kudriavzevii (SkATF1, SkATF2) and S. uvarum (SuATF1, SuATF2). The heterologous expression of the individual ATF1 and ATF2 genes in a host S. cerevisiae resulted in the enhanced production of several higher alcohols and acetate esters. Particularly, an increase of 2-phenylethyl acetate production by the strains that harbored ATF1 and ATF2 genes from S. kudriavzevii and S. uvarum was observed. When grown with individual amino acids as the nitrogen source, the strain that harbored SkATF1 showed particularly high 2-phenylethyl acetate production and the strains with introduced SkATF2 or SuATF2 revealed increased production of isobutyl acetate, isoamyl acetate, and 2-phenylethyl acetate compared to the reference strains with endogenous ATF genes. The alcohol acetyltransferase activities of the individual Atf1 and Atf2 enzymes measured in the cell extracts of the S. cerevisiae atf1 atf2 iah1 triple-null strain were detected for all the measured substrates. This indicated that S. kudriavzevii and S. uvarum Atf enzymes had broad range substrate specificity as S. cerevisiae Atf enzymes. Individual Atf1 enzymes exhibited markedly different kinetic properties since SkAtf1p showed c. twofold higher and SuAtf1p c. threefold higher Km for isoamyl alcohol than ScAtf1p. Together these results indicated that the differences found among the three Saccharomyces species during the aroma-active acetate ester formation may be due, to some extent, to the distinct properties of Atf enzymes.

Effect of yeast assimilable nitrogen on the synthesis of phenolic aroma compounds by Hanseniaspora vineae strains.

In several grape varieties, the dominating aryl alkyl alcohols found are the volatile group of phenylpropanoid-related compounds, such as glycosylated benzyl and 2-phenylethyl alcohol, which contribute to wine with floral and fruity aromas after being hydrolysed during fermentation. Saccharomyces cerevisiae is largely recognized as the main agent in grape must fermentation, but yeast strains belonging to other genera, including Hanseniaspora, are known to predominate during the first stages of alcoholic fermentation. Although non-Saccharomyces yeast strains have a well-recognized genetic diversity, understanding of their impact on wine flavour richness is still emerging. In this study, 11 Hansenisapora vineae strains were used to ferment a chemically defined simil-grape fermentation medium, resembling the nutrient composition of grape juice but devoid of grape-derived secondary metabolites. GC-MS analysis was performed to determine volatile compounds in the produced wines. Our results showed that benzyl alcohol, benzyl acetate and 2-phenylethyl acetate are significantly synthesized by H. vineae strains. Levels of these compounds found in fermentations with 11 H. vineae different strains were one or two orders of magnitude higher than those measured in fermentations with a known S. cerevisiae wine strain. The implications for winemaking in response to the negative correlation of benzyl alcohol, benzyl acetate and 2-phenylethyl acetate production with yeast assimilable nitrogen concentrations are discussed. Copyright © 2016 John Wiley & Sons, Ltd.

Influence of carbon and nitrogen source on production of volatile fragrance and flavour metabolites by the yeast Kluyveromyces marxianus.

The yeast Kluyveromyces marxianus produces a range of volatile molecules with applications as fragrances or flavours. The purpose of this study was to establish how nutritional conditions influence the production of these metabolites. Four strains were grown on synthetic media, using a variety of carbon and nitrogen sources and volatile metabolites analysed using gas chromatography-mass spectrometry (GC-MS). The nitrogen source had pronounced effects on metabolite production: levels of the fusel alcohols 2-phenylethanol and isoamyl alcohol were highest when yeast extract was the nitrogen source, and ammonium had a strong repressing effect on production of 2-phenylethyl acetate. In contrast, the nitrogen source did not affect production of isoamyl acetate or ethyl acetate, indicating that more than one alcohol acetyl transferase activity is present in K. marxianus. Production of all acetate esters was low when cells were growing on lactose (as opposed to glucose or fructose), with a lower intracellular pool of acetyl CoA being one explanation for this observation. Bioinformatic and phylogenetic analysis of the known yeast alcohol acetyl transferases ATF1 and ATF2 suggests that the ancestral protein Atf2p may not be involved in synthesis of volatile acetate esters in K. marxianus, and raises interesting questions as to what other genes encode this activity in non-Saccharomyces yeasts. Identification of all the genes involved in ester synthesis will be important for development of the K. marxianus platform for flavour and fragrance production.

Monitoring a mixed starter of Hanseniaspora vineae–Saccharomyces cerevisiae in natural must: Impact on 2-phenylethyl acetate production

The effect of simultaneous or sequential inoculation of Hanseniaspora vineae CECT 1471 and Saccharomyces cerevisiae T73 in non-sterile must on 2-phenylethyl acetate production has been examined. In both treatments tested, no significant differences in Saccharomyces yeast growth were found, whereas non-Saccharomyces yeast growth was significantly different during all days of fermentation. Independently of the type of inoculation, S. cerevisiae was the predominant species from day 3 till the end of the fermentation. The dynamics of indigenous and inoculated yeast populations showed H. vineae to be the predominant non-Saccharomyces species at the beginning of fermentation in sequentially inoculated wines, whereas the simultaneous inoculation of S. cerevisiae did not permit any non-Saccharomyces species to become predominant. Differences found in non-Saccharomyces yeast growth in both fermentations influenced the analytical profiles of final wines and specifically 2-phenylethyl acetate concentration which was two-fold increased in sequentially inoculated wines in comparison to those co-inoculated. In conclusion we have shown that H. vineae inoculated as part of a sequential mixed starter is able to compete with native yeasts present in non-sterile must and modify the wine aroma profile.