Abstract
The aromatic compounds 2-phenylethanol (2-PE) and 2-phenylethyl acetate (2-PEA) are of high industrial relevance due to their distinctive sensory properties and extensive use in food, fragrance, and wine industries. However, their natural production is costly, motivating interest in sustainable microbial alternatives. This study examined the metabolic regulation of Kluyveromyces marxianus ITD0090, a non-conventional yeast, under nitrogen-limited conditions for enhanced 2-PE and 2-PEA production. Combined genomic and transcriptomic analyses revealed key regulatory points associated with aromatic biosynthesis. K. marxianus ITD0090 showed remarkable metabolic flexibility, favoring 2-PEA over 2-PE. ARO9 overexpression appeared to compensate for ARO8 inactivation, while the shikimate pathway remained active despite external L-phenylalanine, supporting de novo phenylalanine synthesis. The preferential accumulation of 2-PEA may represent a cellular detoxification strategy. These results emphasize the potential of K. marxianus ITD0090 as a robust, non-engineered platform for cost-effective aroma production without genetic modification or expensive supplementation. This work provides novel insights into alternative metabolic strategies in non-conventional yeasts and opens perspectives for optimizing nitrogen- and carbon-regulated pathways to improve the sustainable production of natural flavor compounds.
Supplementary Information
The online version contains supplementary material available at 10.1038/s41598-025-21148-6.
Keywords: 2-PEA, 2-PE, Aroma production, L-phenylalanine, Nitrogen limitation, Volatile compounds
Subject terms: Functional genomics, Metabolic engineering, Biotechnology, Genetics, Molecular biology
Introduction
The aromatic compounds 2-phenylethanol (2-PE) and 2-phenylacetate (2-PEA) are volatile metabolites of great industrial interest due to their unique organoleptic characteristics, which include sweet, fruity, and floral aromas, similar to rose petals. These compounds are used in the oenological, fragrance, and food industries, where they contribute significantly to the sensory profile of fermented products1–3. Despite its high commercial value, natural 2-PE is expensive to produce, with a price tag of approximately $1000/kg, which has led the industry to rely on chemical synthesis from benzene or styrene at a significantly lower cost ($5/kg)4. At the same time, there is a growing interest in natural, bio-based products as sustainable alternatives to synthetic chemicals, with the aim of reducing environmental impact. This global demand has motivated the search for biotechnological alternatives for sustainable and natural production.
The global flavor and fragrance market, which includes compounds, such as 2-PE and 2-PEA, reached a value of $28.5 billion in 2022 and is expected to grow at a Compound Annual Growth Rate (CAGR) of 5.3% between 2023 and 2030, driven by the increasing demand for natural and organic products in the food, cosmetics, and pharmaceutical industries5. The fragrance sector alone represented 35% of this market, underscoring the economic importance of efficient and natural aroma compound production systems5.
Kluyveromyces marxianus is a non-conventional yeast that has emerged as a promising platform for the biosynthesis of aromatic compounds. Beyond aroma production, this yeast has also been reported as a host for the synthesis of other functional bioproducts, such as antioxidant exopolysaccharides obtained under optimized fermentation conditions, which demonstrated significant biological activity6. These examples reinforce its potential not only for aroma production but also for the development of diverse high-value compounds. This thermotolerant yeast is characterized by its rapid growth, broad substrate spectrum (including lactose and inulin), high metabolic flux capacity, and resilience under stress conditions, making it attractive for industrial applications7–10. Its ability to metabolize L-phenylalanine (L-Phe) through the Ehrlich pathway enables the production of fusel alcohols such as 2-PE and their corresponding ester 2-PEA, particularly under nitrogen-limiting conditions11.
In the absence of exogenous L-Phe, K. marxianus is capable of de novo synthesis of aromatic compounds via the shikimate pathway, which utilizes glucose to produce L-Phe, tyrosine, and tryptophan, subsequently feeding into the Ehrlich pathway12. More recently, K. marxianus has also been engineered to produce high-value molecules such as resveratrol by incorporating heterologous plant genes that exploit its native aromatic amino acid biosynthesis pathways13.
While most recent biotechnological strategies rely on metabolic engineering, including overexpression of genes such as ARO9, ARO10, and ATF1 in Saccharomyces cerevisiae or Candida glycerinogenes to boost 2-PE and 2-PEA production14,15, native strains of K. marxianus such as ITD0090 can produce these compounds without genetic modification. Previous studies on engineered K. marxianus strains have achieved significant 2-PE production (1.3 g/L) using minimal media, demonstrating its metabolic potential12,16.
Despite this promise, one of the main challenges associated with the production of 2-PE and 2-PEA is the cytotoxicity of these metabolites, which can impair cell growth and metabolic activity. Therefore, understanding the regulatory and metabolic mechanisms that allow certain strains to tolerate or mitigate this toxicity is critical for optimizing bioprocesses3,9.
In this study, we explore the endogenous regulation of biosynthetic pathways in the native strain K. marxianus ITD0090 under nitrogen-limited conditions. Through genomic and transcriptomic analyses, we identify key metabolic features that contribute to 2-PE and 2-PEA biosynthesis without the need for genetic engineering. Our findings expand the current understanding of K. marxianus physiology and support its application as a sustainable platform for aroma compound production in the context of natural product biotechnology.
To our knowledge, this is the first study that integrates physiological fermentation data with genomic and transcriptomic analyses to explain the endogenous regulation of 2-PE and 2-PEA biosynthesis in a wild-type K. marxianus strain under nitrogen limitation. Unlike most reports focused on genetically engineered yeasts, we show that K. marxianus ITD0090 naturally reprograms its metabolic flux toward ester formation, favoring 2-PEA production as a potential detoxification strategy. By uncovering unique regulatory features, such as differential expression of ARO genes and persistence of shikimate activity in the presence of L-Phe, this work provides novel insights into alternative metabolic strategies for coping with nutrient stress. These findings not only advance the understanding of non-conventional yeast metabolism but also highlight the potential of native strains as sustainable, non-engineered platforms for aroma compound production.
Materials and methods
Biological material
A strain native to the mezcal production process in Mezquital Durango (23° 28’ 22” N, 104° 24’ 40” W), K. marxianus ITD0090, from the Instituto Tecnológico de Durango and belonging to the collection of the Post-harvest Technology Laboratory was used for the trials.
Fermentation with induction and nitrogen-limiting conditions: de Novo 2-PE and 2-PEA synthesis
The method described by Adame et al.17, with some modifications, was used to carry out fermentation. Pre-inoculation of K. marxianus yeast ITD0090 was performed in 500-mL screw-top flasks containing 200 mL of YPD (yeast extract peptone dextrose) medium (20 g/L glucose, 20 g/L casein peptone, and 10 g/L yeast extract). The cells were incubated at 30 °C with shaking (120 rpm) for 12 h. For fermentation, the cells were recovered by centrifugation and resuspended in sterile distilled water and used to inoculate 100 mL flasks containing 50 mL of modified Etschmann’s medium18 (30 g/L glucose, 35 g/L Na2HPO4.2H2O, 10.5 g/L citric acid, 0.28 g/L Na2SO4, 0.17 g/L yeast extract, and 9 g/L L-Phe, called medium with L-Phe and without L-Phe, also called nitrogen limitation (de novo synthesis) at a final cell concentration of 107 cells/mL validated by Neubauer chamber counting and optical density. The cells were incubated at 30 °C with shaking (120 rpm) for 30 h. Experiments were carried out in triplicate, and samples were collected at 0, 8, 12, 24, and 30 h. The biomass and supernatant were frozen at −20 °C for analysis of aromatic compounds and expression analysis.
Quantification of aromatic compounds
To analyze the aromatic compounds produced by the yeast, volatile compounds were extracted using headspace solid-phase microextraction (HS-SPME) with a 50/30-mm divinylbenzene/carboxene/polydimethylsiloxane (DVB/CAR/PDMS) fiber at 35 °C for 1 h. Extraction was performed with 2 mL of culture medium in 10-mL vials sealed with an aluminum cap with an olitetrafluoroethylene (PTFE)/silicone septum. Quantification was performed using gas chromatography-mass spectrometry (GC-MS) (Agilent Technologies, 6890 N) equipped with an Innowax capillary column (60 μm and 0.25 mm inner diameter, 0.25 μm film thickness). The oven temperature was maintained at 40 °C for 5 min, then increased to 220 °C in increments of 10 °C per minute, and finally maintained at 220 for 30 min. High-purity helium was used as carrier gas at 0.7 mL per minute. according to the methodology previously described by Rodriguez-Campos et al.19. Compounds were identified by comparison with mass spectra in the NIST database. Standard curves were used to quantify 2-PE and 2-PEA.
Genomic study and quantification of the expression of the associated pathways for 2-PE and 2-PEA production
a) Genomic analysis.
For the genomic exploration of the 2-PE and 2-PEA production pathways, different in silico tools were used. To search the genes, present in the shikimate and Ehrlich pathways in K. marxianus, the Kyoto Encyclopedia of Genes and Genomes (KEGG) database available at https://www.genome.jp/kegg/ (L-phenylalanine, tyrosine and tryptophan biosynthesis pathway ID 00400 6/10/24 and L-phenylalanine metabolism pathway ID 00360 5/22/25) was used20–22. The reference genome of K. marxianus strain DMKU3-1042 was used to screen genes that were not found in the KEGG database and to search for transcription factors. For comparative analyses of key gene products, the amino acid sequences of K. marxianus strain DMKU3-1042 and S. cerevisiae S288C were compared using protein BLAST23. Primers were designed to assess the expression of key genes, and gene libraries were obtained from representative sequences reported in NCBI (available at https://www.ncbi.nlm.nih.gov/)24. Sequence comparison was performed by local alignments using MEGA 11 with the integrated ClustalW algorithm (available at https://www.megasoftware.net/)25. The genes selected for expression analysis, the primers designed, and their characteristics are listed in Table 1.
Table 1.
Primers designed for this study.
| Gene | Sequence | Tm | Amplicon (bp) |
|---|---|---|---|
| ALG9 | 3’-CCATCTCAGGATCCCTCTTC-5’ | 53.8 | 148 |
| 5’-CGATTCCAGCGAATAGTTGA-3’ | 51.7 | ||
| UBC6 | 3’-CCATACGAGAATGGACAATACCACG-5’ | 57.7 | 172 |
| 5’-CCACAGACCATGCTGGGTTCC-3’ | 58.3 | ||
| ARO3 | 3’-TCTGCGGTGTAATGATCGAGTC-5’ | 54.8 | 133 |
| 5’-ACCTCATCAGTGGTATCCCAA-3’ | 52.4 | ||
| ARO4 | 3’-CTGGTTTATCCTTCCCAGTCG-5’ | 54.4 | 191 |
| 5’-TGTTCCCTTCTTACCACCTC-3’ | 51.8 | ||
| PHA2 | 3’-ATTGGAAGTCGTGCTAGTGC-5’ | 58.4 | 120 |
| 5’-GCGATTATTCGGCTTACGCCTTC-3’ | 57.1 | ||
| ARO8 | 3’-AATTCGGACAACCACAGAGCA-5’ | 52.4 | 186 |
| 5’-GCCCTATAACCCAGCCTAATC-3’ | 54.4 | ||
| ARO9 | 3’-GACGGTACGATCACCTATGAC-5’ | 54.4 | 63 |
| 5’-AATTGTGAGGTAGGATGGCGT-3’ | 52.4 | ||
| ARO10 | 3’-GATCTTGTGTGAAGGTGATGGTG-5’ | 55.3 | 141 |
| 5’-CTGGTTGGTCCTAGAATAGC-3’ | 51.8 | ||
| ARO80 | 3’-GCTCTCTGTACTATCACCGTTG-5’ | 54.8 | 294 |
| 5’-TTCGCAGCGTTGTATGCAAG-3’ | 51.8 | ||
| CAT8 | 3’-CGCTCGTGGTTCGTTAGAGTAC-5’ | 56.7 | 132 |
| 5’-CTATGCCAGCTCATTGTGC-3’ | 57.5 | ||
| MIG1 | 3’-GCTCAAACATGGGATTCGGAACC-5’ | 57.1 | 120 |
| 5’-CCTTCTCATCACCAGCACTACG-3’ | 56.7 |
a) Expression analysis.
To analyze the expression of key genes, the cell pellet was recovered from each fermentation sampling time, and RNA extraction was performed using TRIsure® and liquid nitrogen. The methods established in the BIOLINETM TRIsure® kit and liquid nitrogen extraction described by Sambrock and Rusel26 were used with some modifications. Cell lysis for the separation of protein and nucleic acids was performed with chloroform, and RNA precipitation was performed using isopropyl alcohol. RNA was washed twice with 75% ethanol. Finally, RNA was resuspended in diethylpyrocarbonate (DEPC)-treated water. The RNA concentration and quality were confirmed using Nanodrop® (ThermoFisher Scientific) and 1.5% agarose gel with 10% 3-(N-morpholino)-b propanesulfonic acid (MOPS), 10X acid buffer (3-(N-morpholino)-propanesulfonic acid), and 18% formaldehyde. To ensure DNA removal, treatment was performed with a DNase kit from Promega® according to protocol specifications. cDNA was synthesized following the protocols recommended by QIAGEN for the Omniscript® reverse transcription kit. Endpoint PCR was used to standardize the amplification conditions of the designed primers (Table 1), including annealing temperature and cycle parameters.
RT-qPCR was performed following the methodology established by BIO-RAD for the Sso Advanced™ Universal SYBR® Green Supermix Kit. Finally, data analyses were performed according to the specific instructions for the CFX96 Thermocycler™. All assays were performed in biological duplicate and experimental triplicate. Gene expression data were analyzed and normalized using the ΔΔCt method27. After evaluating the expression stability of multiple candidate reference genes, ALG9 and UBC6 were selected as the most suitable for normalization under the tested conditions28.
The equation used in the ΔΔCt method for the relative quantification of gene expression was as follows:
where Ct is the amplification threshold cycle; ΔCt corrects for differences in initial RNA loading; ΔΔCt compares the relative expression between the experimental sample and the control conditions; and 2−ΔΔCt determines the relative expression of the gene of interest.
Statistical analysis
The data for the aromatic compounds 2-PE and 2-PEA were assessed using the HSD-Tukey-Kramer comparison test at α = 0.01. All statistical analyses were performed using JMP software version 13.2 (SAS Institute, Inc., NC, USA).
Results and discussion
Aromatic compound production
Aromatic compounds produced by the yeast K. marxianus were detected after cultivation under nitrogen-limiting conditions (de novo synthesis) and induction conditions for the activation of these compounds. Those produced by the Ehrlich route from phenylalanine were identified. The complete aromatic composition detected in our fermentation assays, including alcohols, esters, and fatty acids with relevant organoleptic properties, is summarized in Table 2. These metabolites represent the compounds of greatest interest for fermentation-derived aroma production. The presence of esters derived from higher alcohols and fatty acids was particularly notable, as these metabolites contribute fruity and floral notes to fermented products. Similar profiles of volatile esters have been reported in previous studies17,29, where they were associated with the distinctive aroma of alcoholic beverages produced from musts30–32. The presence of phenylalanine in the culture medium favors aroma production. It has been reported that isoamyl acetate, 2-PE, and 2-PEA are produced de novo independent of a nitrogen source29. In addition, fermentations of agave must with K. marxianus under nitrogen-limiting conditions have been reported to preferentially enhance the production of 2-PE and 2-PEA33. This suggests that the nitrogen composition of the natural substrate plays a key role in redirecting metabolic flux toward the Ehrlich pathway, thereby favoring the accumulation of aromatic alcohols and esters during long fermentation processes. The production of acetate esters, such as isoamyl acetate and 2-PEA, is carried out by synthesizing acetyl-CoA and alcohol (isoamyl and 2-PE, respectively) and an alcohol acetyltransferase enzyme (AATase). This synthesis is regulated by parameters such as the presence of unsaturated fatty acids, precursor molecules, nitrogen sources, and oxygen. However, the most determining factors are the availability of the substrate (higher alcohol), the levels of acetyl-CoA in the cytoplasm, and the expression and activity of alcohol acetyltransferase enzymes32,34–36.
Table 2.
Volatile metabolites synthesized by K. marxianus ITD0090 during fermentation under nitrogen limitation and L-Phe supplementation.
| Compound | RT | Formula | m/z | Sensorial description |
|---|---|---|---|---|
| Isoamyl acetate | 6.8 | C7H14O2 | 87-70-61-55-43 | Banana, fruity and sweet |
| Isoamyl alcohol | 9.5 | C5H12O | 70-55-41 | Banana, fruity and malt |
| Benzaldehyde | 19.8 | C7H6O | 84-77-63-51 | Almonds, cherry and sweet |
| 2-Phenylethyl acetate | 28.8 | C10H12O2 | 104-91-78-65-51-43 | Floral, fruity and sweet |
| 2-Phenylethyl propanoate | 30.5 | C11H14O2 | 104-91-77-57-41 | Floral, rose and sweet |
| 2-Phenylethanol | 31.3 | C8H10O | 103-91-77-65-51 | Roses, fresh and leafy |
The metabolites that could be quantified in this study corresponded to 2-PE and 2-PEA, the final metabolites of the Ehrlich pathway produced by the presence of L-Phe as an inducer. Production occurred both in de novo synthesis via the shikimate pathway and subsequent incorporation into the Ehrlich pathway to produce these aromatic metabolites12. Additionally, 0.227 g/L of 2-PE and 0.630 g/L of 2-PEA were produced by de novo synthesis. When production was induced with L-Phe, 0.435 g/L of 2-PE and 1.0 g/L of 2-PEA were produced (Table 3and Table S1). Studies have shown that 2-PE and 2-PEA production in K. marxianus strains varies depending on the composition of the culture medium and the strain studied. Ivanov et al.37 used K. marxianus NBIMCC1984 and K. marxianus 35 to evaluate aroma production in culture with L-Phe, achieving 0.88 and 1.10 g/L of 2-PE after 36 h of culture. Wittmann et al.38 evaluated K. marxianus strain CBS 5670 for 2-PE and 2-PEA production with carbon sources, achieving a maximum production of 15 mM 2-PE at 40 h and 5 mM 2-PEA at 15 h. However, 2-PEA production stopped at 22 h. In contrast, in our results, production had not ceased after 30 h, indicating that bioconversion to 2-PE and 2-PEA continued to be active, with no decrease in biomass production or cell viability. The activity of the Ehrlich pathway is associated with growth, particularly in the exponential phase, so if cells continue to grow, both metabolites continue to be produced39. Increased production occurs once nitrogen and carbon sources are consumed, although intoxication by end products, such as ethanol and 2-PE, can inhibit K. marxianus metabolism32,40,41, in addition to feedback blocking the production pathway42. However, in this study, neither growth inhibition nor intoxication phenomenon occurred, as metabolism was more efficient for ester production. Garavaglia et al.43 determined that without L-Phe as a precursor and optimization of the culture medium, 2-PE production by K. marxianus was usually low, generally between 0.01 and 0.10 g/L. The fermentation model, with a limited nitrogen source of 0.17 g/L yeast extract and 9 g/L L-Phe18, resembles the natural conditions of agave must, in which K. marxianus ITD0090 can develop long fermentation times without compromising biomass production, producing a variety of aromatic compounds17,33,44. Tolerance to toxic products is crucial for optimizing production in bioprocesses, and strategies such as in situ product removal (ISPR) and adaptation and selection of tolerant strains have been shown to significantly improve productivity. ISPR methods, such as adsorption on resins and extraction in two-phase systems, mitigate product inhibition and increase the fermentation efficiency45–48. In addition, through the hybrid combination of gas extraction and vacuum evaporation, recovery processes have been shown to be effective in the initial separation of these products from liquid culture27.
Table 3.
Comparison of 2-PEA and 2-PE production by K. marxianus ITD0090 under L-phenylalanine-induced and nitrogen-limited (non-induced) conditions.
| Production of 2-PEA (g/L) | ||||||||
|---|---|---|---|---|---|---|---|---|
| Time | Whit L-Phe inductor | Nitrogen limitation | P-value | |||||
| (h) | Mean | S.E. | Mean | S.E. | ||||
| 8 | 0.170 | ± | 0.038 | 0.133 | ± | 0.001 | 0.4352 | |
| 30 | 1.00 | ± | 0.035 | 0.630 | ± | 0.030 | 0.0153* | |
| Production of 2-PE (g/L) | ||||||||
|---|---|---|---|---|---|---|---|---|
| Time | Whit L-Phe inductor | Nitrogen limitation | P-value | |||||
| (h) | Mean | S.E. | Mean | S.E. | ||||
| 8 | 0.223 | ± | 0.023 | 0.149 | ± | 0.011 | 0.0994 | |
| 30 | 0.435 | ± | 0.020 | 0.270 | ± | 0.034 | 0.0334* | |
*Significantly different means in the comparison of the effect in the presence/absence of L-phenylalanine.
Genetic engineering and synthetic biology have driven advances in the microbial production of 2-PE and 2-PEA. Several microorganisms have been modified to optimize metabolic pathways and improve their efficiency. Various strategies have enhanced 2-PE production in microorganisms: C. glycerinogenes reached 5.0 g/L via overexpression of AAP9, ARO9, ARO10, and SLC149; S. cerevisiae, 4.02 g/L through pathway fusion and PDC5 deletion50; a consortium of E. coli and M. guilliermondii, 3.77 g/L51; while K. marxianus produced >0.800 g/L using minimal media12.
2-PEA production has also been enhanced in bacterial systems. In E. coli, overexpression of aroG fbr, pheA fbr, atf1, and aro8, along with heterologous KDC and yjgB, yielded 1 g/L 2-PE and 0.687 g/L 2-PEA52. In Pseudomonas putida DOT-T1E, plasmid-based expression of Ehrlich pathway genes boosted 2-PEA production to 100 ppm from glucose53.
In this study, competitive production was achieved without genetic modification, indicating that K. marxianus strain ITD0090 can be considered a potential microbial chassis for the biosynthesis of aromatic compounds, offering a favorable cost-benefit ratio by not requiring supplementation with expensive amino acids or nitrogen sources based on ammonium salts that limit aroma production due to transcriptional inhibition of metabolic pathways.
Genomic study and quantification of the expression of the associated pathways for 2-PE and 2-PEA production
a) Via the shikimate pathway.
2-PE and 2-PEA can be produced de novo through the shikimate pathway, which uses phosphoenolpyruvate (PEP), a derivative of glycolysis, and erythrose-4-phosphate (E4P), a product of the pentose phosphate pathway, as substrates. In yeast, the 3-deoxy-D-arabinoheptulosonate-7-phosphate (DAHP) synthases Aro3 and Aro4 initiate the biosynthesis of L-phenylalanine, tyrosine, and tryptophan, converting E4P and PEP to DAHP. These enzymes are regulated through a negative feedback process in which Aro3 is inhibited by L-Phe and high concentrations of tyrosine and tryptophan and Aro4 are inhibited by the presence of tyrosine and high concentrations of L-Phe and tryptophan54. The K. marxianus reference strain possesses a single copy of the ARO3 and ARO4 genes. However, analysis of its conserved domain revealed structural differences compared to S. cerevisiae (Table 4), suggesting possible variations in their function. In expression analyses, ARO3 was overexpressed at 8 h, maintaining this level up to 12 h under both experimental conditions. ARO4 showed overexpression at 8 h in the presence of L-Phe, and its expression doubled during de novo synthesis, indicating a possible differential regulatory mechanism for this strain.
Table 4.
Comparative analysis of the amino acid sequence of the evaluated genes. The gene identifier, amino acid length, and predicted conserved domain are included.
| Gene | K. marxianus | S. cerevisiae | ||||
|---|---|---|---|---|---|---|
| Locus tag | Aa | Conserved Domain | Locus tag | Aa | Conserved Domain | |
| ARO3 | KLMA_40107 | 372 | AroG1 | YDR035W | 370 | AroFGH |
| ARO4 | KLMA_20414 | 364 | AroG1 | YBR249C | 370 | AroFGH |
| PHA2 | KLMA_70162 | 311 |
PBP2_PDT_like, ACT_CM-PDT. |
YNL316C | 334 | PBP2_PDT_like, ACT_CM-PDT |
| ARO8 1 | KLMA_20259 | 497 | Aro8 | YGL202W | 500 | Aro8 |
| ARO8 2 | KLMA_50151 | 477 | Aro8 | Not found in S.c. | ||
| ARO8 3 | KLMA_20431 | 451 | Aro8 | Not found in S.c. | ||
| ARO9 | KLMA_60423 | 530 | Aro8 | YHR137W | 513 | Aro8 |
| ARO10 | KLMA_20597 | 630 | PDC1 | YDR380W | 635 | PDC1 |
| PDC1 | KLMA_60075 | 564 | PDC1 | YLR044C | 563 | PDC1 |
| PDC1 2 | KLMA_40053 | 578 | PDC1 | Not found in S.c. | ||
| ADH | KLMA_40624 | 386 | FDH like ADH2 | Not found in S.c | ||
| ADH1 | KLMA_40102 | 348 | CAD3 | YOL086C | 348 | CAD3 |
| ADH2 | KLMA_40220 | 348 | CAD3 | YMR303C | 348 | CAD3 |
| ADH3 | KLMA_80306 | 351 | CAD3 | YMR083W | 375 | CAD3 |
| ADH4A | KLMA_20005 | 418 | PDDH | YGL256W | 382 | PDDH |
| ADH4B | KLMA_20158 | 379 | CAD3 | Not found in S.c | ||
| ADH5 | Not found in K.m. | YBR145W | 351 | CAD3 | ||
| ADH6 | KLMA_80339 | 366 | CAD1 | YMR318C | 360 | CAD1 |
| ADH7 | Not found in K.m. | YCR105W | 361 | CAD1 | ||
| SFA1 | KLMA_50315 | 384 | Alcohol DH III | YDL168W | 386 | Alcohol DH III |
| ALDA | KLMA_20672 | 583 | ALDH-SF | Not found in S.c | ||
| ALD2 | KLMA_20673 | 581 | ALDH-SF | YMR170C | 506 | ALDH_ALD2 |
| ALD22A | KLMA_30421 | 640 | ALDH_F15-22 | Not found in S.c | ||
| ALD3 | Not found in K.m. | YMR169C | 506 | ALDH-SF | ||
| ALD4 | KLMA_50012 | 521 | ALDH_F1-2_Ald2-like | YOR374W | 519 | ALDH_F1-2_Ald2-like |
| ALD5 | KLMA_40404 | 514 | ALDH_F1-2_Ald2-like | YER073W | 520 | ALDH_F1-2_Ald2-like |
| ALD6 | KLMA_10742 | 507 | ALDH_F1-2_Ald2-like | YPL061W | 500 | ALDH_F1-2_Ald2-like |
| ATF1 | KLMA_30203 | 515 | AAtase | YOR377W | 525 | AATase |
| ATF2 | Not found in K.m. | YGR177C | 535 | AATase | ||
| ARO80 | KLMA_30668 | 924 | GAL4 | YDR421W | 950 | GAL4, Fungal_TF_MHR |
| CAT8 | KLMA_80046 | 1412 | Fungal_trans, GAL4, ZIP-Cat8 | YMR280C | 1433 | Fungal_trans, GAL4, ZIP-Cat8 |
| MIG1 | KLMA_20059 | 556 | COG5048 | YGL035C | 504 | COG5048 |
| GLN3 | KLMA_30682 | 797 | ZnF-GATA, GAT1 | YER040W | 730 | GAT1 |
| GAT1 | Not found in K.m. | YFL021W | 510 | GAT1 | ||
* The reference strains K. marxianus DMKU3-1042 and S. cerevisiae S288C were used.
The presence of aromatic amino acids (AAAs) has been reported to repress Aro3 due to its affinity for L-Phe and the negative feedback mechanism. Both genes are regulated by the general control system of amino acid biosynthesis, mediated by the activator Gcn455–57. This system allows the derepression of genes under amino acid shortage, suggesting the possible intervention of other factors that favor their expression, as shown in Figure S1. This dysregulation could be due to the tyrosine-insensitive alleles of ARO4, which significantly increase the intracellular concentration of phenylalanine and tyrosine, promoting the production of derived aromatic compounds58,59. Interestingly, the overexpression of ARO3 and ARO4, as key players in the de novo synthesis of phenylalanine, is consistent with the observations of60, who posited that the overexpression of genes related to the Ehrlich pathway, including ARO9 and ARO10, could increase 2-PE and 2-PEA production.
Dihydroxyacetone phosphate (DHAP) is converted to chorismate through the action of the Aro1 and Aro2 enzymes. From this point, chorismate is channeled into the production of prefenate, which is subsequently transformed into phenylpyruvate. At this stage, the synthesis of the amino acids L-Phe and tyrosine is regulated by Aro7, and the conversion of chorismate to anthranilate, a precursor of tryptophan, is mediated by Trp2 and Trp3. The PHA2 gene plays a key role in the distribution of shikimate pathway intermediates to phenylalanine synthesis. Gene expression analyses showed that PHA2 was active in presence and absence of L-phenylalanine as inducer, with expression levels between 1.7 and 3 times higher than the threshold during fermentation. These results confirm the de novo synthesis of phenylalanine from precursors of the shikimate pathway. However, previous studies have reported that Pha2 activity may be regulated by the intracellular L-Phe concentration12,61. High phenylalanine concentrations have been observed to inhibit Pha2 enzymatic activity, limiting its function and preventing its excessive overproduction. However, in K. marxianus ITD0090, this negative feedback mechanism was not detected, suggesting differential regulation of the pathway in this strain. Once L-Phe is produced, it is used to produce 2-PE and 2-PEA via the Ehrlich pathway. This route has been used as an inducer system by exogenously adding L-Phe and stimulating the production of these metabolites.
a) Ehrlich pathway
In S. cerevisiae, the first step of transamination of L-Phe to phenylpyruvate is catalyzed by amino acid transaminase isoenzymes associated with the ARO8 and ARO9 genes. In the results obtained from the in silico analysis performed using the Ehrlich pathway in K. marxianus (Table 4), this first step can be catalyzed by four genes encoding three copies of the ARO8 gene and one copy of the ARO9 gene. This represents an overrepresentation of genes in this step of the pathway with respect to S. cerevisiae. Both Lertwattanasakul et al.62 and Rajkumar and Morrissey12 discussed the presence of one copy of the ARO8 gene; however, three duplicated proteins were found to share features, such as the same functional aminotransferase domain, lysine residue as the catalytic site, enzyme folding sites, and pyridoxal 5’-phosphate binding and homodimerization sites, suggesting their functional potential.
According to in silico analysis, ARO9 is conserved in a single copy, as in S. cerevisiae. The first step can also be catalyzed by other aminotransferase enzymes with similar functional domains, such as AAT1, AAT2, and HIS5, reported with a single copy in the genome of K. marxianus. However, these enzymes have been related more to the synthesis of aspartate, asparagine, and histidine63.
ARO8 expression levels remain below threshold and are significantly lower in the presence of L-Phe (Fig. 1). This repression of aminotransferase expression contradicts literature reports. Although Romagnoli et al.61 reported that ARO8 is constitutively expressed and participates in L-Phe degradation with particularly low expression levels, the observed values were almost 0, despite having 3 copies of the gene. In contrast, in the absence of a nitrogen source, de novo synthesis resulted in an expression level close to the threshold representing constitutive expression, with a downward trend towards 30 h, which could be considered a repression in the expression of this gene. Studies have suggested that ARO8 repression in yeast is influenced by catabolic nitrogen and glucose repression, affecting 2-PE production and the expression of related genes14,64.
Fig. 1.
Comparison of metabolic pathways and gene expression levels of K. marxianus ITD0090 with and without L-phenylalanine as inducer. (A) Shows the deregulation of the Shikimate and Ehrlich pathways in the presence and absence of L-phenylalanine, highlighting the differences in key gene expression and metabolic fluxes. Metabolic pathway based on that reported in KEGG20–23. (B) Shows that ARO8, ARO9, ARO10 and other key factors are differentially regulated (green: overexpression, red: repression). Numerical values represent relative expression levels under each condition, while (C) Illustrates the genes that are transcription factors and the genes they regulate. Arrows indicate transcription or repression action.
However, ARO9 showed overexpression in the presence of L-Phe, with two major peaks: the first at 8 h with an 8-fold overexpression and the second at 24 h with a 22-fold overexpression (Figure S1). Romagnoli et al.60 reported that ARO9 was inducible by aromatic aminoacids, such as L-Phe, tyrosine, and tryptophan, participating in the degradation of the latter when in excess. In de novo synthesis, ARO9 overexpression was even higher, maintaining this overexpression throughout fermentation.
The apparent inactivity of ARO8 in K. marxianus strain ITD0090 contrasts with reported results14,61. Because there is variation in the expression levels, at least one of the copies has activity, in addition to the presence of a functional analogue, such as ARO9, which could be the main analogue. Although ARO9 showed different kinetic properties from ARO8, elements outside the gene architecture, such as position in the genome, regulatory modules, transcriptional factors, and even null mutations in ARO8 in any of the copies, can be partially complemented by it, which may have occurred in this study.
The apparent ARO8 dysfunction is notable, as mutations in essential metabolic genes are uncommon. This may reflect adaptive evolution in K. marxianus, a yeast known for its superior fermentation capacity and metabolic efficiency compared to S. cerevisiae, largely due to its distinct genome structure62. Transcriptomic analyses reveal specialized pathways for oxidative stress tolerance, rapid growth, and high metabolite yields, supported by an overrepresented transporter system that enhances enzyme mobilization and overall metabolic performance7,8.
Aro8 has been reported to not be functional when the main nitrogen source is ammonium. However, in this study, the main nitrogen source was L-Phe. Wang et al.14 showed that ammonium sulfate did not affect ARO8 expression but significantly decreased enzymatic activity, which was related to lower 2-PE production. Mares-Rodriguez et al.44 suggested a constant production of ammonium by environmental nitrogen fixation due to the presence of the endosymbiont bacterium, Bacillus tequilensis, but no decrease in 2-PE production was observed, which could be attributed to the fact that ARO9 has this function.
Deletion of ARO8 has been reported to trigger de novo production of L-Phe, which increases 2-PE production in cultures using glucose and ammonium as nitrogen sources12,61. Although our experimental conditions were not identical, we observed that the level of ARO8 transcripts in both conditions was very low. ARO9 overexpression in the absence of the inducer is evidence of de novo L-Phe synthesis. In the presence of the inducer, de novo-produced L-Phe was targeted for conversion to 2-PE and subsequently 2-PEA, along with L-Phe present in the medium, resulting in high concentrations of these aromatic compounds. ARO9 overexpression is a subject of interest in metabolic engineering for 2-PE and 2-PEA production, as ARO9 and ARO10 overexpression together has been shown to significantly increase 2-PE production60. However, K. marxianus ITD0090 appears to only require ARO9 for that purpose.
The second step of the Ehrlich pathway involves the decarboxylation of phenylpyruvate to synthesize phenylacetaldehyde. In S. cerevisiae, this reaction is catalyzed by three pyruvate decarboxylase isoenzymes, Pdc1, Pdc5, and Pdc6, in addition to the phenylpyruvate decarboxylase Aro10, which generally has a higher affinity for the substrate11,38,65. In the genome annotated by the KEGG database of K. marxianus, Aro10 was the only enzyme predicted in this reaction. However, two homologous genes containing the pyruvate decarboxylase (PDC) domain were identified in the K. marxianus genome (Table 4). Moreover, Rajkumar and Morrissey12 identified a PDC5 gene, whose enzymatic activity is not yet fully characterized, but which could also function as a possible analog for this step. In this study, ARO10 showed low expression levels in de novo synthesis and induction with L-Phe, which remained stable throughout fermentation under both conditions. This result was not related to the kinetics of 2-PE or 2-PEA production, which were produced after 8 h of fermentation (Table S1).
Romagnoli et al.66 noted that only Aro10 and Pdc5 could decarboxylate phenylpyruvate, whereas Pdc1 and Pdc6 did not exhibit this activity, suggesting that low Aro10 levels could be compensated for by the action of another enzyme with pyruvate decarboxylase activity. Furthermore, in silico analyses revealed that the conserved domain of ARO10 in K. marxianus was similar to that of the two copies of PDC1, indicating a functional analogy between these enzymes and reinforcing the idea of compensatory activity. However, the slight difference in ARO10 expression levels at 30 h could be related to high cell density, which coincides with the time of highest aroma production during the stationary phase according to Wang et al.67.
Once phenylacetaldehyde is formed, it can be reduced to form 2-PE or oxidized to form phenylacetate. To produce phenylacetate (PA), which competes with 2-PE, we identified six aldehyde dehydrogenase enzymes, which have also been reported to be present in S. cerevisiae, with some located in the cytosol (Ald2, Ald3, and Ald6) and others in the mitochondria (Ald4, Ald5, and Hfd1). However, only Ald4 and Ald6 have been shown to participate in acetate formation.
In S. cerevisiae, the reduction of phenylacetaldehyde to form 2-PE is performed by several alcohol dehydrogenases (Adh1, Adh2, Adh3, Adh4, and Adh5) or formaldehyde dehydrogenase Sfa168. In S. cerevisiae, this step, which is not yet fully elucidated in KEGG, has not identified the specific gene that acts as an alcohol dehydrogenase in L-Phe metabolism in K. marxianus. In our reference genome analysis, eight genes were detected with this possible function (Table 4). Some yeasts, such as Starmerella bacillaris, have confirmed that the enzyme Adh5 is responsible for 2-PE production69, and in K. marxianus, several isoenzymes of alcohol dehydrogenase (Adh) were identified and characterized, of which four genes stand out: KmADH1, KmADH2, KmADH3, and KmADH4. In general, the ADH genes show high sequence similarity and differential expression according to growth phase and carbon source, suggesting that each have specialized functions within the cell70.
2-PE is transformed into 2-PEA by transesterification catalyzed by alcohol acetyltransferase (Aat) enzymes, using acetyl-CoA and 2-PE as the main substrates in a process associated with their degradation68,71–73. AATs are bisubstrate enzymes that catalyze the transfer of acyl groups from an acyl-CoA donor to an acceptor alcohol74,75. In S. cerevisiae, the enzymes Atf1p and Atf2p are responsible for the synthesis of various acetate esters, whereas in K. marxianus, only ATF1 has been identified, which retains the functional domain of its homologue in S. cerevisiae76,77. The overexpression of ATF1P and ATF2P in S. cerevisiae has been reported to significantly increase acetate ester production78–80. In addition, there is evidence that Atf2p plays a key role in sterol detoxification76. AATs are not only involved in ester synthesis but also play essential roles in the detoxification of ethanol and other metabolites, CoA recycling from acyl-CoA, and fatty acid metabolism76,77,81,82. These findings suggest that ester production is not solely dependent on TAA activity but is closely linked to metabolic mechanisms that protect cellular integrity against the dysfunction of pathways essential for survival83.
A 9:1 ratio of 2-PE to 2-PEA is produced in S. cerevisiae84,85. In contrast, we obtained a 1:2 ratio between 2-PE and 2-PEA. These differences can be attributed to the addition of L-Phe3. Some strategies have been implemented to increase 2-PEA production, such as co-fermentation. The combination of K. marxianus and M. guilliermondii can limit 2-PE accumulation and favor conversion to 2-PEA86. Similarly, co-fermentation of Hanseniaspora vineae and S. cerevisiae showed a synergistic effect that significantly increased 2-PEA production possibly due to the metabolic complementarity between the species87. The gene pool of each strain also influences 2-PEA production; differences in enzymatic activity and gene regulation have been reported as determining factors. Variants of the ARO80 gene in different Saccharomyces species modify the conversion of L-Phe to 2-PEA83.
The genetic basis of aromatic compound synthesis in yeasts is complex and species-specific88. While the shikimate pathway contributes, its efficiency is limited as sugars are prioritized for growth2. In contrast, K. marxianus favors volatile production via L-Phe biotransformation through the Ehrlich pathway89,90.
Transcription factors involved in 2-PE and 2-PEA production
The regulation of the Ehrlich pathway, which is central to the biosynthesis of 2-PE and 2-PEA, is a complex and multifactorial process influenced by transcriptional regulation, nutrient availability, and environmental conditions. The transcription factor Aro80 has been identified as a key activator of ARO9 and ARO10 expression in response to aromatic amino acids such as L-phenylalanine85,91. However, its activity is modulated by additional elements, including GATA transcription factors (Gln3p, Gat1p, and Nil1p), which are responsive to nitrogen availability9.
Further complexity is added by regulators such as Gcn4p and Gln3p, which respond to amino acid availability, and carbon metabolism regulators including Mig1p, Rgt1p, and Nrg1p, which mediate glucose repression92,93. Factors involved in stress and nutrient limitation, such as Hsf1p (heat stress), Cat8p, Sip4p, Adr1p (glucose starvation), and Tye7p, Gcr1p, Ert1p, and Tda9p (growth and adaptation), may also contribute to the modulation of this pathway (Figure S2)94–96.
In silico analyses revealed differential expression of MIG1 and CAT8 during fermentation, suggesting that multiple overlapping transcriptional programs co-regulate aromatic compound production. These findings support the idea that 2-PE and 2-PEA biosynthesis is governed by a dynamic and interconnected regulatory network sensitive to nitrogen and carbon status.
Impact of key gene deregulation of the Shikimate and Ehrlich pathways on 2-PE and 2-PEA production
Our analyses revealed that deregulation of genes, such as ARO8 and ARO9, significantly influenced 2-PE and 2-PEA production. The absence of ARO8 at the transcriptomic level in both experimental conditions seemed to favor de novo phenylalanine synthesis, which increased 2-PE production, especially in cultures with glucose and ammonium as carbon and nitrogen sources12,61. In the presence of L-Phe as an inducer, the high activity of Aro9, with a higher affinity for tryptophan (Km 0.4 mM) than for phenylalanine (Km 0.2 mM) or tyrosine (Km 0.2 mM), prioritized tryptophan degradation, releasing feedback inhibition of ARO3 and ARO4. This activated the shikimate pathway, producing first tryptophan and then L-Phe and tyrosine, which subsequently inhibited ARO3 and ARO4 in the advanced stages of fermentation. In the absence of L-Phe, de novo AAA synthesis was directly activated, with Aro3 and Aro4 operating until 12 h, at which time tryptophan, L-Phe, and tyrosine production inhibited these enzymes. Aro80 expression, induced by tryptofol (tryptophan metabolite), and sustained Pha2 activity confirmed de novo L-Phe production in the presence and absence of L-phenylalanine as inducer.
The production of 2-PE and 2-PEA in the presence of L-Phe was derived from both the added inducer and de novo synthesis, whereas in its absence, it depended exclusively on the latter. ARO9 overexpression compensated for the inhibition of ARO8, driving both pathways. However, the low activity of ARO10 and ARO80 could be related to their repression in the presence of preferred nitrogen sources, such as glutamine and ammonium60. These findings highlight the regulatory complexity of the shikimate and Ehrlich pathways, suggesting the involvement of other yet unidentified genes in the production of amino acids and their derived metabolites. The phenotypic variability observed in yeast underscores the need for further studies to elucidate these mechanisms.
Our results indicate that the 2-PEA production pathway could be favored at the enzymatic level due to similarities in gene architecture and regulation, which could have significant implications for yeast physiology. In addition, 2-PEA production could be a cell strategy for detoxification. Although some enzymes are constitutively expressed, others are induced under stress or high alcohol concentrations, and function to detoxify harmful chemical intermediates and break down toxic aldehydes accumulate under stress conditions. These enzymes are usually repressed by glucose; thus, high 2-PEA production could be a defense mechanism for the cell to handle high 2-PE concentrations in the medium97–99.
Conclusions
Under nitrogen-limited conditions, K. marxianus ITD0090 consistently favored 2-phenylethyl acetate (2-PEA) over 2-phenylethanol (2-PE). With L-phenylalanine (L-Phe) supplementation, titers reached 1.00 g/L 2-PEA and 0.435 g/L 2-PE; under de novo conditions, 0.630 g/L 2-PEA and 0.227 g/L 2-PE were obtained within 30 h. Transcriptome analyzes at 8 h and 30 h indicated upregulation of Ehrlich-pathway genes, notably ARO9, while ARO8 showed low expression, suggesting possible functional compensation by ARO9. Shikimate-pathway genes (ARO3, ARO4) were expressed early and declined by 30 h, more evidently without L-Phe, consistent with a transient de novo contribution to phenylalanine supply. Together, these observations support a nitrogen-responsive shift that favors ester formation and are consistent with a hypothesis in which conversion of 2-PE to 2-PEA may mitigate product toxicity. No overt growth inhibition was observed during the 30 h window. Nevertheless, this study has limitations, as it was based on a single wild isolate and gene-expression profiling without direct flux or enzyme activity measurements. Future work should benchmark these findings against reference strains, explore targeted gene perturbations (ARO8 complementation or AATase regulation), and examine the influence of nitrogen and carbon sources, acetyl-CoA availability, and transcriptional regulators such as Aro80, GATA factors, and Mig1p-Cat8p. These directions will help establish causality, optimize titers, and guide the sustainable application of K. marxianus as a microbial platform for aroma compound production.
Supplementary Information
Below is the link to the electronic supplementary material.
Acknowledgements
The authors thank the institutions that provided the facilities, equipment, and reagents used in this work.
Author contributions
Conceptualization: KJGL, OMRQ and ETAC; investigation and data curation: KJGL, SNRF, OMRQ and ETAC; methodology: KJGL, SNRF, SMCR, JRC, OMRQ and ETAC; validation, formal analysis, and resources: KJGL, SNRF, SMCR, JRC and ETAC; writing-original draft preparation: KJGL and ETAC; writing-review and editing: KJGL, SMCR, JRC, OMRQ and ETAC; supervision: KJGL, SMCR, JRC and ETAC; project administration and funding acquisition: ETAC.
Funding
This research was supported by the National Council of Humanities, Sciences and Technologies (CONAHCYT), grant number 252373/SEP-CONACYT, through project CBF2023-2024-3120 and a scholarship for PhD student KJGL (No. 700634).
Data availability
The datasets used and/or analysed during the current study available from the corresponding author on reasonable request.
Declarations
Competing interests
The authors declare no competing interests.
Footnotes
Publisher’s note
Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
These authors contributed equally to this work: Katia J. González-Lozano and Sofía N. Rodríguez-Flores.
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Associated Data
This section collects any data citations, data availability statements, or supplementary materials included in this article.
Supplementary Materials
Data Availability Statement
The datasets used and/or analysed during the current study available from the corresponding author on reasonable request.

