Open Access Article
Pedro Florido-Moreno
a,
Diego Rodríguez-Rodrígueza,
José J. Benítezb,
Jorge Rencoret
c,
Ekram Wasseld,
Ruth E. Stark
d,
Susana Guzmán-Puyol
a,
José A. Heredia-Guerrero*a and
José C. del Río
c
aInstituto de Hortofruticultura Subtropical y Mediterránea La Mayora, Consejo Superior de Investigaciones Científicas-Universidad de Málaga (IHSM, CSIC-UMA), Bulevar Louis Pasteur 49, Malaga, 29010, Spain. E-mail: ja.heredia@csic.es
bInstituto de Ciencia de Materiales de Sevilla, Centro Mixto CSIC-Universidad de Sevilla, Calle Americo Vespucio 49, Isla de la Cartuja, Sevilla 41092, Spain
cInstituto de Recursos Naturales y Agrobiología de Sevilla, CSIC, Avda. Reina Mercedes, 10, Seville, 41012, Spain
dDepartment of Chemistry and Biochemistry, The City College of New York, City University of New York, and CUNY Institute for Macromolecular Assemblies, 85 Saint Nicholas Terrace, New York, New York 10031, USA
First published on 14th April 2026
Suberin-rich potato peel waste from the food industry was explored as a renewable source of multifunctional aliphatic and aromatic compounds. A green extraction methodology, consisting of an initial water-based extraction followed by alkaline hydrolysis with NaOH, was optimized by varying reaction time (2, 4, 6, and 8 h), temperature (40, 55, 70, 85, and 100 °C), and base concentration (0.1, 0.5, and 1 M). Response surface methodology revealed a strong combined effect of temperature and reaction time, identifying 0.5 M NaOH, 85 °C and 2 h as optimal conditions that balanced recovery yield and process sustainability. The composition of the hydrolysates was thoroughly characterized by gas chromatography-mass spectrometry (GC-MS). For comparison, a classic methanolysis protocol using extractive-free potato peels was also applied. In both approaches, the predominant compound families identified were α,ω-dicarboxylic acids and ω-hydroxy fatty acids, with octadec-9-ene-1,18-dioic acid and 18-hydroxyoctadec-9-enoic acid, respectively, as the most abundant components. Additional compound classes included fatty acids, fatty alcohols, monoglycerides, and aromatic derivatives. Unlike the classic method, which results in partial methylation of the carboxylic groups, the green method preserves these functionalities, therefore improving their suitability as potential building blocks for polymer synthesis, as demonstrated by melt-polycondensation for the fabrication of polymer coatings on aluminum substrates. The glycoalkaloids α-solanine and α-chaconine, naturally present in potato peels and highly toxic to humans, were largely removed during processing, as α-solanine was not detected and only trace amounts of α-chaconine could be found in both hydrolysates, likely due to their removal during the extraction steps and precipitation of the remainder under high-pH conditions.
Green foundation1. This work contributes to green chemistry by developing and optimizing an aqueous NaOH-based method to extract multifunctional suberin-derived compounds from potato peel waste, offering a safer and more sustainable alternative to traditional organic solvent-based methanolysis.2. The process avoids flammable solvents and hazardous reagents, significantly reduces glycoalkaloids to trace levels, and preserves carboxylic groups without methylation, enhancing their reactivity for polymer synthesis. Under optimized conditions (0.5 M NaOH, 85 °C, and 2 h), the method achieved up to 25% yield relative to dry biomass. 3. Further greening could involve replacing alkaline hydrolysis with enzymatic depolymerization using cutinases or esterases. These biocatalysts may allow depolymerization under milder, near-neutral conditions, increase selectivity for ester bonds, reduce energy consumption, and improve the environmental profile of the process within an integrated biorefinery framework. |
000 to 140
000 tons per year. This waste is especially rich in phenolic compounds and specialized plant biopolymers such as suberin.5,7
Suberin is a complex hydrophobic biopolyester, composed of a poly(phenolic) and a poly(aliphatic) domain, which plays a crucial physiological role in plant defense and water balance.8 It is predominantly deposited in the cell walls of specialized tissues such as the periderm, endodermis, and wound-healing layers, where it acts as a protective barrier. Suberin restricts the uncontrolled movement of water and solutes, prevents pathogen invasion, and minimizes mechanical damage. Its poly(aliphatic) domain is composed of long-chain fatty acids (mainly α,ω-dicarboxylic acids and ω-hydroxy fatty acids that can be functionalized in mid-positions with double bonds, diols, and epoxy groups), fatty alcohols, glycerol and derivatives, and phenolic compounds (in particular, ferulic acid) cross-linked into a polyester matrix, Fig. 1.9 The monomeric constituents of the suberin poly(aliphatic) domain have attracted increasing interest for their potential in the development of sustainable materials.9,10 Upon depolymerization, these suberin-derived monomers can serve as precursors for the synthesis of bio-based polyesters, hydrophobic coatings, adhesives, and resins. Their unique chemical structures, combining hydrophobic aliphatic chains and aromatic structures with reactive functional groups, enable the design of materials with tailored barrier, antimicrobial, and/or hydrophobic properties. Moreover, several suberin monomers, mainly aromatic molecules, exhibit antioxidant or antibacterial activity, expanding their potential uses in food packaging, biomedical formulations, and agricultural applications.
![]() | ||
| Fig. 1 Schematic representation of the proposed chemical architecture of potato suberin adapted from ref. 11, highlighting its biphasic nature with an aromatic (polyphenolic) domain associated with the primary cell wall and an aliphatic, glycerol-based polyester domain organized in lamellae. The structure of the poly(aliphatic) domain is mainly composed of long-chain fatty acids, ω-hydroxyacids, α,ω-dicarboxylic acids, glycerol, and phenolic moieties interconnected through ester linkages. These ester bonds constitute the primary cleavage sites during alkaline hydrolysis, enabling the release of multifunctional aliphatic and aromatic building blocks. The model illustrates a simplified two-dimensional section of the three-dimensional suberin network. C (in blue): carbohydrate; P (in red): phenolic; and S (in green): suberin (phenolic or aliphatic). | ||
Several methodologies have been developed for the isolation and depolymerization of suberin from plant sources. The most established approach involves exhaustive solvent extraction to remove extractives, followed by alkaline methanolysis using sodium methoxide in methanol under reflux conditions.12 On the other hand, aqueous alkaline hydrolysis is a methodology traditionally used for the chemical determination of suberin monomers13 that offers a greener and safer alternative by avoiding flammable solvents, though it may lead to partial degradation of base-sensitive molecules. More recently, ionic liquids have emerged as powerful media for suberin solubilization and mild depolymerization due to their ability to disrupt hydrogen bonding networks and ester linkages while preserving sensitive moieties.14,15 Additionally, steam-explosion has also been explored to depolymerize suberin, offering a scalable and environmentally benign alternative, though partial hydrolysis and limited chemical integrity of labile functional groups remain challenges.16 The choice of the depolymerization method significantly influences the yield, purity, and composition of the recovered suberin monomers, making method selection critical depending on the target application.
Potato peels are known to accumulate glycoalkaloids, predominantly α-solanine and α-chaconine, which serve as natural defense compounds against pests and pathogens.5 These secondary metabolites are primarily localized in the outer layers of the tuber and their concentration can be influenced by factors such as the potato variety, cultivation conditions, and storage practices. Although essential for plant protection, elevated levels of glycoalkaloids pose concerns for human health due to their toxicity.17 Therefore, proper handling and processing of potato peel by-products are critical to mitigate the risks associated with glycoalkaloid exposure and to enable their valorization in food or material applications. Several strategies have been explored to reduce the glycoalkaloid content in potato-derived materials, particularly in the peels. An effective removal strategy is achieved through solvent extraction, typically using chloroform/methanol or water/acetic acid mixtures, which can dissolve glycoalkaloids and facilitate their removal from the plant matrix.18 Ultrasound-assisted extraction has been employed to reduce extraction times as well as energy and solvent consumption, while increasing glycoalkaloid recovery yields.19 In addition, alkaline conditions have been reported to precipitate glycoalkaloid structures, representing a promising approach for detoxification of potato processing residues.20,21
In this work, we report a sustainable approach for the valorization of suberin-rich potato peels, a by-product from the food processing industry, through the development and optimization of a green extraction methodology for the recovery of multifunctional aliphatic and aromatic molecules. The process involves a preliminary aqueous extraction step followed by alkaline hydrolysis using sodium hydroxide, with systematic variation of reaction time, temperature, and base concentration to identify optimal conditions. The chemical composition of the resulting hydrolysates was analyzed comprehensively using gas chromatography-mass spectrometry (GC-MS) and compared with that obtained through a conventional methanolysis protocol applied to extractive-free potato peels. Particular attention was paid to evaluating the reduction of toxic glycoalkaloids under alkaline conditions.
Sodium metal, methanol, and dichloromethane were purchased from Sigma-Aldrich. Sodium hydroxide pellets and ethanol were obtained from Panreac. Ultrapure water (Milli-Q grade) was used in all procedures.
In both methods, the recovery yield was determined. It represents the percentage of material solubilized and recovered after hydrolysis relative to the initial dry weight of extractive-free potato peels (only the water-soluble extractives in the case of the green method) used in the reaction. It provides an estimation of the efficiency of the hydrolytic process in releasing soluble compounds from the solid matrix. The recovery yield (%) was calculated using the following eqn (1):
![]() | (1) |
The hydrolysis conditions of the green method were optimized through a face centered composite design. Two independent variables, temperature (X1, °C) and time (X2, min), were selected for the experimental design, while the yield (%) was considered as the response. Four and five variation levels were chosen for time and temperature, respectively. Factors were coded as −1, −0.3333, +0.3333, and +1 for time and as −1, −0.5, 0, +0.5, and +1 for temperature, Table S1. The statistical experimental design and optimization calculations were performed using R software (v3.63, https://www.r-project.org). The responses and variables were correlated by response surface analysis to obtain the coefficients of the following quadratic equation:
![]() | (2) |
:
1 v/v) under magnetic stirring at 1600 rpm for 10 min. Subsequently, 0.15 mL of the dispersion was electrosprayed onto an aluminum substrate (4 × 4 cm2) using a Spinbox electrospray system (Fluidnatek, Spain) operated at a voltage of 17 kV, a tip-to-substrate distance of 5 cm, and a flow rate of 0.02 mL min−1. The deposition step was repeated three times to ensure homogeneous film coverage. The resulting coatings were then subjected to thermal polymerization in an air-circulating oven at 175 °C for 60 min. For comparison, non-polymerized coatings were prepared following the same procedure but omitting the thermal curing step.
The total color difference (ΔE) between samples was calculated according to eqn (3):
![]() | (3) |
,
, and
correspond to the reference values of the unpolymerized coating.
The Browning Index (BI) was calculated using eqn (4) and (5):
| BI (%) = 100 × (x − 0.31)/0.172 | (4) |
| x = (a + 1.75 L)/(5.64 L + a − 3.012b). | (5) |
| Compounds | Classic | Green |
|---|---|---|
| α,ω-Dicarboxylic acids | 427.64 | 398.99 |
| Octane-1,8-dioic acid | 5.17 | 0.00 |
| Nonane-1,9-dioic acid | 8.90 | 0.32 |
| Hexadecane-1,16-dioic acid | 3.55 | 10.18 |
| Hexadecane-1,16-dioic acid monomethyl ester | 0.33 | — |
| Hexadecane-1,16-dioic acid dimethyl ester | 1.54 | — |
| Octadeca-9,12-dien-1,18-dioic acid | 1.44 | 3.39 |
| Octadeca-9,12-dien-1,18-dioic acid monomethyl ester | 0.00 | — |
| Octadeca-9,12-dien-1,18-dioic acid dimethyl ester | 0.48 | — |
| Octadec-9-ene-1,18-dioic acid (I) | 156.29 | 318.25 |
| Octadec-9-ene-1,18-dioic acid monomethyl ester | 23.31 | — |
| Octadec-9-ene-1,18-dioic acid dimethyl ester | 138.81 | — |
| Hydroxyoctadec-9-ene-1,18-dioic acid (various isomers) | 23.43 | 25.95 |
| Hydroxyoctadec-9-ene-1,18-dioic acid monomethyl ester (various isomers) | 2.74 | — |
| Hydroxyoctadec-9-ene-1,18-dioic acid dimethyl ester (various isomers) | 25.09 | — |
| Octadecane-1,18-dioic acid | 5.97 | 15.93 |
| Octadecane-1,18-dioic acid monomethyl ester | 0.33 | — |
| Octadecane-1,18-dioic acid dimethyl ester | 3.11 | — |
| 9,10-Dihydroxyoctadecane-1,18-dioic acid | 2.64 | 1.63 |
| 9,10-Dihydroxyoctadecane-1,18-dioic acid monomethyl ester | 0.80 | — |
| 9,10-Dihydroxyoctadecane-1,18-dioic acid dimethyl ester | 1.87 | — |
| Eicos-9-ene-1,20-dioic acid | 1.20 | 0.72 |
| Eicos-9-ene-1,20-dioic acid monomethyl ester | 0.25 | — |
| Eicos-9-ene-1,20-dioic acid dimethyl ester | 0.57 | — |
| Eicosane-1,20-dioic acid | 1.03 | 3.39 |
| Eicosane-1,20-dioic acid monomethyl ester | 0.28 | — |
| Eicosane-1,20-dioic acid dimethyl ester | 1.18 | — |
| Docosane-1,22-dioic acid | 2.41 | 6.02 |
| Docosane-1,22-dioic acid monomethyl ester | 0.50 | — |
| Docosane-1,22-dioic acid dimethyl ester | 2.59 | — |
| Tetracosane-1,24-dioic acid | 3.01 | 7.99 |
| Tetracosane-1,24-dioic acid monomethyl ester | 0.51 | — |
| Tetracosane-1,24-dioic acid dimethyl ester | 3.45 | — |
| Hexacosane-1,26-dioic acid | 1.09 | 3.73 |
| Hexacosane-1,26-dioic acid monomethyl ester | 0.44 | — |
| Hexacosane-1,26-dioic acid dimethyl ester | 1.71 | — |
| Octacosane-1,28-dioic acid | 0.15 | 1.50 |
| Octacosane-1,28-dioic acid monomethyl ester | 0.23 | — |
| Octacosane-1,28-dioic acid dimethyl ester | 1.23 | — |
| ω-Hydroxyfatty acids | 318.23 | 257.78 |
| 16-Hydroxyhexadecanoic acid | 1.73 | 3.80 |
| 16-Hydroxyhexadecanoic acid methyl ester | 1.29 | — |
| 18-Hydroxyoctadeca-9,12-dienoic acid | 1.22 | 2.18 |
| 18-Hydroxyoctadeca-9,12-dienoic acid methyl ester | 1.42 | — |
| 18-Hydroxyoctadec-9-enoic acid (II) | 97.61 | 164.71 |
| 18-Hydroxyoctadec-9-enoic acid methyl ester | 116.34 | — |
| Dihydroxyoctadec-9-enoic acid (various isomers) | 15.18 | 17.12 |
| Dihydroxyoctadec-9-enoic acid methyl ester (various isomers) | 17.82 | — |
| 9,10,18-Trihydroxyoctadecanoic acid (III) | 1.34 | 0.58 |
| 9,10,18-Trihydroxyoctadecanoic acid methyl ester | 0.48 | — |
| 18-Hydroxyoctadecanoic acid | 0.31 | 0.83 |
| 18-Hydroxyoctadecanoic acid methyl ester | 0.46 | — |
| 20-Hydroxyeicosanoic acid | 0.64 | 1.28 |
| 20-Hydroxyeicosanoic acid methyl ester | 0.94 | — |
| 22-Hydroxydocosanoic acid | 5.65 | 11.36 |
| 22-Hydroxydocosanoic acid methyl ester | 5.60 | — |
| 24-Hydroxytetracosanoic acid | 9.78 | 26.39 |
| 24-Hydroxytetracosanoic acid methyl ester | 12.14 | — |
| 26-Hydroxyhexacosanoic acid | 5.56 | 15.80 |
| 26-Hydroxyhexacosanoic acid methyl ester | 10.54 | — |
| 28-Hydroxyoctacosanoic acid | 3.35 | 12.40 |
| 28-Hydroxyoctacosanoic acid methyl ester | 7.72 | — |
| 30-Hydroxytriacontanoic acid | 0.56 | 1.34 |
| 30-Hydroxytriacontanoic acid methyl ester | 0.57 | — |
| Fatty acids | 104.50 | 170.43 |
| n-Tetradecanoic acid | 0.20 | 0.49 |
| n-Hexadecanoic acid | 5.95 | 8.92 |
| n-Heptadecanoic acid | 0.10 | 0.26 |
| Octadeca-9,12-dienoic acid | 0.52 | 2.11 |
| Octadec-9-enoic acid | 0.81 | 1.96 |
| n-Octadecanoic acid | 3.62 | 4.37 |
| n-Eicosanoic acid | 0.33 | 1.64 |
| n-Eicosanoic acid methyl ester | 0.41 | — |
| n-Heneicosanoic acid | 0.23 | 0.54 |
| n-Docosanoic acid | 1.77 | 2.51 |
| n-Docosanoic acid methyl ester | 2.87 | — |
| n-Tricosanoic acid | 0.37 | 1.40 |
| n-Tetracosanoic acid | 4.70 | 15.42 |
| n-Tetracosanoic acid methyl ester | 6.01 | — |
| n-Pentacosanoic acid | 0.17 | 1.11 |
| n-Hexacosanoic acid | 7.26 | 20.38 |
| n-Hexacosanoic acid methyl ester | 11.82 | — |
| n-Heptacosanoic acid | 0.28 | 1.59 |
| n-Octacosanoic acid (IV) | 17.81 | 47.56 |
| n-Octacosanoic acid methyl ester | 16.75 | — |
| n-Nonacosanoic acid | 3.06 | 15.46 |
| n-Triacontanoic acid | 12.31 | 42.42 |
| n-Triacontanoic acid methyl ester | 6.07 | — |
| n-Hentriacontanoic acid | 0.13 | 1.50 |
| n-Dotriacontanoic acid | 0.70 | 0.77 |
| n-Dotriacontanoic acid methyl ester | 0.22 | — |
| Fatty alcohols | 78.41 | 148.51 |
| n-Hexadecanol | 2.09 | 2.29 |
| n-Heptadecanol | 0.14 | 0.13 |
| n-Octadecanol | 3.48 | 4.18 |
| n-Nonadecanol | 2.33 | 2.97 |
| n-Eicosanol | 1.04 | 1.59 |
| n-Heneicosanol | 15.08 | 15.84 |
| n-Docosanol | 6.20 | 9.30 |
| n-Tricosanol | 2.81 | 1.66 |
| n-Tetracosanol | 7.03 | 10.89 |
| n-Pentacosanol | 0.46 | 1.22 |
| n-Hexacosanol | 10.92 | 18.30 |
| n-Heptacosanol | 0.68 | 2.20 |
| n-Octacosanol (V) | 24.23 | 61.29 |
| n-Nonacosanol | 1.10 | 7.74 |
| n-Triacontanol | 0.84 | 8.92 |
| Monoglycerides | 42.07 | 3.52 |
| Monoacylglyceryl esters of fatty acids | ||
| 1-Monohexadecanoylglycerol | 0.50 | 0.74 |
| 1-Monooctadecanoylglycerol | 1.00 | 2.78 |
| 1-Monoeicosanoylglycerol | 0.11 | 0.00 |
| 1-Monodocosanoylglycerol | 0.23 | 0.00 |
| 1-Monotetracosanoylglycerol | 0.42 | 0.00 |
| 1-Monohexacosanoylglycerol | 1.12 | 0.00 |
| 1-Monooctacosanoylglycerol (VI) | 2.01 | 0.00 |
| 1-Monotriacontanoylglycerol | 1.00 | 0.00 |
| Monoacylglyceryl esters of α,ω-dicarboxylic acids | ||
| 2-Mono(octadec-9-ene-18-oic acid-oyl)glycerol | 1.45 | 0.00 |
| 2-Mono(octadec-9-ene-18-oic acid-oyl)glycerol methyl ester | 0.91 | — |
| 1-Mono(octadec-9-ene-18-oic acid-oyl)glycerol (VII) | 10.40 | 0.00 |
| 1-Mono(octadec-9-ene-18-oic acid-oyl)glycerol methyl ester | 14.15 | — |
| Monoacylglyceryl esters of ω-hydroxyfatty acids | ||
| 2-Mono(18-hydroxyoctadec-9-enoyl)glycerol | 0.78 | 0.00 |
| 1-Mono(18-hydroxyoctadec-9-enoyl)glycerol (VIII) | 8.00 | 0.00 |
| Aromatics | 29.14 | 20.78 |
| Vanillin | 0.35 | 0.69 |
| Vanillic acid (IX) | 1.75 | 1.02 |
| Vanillic acid methyl ester | 2.25 | — |
| Coniferyl alcohol | 0.46 | 1.16 |
| Ferulic acid (X) | 2.25 | 8.02 |
| Ferulic acid methyl ester | 3.16 | — |
| Caffeic acid (XI) | 0.08 | 0.67 |
| Quinic acid (XII) | 10.84 | 0.28 |
| Feruloyl esters | ||
| Glycerol ferulate (XIII) | 2.88 | 0.00 |
| n-Hexadecyl ferulate | 0.00 | 1.12 |
| n-Octadecyl ferulate | 0.00 | 1.04 |
| n-Nonadecyl ferulate | 0.00 | 0.42 |
| n-Eicosanyl ferulate | 0.00 | 0.34 |
| n-Heneicosanyl ferulate | 0.00 | 3.53 |
| n-Docosanyl ferulate | 0.00 | 0.87 |
| n-Tricosanyl ferulate | 0.00 | 0.73 |
| n-Tetracosanyl ferulate | 0.00 | 0.89 |
| Feruloyl esters of ω-hydroxyfatty alcohols | ||
| 18-O-Feruloyloxyoctadec-9-enoic acid methyl ester (XIV) | 5.12 | — |
Different families of compounds were identified in the hydrolysates obtained by the classic and green methods, and their relative abundances, calculated from the data reported in Table 1, are presented in the histogram shown in Fig. 5. The most abundant in both hydrolysates was α,ω-dicarboxylic acids, reaching 427.64 mg g−1 of hydrolysate in the classic method and 398.99 mg g−1 in the green one. These were followed by ω-hydroxyfatty acids, with concentrations of 318.23 and 257.78 mg g−1 for the classic and green methods, respectively. Other families included fatty acids (104.50 and 170.43 mg g−1), fatty alcohols (78.41 and 148.51 mg g−1), monoglycerides (42.07 and 3.52 mg g−1), and aromatic compounds, including alkyl ferulates (29.14 and 20.78 mg g−1), for the classic and green methods, respectively.
![]() | ||
| Fig. 5 Abundance (mg g−1 of hydrolysate) of the main families of compounds released from potato suberin using the classic and green methods. | ||
Notably, the green aqueous NaOH hydrolysis yielded higher amounts of free fatty acids and fatty alcohols compared to the classical methanolysis. This behavior can be attributed to the absence of organic solvent-based extraction during the pre-treatment step, which in the classical protocol removes a significant portion of the lipophilic compounds, which are known to be present in potato peels,23 prior to depolymerization. By omitting this extraction stage, the green method retains these components within the matrix, allowing their subsequent release during alkaline hydrolysis. Conversely, monoglycerides were reduced by more than 90% under green conditions, likely due to more extensive ester bond cleavage promoted by the aqueous alkaline medium. Such hydrolysis also contributes to the observed increase in free fatty acid content, as monoglycerides are converted into their corresponding fatty acids and glycerol units.
Importantly, the classic method (based on methanolysis with sodium methoxide that acts simultaneously as a strong nucleophile and transesterification catalyst) induces partial methylation of carboxylic acid groups, leading to the formation of methyl esters. This transesterification complicates the GC-MS interpretation, particularly for α,ω-dicarboxylic acids, which may appear as free acids, mono- or dimethyl esters, thereby increasing chromatographic complexity in interpretation and quantification. In contrast, the green NaOH hydrolysis preserves the free carboxylic functionalities of the released monomers, facilitating their identification and enabling a more straightforward structural characterization. From a functional standpoint, the presence of unsubstituted carboxylic and hydroxyl groups substantially enhances the reactivity of the monomers in condensation reactions, making them more effective and versatile precursors for the synthesis of bio-based polyesters. This difference underscores not only the chemical selectivity and structural integrity achieved by the green method, but also its superior suitability for downstream polymerization and sustainable material design.
The most important monomeric compounds released using the classic method (Fig. 3A and Table 1) were octadec-9-ene-1,18-dioic acid (peak 15, structure I) and 18-hydroxyoctadec-9-enoic acid (peak 13, structure II), alongside their methyl ester derivatives octadec-9-ene-1,18-dioic acid dimethyl ester (peak 8) and 18-hydroxyoctadec-9-enoic acid methyl ester (peak 9). Similarly, the most prominent monomeric compounds released using the green hydrolysis method (Fig. 3B and Table 1) were 18-hydroxyoctadec-9-enoic acid (peak 13) and octadec-9-ene-1,18-dioic acid (peak 15). These results are in agreement with those from previous studies.12,22,24
The series of α,ω-dicarboxylic acids was the most abundant class of compounds released by both methods. This series ranged from octane-1,8-dioic acid (C8) to octacosane-1,28-dioic acid (C28) with the exclusive occurrence of the even carbon atom numbered homologues, and also including unsaturated compounds such as octadec-9-ene-1,18-dioic acid (I), which was the most abundant compound in the series, as well as octadeca-9,12-dien-1,18-dioic acid and eicos-9-ene-1,20-dioic acid. Mid-chain monohydroxy and dihydroxy α,ω-dicarboxylic acids were also released, including 9,10-dihydroxyoctadecane-1,18-dioic acid and various isomers of hydroxyoctadec-9-ene-1,18-dioic acid.
The series of ω-hydroxyfatty acids were the second most abundant class of compounds released using both methods. This series ranged from 16-hydroxyhexadecanoic acid (C16) to 30-hydroxytriacontanoic acid (C30), with the exclusive occurrence of the even carbon atom numbered homologues, and including unsaturated compounds, such as 18-hydroxyoctadec-9-enoic acid (II), which was the most abundant one. Additionally, several di-and tri-hydroxyfatty acids were identified, including 9,10,18-trihydroxyoctadecanoic acid (III).
The series of fatty acids were found in the range from n-tetradecanoic acid (C14) to n-dotriacontanoic acid (C32), with a strong predominance of the even carbon-numbered homologues, and n-octacosanoic acid (C28, IV) being the most predominant compound. Additionally, the unsaturated octadec-9-enoic (oleic, C18:1) and octadeca-9,12-dienoic (linoleic, C18:2) acids were also released, albeit in lower amounts.
Significant amounts of fatty alcohols were also found in the hydrolysates, particularly from the green method. The series extended from n-hexadecanol (C16) to n-triacontanol (C30), with strong predominance of the even carbon atom numbered homologues and n-octacosanol (C28, V) being the most predominant alcohol released using both methods; no unsaturated alcohols were released.
Monoglycerides were released from both methods, with a higher yield using the classic method compared to the green one, where they were present in minor quantities, as discussed above. The classic method released different classes of monoglycerides, including monoacylglycerides of fatty acids, monoacylglycerides of ω-hydroxyfatty acids and monoacylglycerides of α,ω-dicarboxylic acids. In contrast, the green method exclusively released monoacylglycerides of fatty acids, specifically 1-monohexadecanoylglycerol (1-monopalmitin) and 1-monooctadecanoylglycerol (1-monostearin). In the classic method, monoacylglycerides of fatty acids ranged from 1-monohexadecanoylglycerol (C16) to 1-monotriacontanoylglycerol (C30), featuring only even carbon atom numbered homologues with the maximum for 1-monooctacosanoylglycerol (C28, VI) and the absence of unsaturated fatty acids. The monoacylglycerides of α,ω-dicarboxylic acids released were primarily represented by 1-mono(octadec-9-ene-18-oic acid-oyl)glycerol (VII) (both in its free form and as its methyl ester), with minor amounts of the 2-mono(octadec-9-ene-18-oic acid-oyl)glycerol isomers. Similarly, monoacylglycerides of ω-hydroxyfatty acids predominantly comprised 1-mono(18-hydroxyoctadec-9-enoyl)glycerol (VIII) alongside minor amounts of its 2-mono(18-hydroxyoctadec-9-enoyl)glycerol isomer.
Finally, various aromatic compounds were identified, including vanillic acid (IX), ferulic acid (X), and caffeic acid (XI), alongside quinic acid (XII), which is produced from the hydrolysis of chlorogenic acid. Furthermore, several feruloyl esters were also identified. For example, glycerol ferulate (XIII) was released exclusively using the classic method. In contrast, a series of n-alkylferulates, ranging from n-hexadecylferulate (C16) to n-tetracosanylferulate (C24), was released solely through the green method, albeit in very small amounts, likely due to their partial hydrolysis. These alkylferulates are extractives present in significant amounts in the potato peel and were largely removed during the solvent extraction steps of the classical method. Moreover, significant amounts of feruloyl esters of ω-hydroxyfatty acids, particularly 18-O-feruloyloxyoctadec-9-enoic acid methyl ester (XIV), were released using the classic method but were absent when using the green method.
The surface morphology of the coatings was investigated by SEM, Fig. 7B. The unpolymerized coating, Fig. 7B left, exhibited a heterogeneous and wrinkled surface characterized by overlapping lamellar features and pronounced roughness at the micrometric scale. Although the layer appears largely continuous, the presence of irregular domains and occasional agglomerated fragments indicates limited coalescence and cohesion, consistent with a physically deposited film. In contrast, the thermally polymerized coating, Fig. 7B right, presents a more compact and particulate morphology, with coalesced granular domains. This microstructural evolution reflects material rearrangement and densification during thermal curing.
The thermal polymerization performed at 175 °C for 60 min in the melt state was monitored by ATR-FTIR spectroscopy. Fig. 7C shows the carbonyl stretching region (1775–1600 cm−1) of the coatings before and after curing. The spectrum of the as-sprayed coating was dominated by an intense band centered at approximately 1690 cm−1, assigned to the C
O stretching vibration of hydrogen-bonded carboxylic acid groups.26 After thermal curing, this band underwent a marked shift toward higher wavenumbers, giving rise to two main contributions at approximately 1719 and 1731 cm−1, attributed to the C
O stretching modes of hydrogen-bonded ester groups and free ester carbonyls, respectively.27 This evolution reflects the conversion of carboxylic acids into ester linkages and the concomitant reduction of acid–acid hydrogen bonding, providing spectroscopic evidence of melt-polycondensation between suberin-derived monomers.
To further characterize the thermally polymerized coating, solid-state 13C NMR spectroscopy was employed, Fig. 7D. The main resonances were assigned as follows: long-chain aliphatic methylenes (CH2)n at ∼30 ppm, methoxy carbons (CH3O) at ∼56 ppm, alkoxy methylenes (CH2O) at ∼64 ppm, secondary alcohol carbons (CHO) at ∼72 ppm, olefinic carbons (C
C) at ∼130 ppm, ester carbonyls (C
OOR) at ∼173 ppm, and carboxylic acid carbonyls (C
OOH) at ∼179 ppm.28 These signals are consistent with the chemical fingerprint of partially esterified suberin-derived monomers forming a polyester network. To estimate the extent of esterification, the carbonyl region was deconvolved into contributions from ester (C
OOR) and carboxylic acid (C
OOH) groups (inset of Fig. 7D). The analysis revealed that approximately 38% of the carbonyl functionalities correspond to ester groups, indicating partial conversion during the melt-polycondensation. This outcome can be attributed to an excess of carboxylic acid groups relative to hydroxyl groups in the hydrolyzate, in agreement with the compositional data reported in Table 1.
Compositional analysis of the hydrolysates by GC-MS revealed that the green extraction method produced a complex mixture of α,ω-dicarboxylic acids, ω-hydroxyfatty acids, fatty alcohols, free fatty acids, and aromatic derivatives. The green method presented several key advantages: (i) slightly higher overall monomeric yields compared to those with the classic sodium methoxide-based methanolysis, (ii) elimination of organic solvents and flammable reagents, (iii) preservation of a broader array of low-polarity compounds, (iv) preservation of free carboxylic groups, thus improving their suitability as potential building blocks for polymer production, and (v) significant reduction of glycoalkaloid (α-solanine and α-chaconine) content, enhancing the safety of the resulting materials.
The direct melt polycondensation of the green suberin-rich hydrolysate into polymer coatings emphasizes the practical potential of the recovered multifunctional monomers for sustainable material fabrication, establishing a complete valorization route from agro-industrial waste to bio-based coatings.
These results highlight the potential of aqueous alkaline hydrolysis as a greener, safer, and scalable alternative for suberin depolymerization in complex agro-waste, paving the way for the development of sustainable materials and chemicals from potato processing residues.
The authors thank El Tío de las Papas S.L. for kindly providing the potato peels used in this study.
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