Avocado Hass peel from industrial by-product: effect of extraction process variables on yield, phenolic compounds and antioxidant capacity

Abstract

At present in Peru, a substantial quantity of avocado by-products (peel and seed) is produced due to avocado processing. It is essential to revalue these products. The meticulous selection of parameters in solid–liquid extraction through maceration, which is the industrial preference, is crucial to obtain a greater recovery of phenolic compounds from avocado Hass peels. Therefore, the aim of this study was to assess the impact of process variables (ethanol concentration, temperature and solvent:feed (S/F) ratio) on the global yield of extraction (GY), total phenolic content (TPC), total flavonoid content (TFC), and antioxidant capacity (DPPH) of avocado Hass peel extract at two different stages of maturity. Furthermore, the quantification of phenolic compounds was using High Performance Liquid Chromatography with Diode Array Detection (HPLC-DAD) and antioxidant capacity using ABTS and FRAP assays were determined in higher yielding extracts. The dry matter content (dm) was determined in the pulp of unripe avocados (UA, 22.57% dm) and ripe avocados (RA, 27.30% dm). The results showed that, for all treatments, ethanol concentration, temperature, S/F ratio had a significant influence (p < 0.05) on GY, TPC, TFC and antioxidant capacity, and the UA peel extracts obtained with 40% ethanol, 49.3°C, S/F ratio (14.3 mL/g) and 60 min showed the highest values of TPC (44.24 mg GAE/g peel dw), TFC (786.08 mg QE/g peel dw) and antioxidant capacity against DPPH (564.82 μmTE/g peel dw), ABTS (804.40 μmTE/g peel dw) and FRAP (1006.21 μmTE/g peel dw). Meanwhile, for the HPLC-DAD analysis, vanillic acid and 4-hydroxyphenylacetic acid are the main phenolic compounds present in avocado peel extracts. The results of this research indicate that avocado peels are a source of natural phenolic components, with potential application in the food industry as a viable alternative to synthetic antioxidants, thus reducing their use.

Schematic diagram of by-product (peel) of unripe and ripe Hass avocado and its extracts, effect of main variables of extraction on the phenolic total content and the phenolic compounds in yield higher extract.

1. Introduction

One of the major current global problems is the generation of by-products from global the agro-industrial sector on a global scale. By 2010, 140 billion tons were already being produced annually, and in recent years approximately 600 million tons of fruit by-products have been generated worldwide. The by-products produced, which are considered to possesses low commercial value, exhibit a diverse variety, including peels, seeds, leaves, roots, stems, bark, bagasse, pulp, pomace, among others. One of the main concerns about these by-products is their disposal into the environment without any form of treatment, thereby posing an environmental hazard due to their high biodegradability. The biological degradation of plant by-products is the third anthropogenic contribution to atmospheric methane emissions (Banerjee et al., 2017; Mazzutti et al., 2021; Šelo et al., 2021). This process not only has environmental implications but it also has economic consequences, with estimated annual losses of approximately 940,000 million dollars (Martínez-Inda et al., 2023). In certain cases, these by-products are used for animal feed or as an ingredient in the production of animal diets (Mazzutti et al., 2021). Faced with this scenario, decisive changes in the food industry management system must be implemented within the context of the circular economy to prevent, reuse or recover the by-products by this sector (Del Rio Osorio et al., 2021; Martínez-Inda et al., 2023). In this context, the avocado processing industry is no stranger to this reality.

Avocado is one of the most produced and consumed fruits globally, and its demand has grown significantly in recent years (Rodríguez-Martínez et al., 2021; Bangar et al., 2022). Peru is the third largest avocado producer worldwide and annually yields 672,232 thousand tons (FAOSTAT, 2020). The processed avocado market will rise from US$1.70 billion in 2018 to approximately US$2.70 billion by 2024 (Ramos-Aguilar et al., 2021; Nyakangi et al., 2023). During avocado processing, the pulp is used for oil extraction, paste production, and other products. Approximately 2.42 million tons of by-products such as peel and seed are generated, which are typically discarded into the environment (Nyakangi et al., 2023). Hass variety peel represents 11–17% of the weight of the fruit (Wang et al., 2010; Rodríguez-Carpena et al., 2011; Calderón-Oliver et al., 2016; Araújo et al., 2021) and several studies indicate that it contains bioactive compounds such as organic acids (citric acid and quinic acid), phenolic acids and phenolic alcoholic derivatives (gallic acid, 5-O-caffeoylquinic acid, 3,4-dihydroxybenzoic acid, 4-hydroxybenzoic acid, syringic acid, O-caffeoylquinic acid, 5-O-caffeoyoylquinic acid, tyrosol-glucosyl-pentoside and 4-O-caffeoylquinic acid), flavonoids (rutin, quercetin-diglucoside, luteolin 7-O-(2″-O-pentosyl) hexoside, quercetin-O-arabinosyl-glucoside, quercetin glucuronide, quercetin, multinoside A, naringenin, quercetin-xylosyl-rhamnoside, kaempferol-O-glucosyl-rhamnoside, quercetin-3-β-glucoside, kaempferol and quercetin-3-O-arabinoside), catechins and procyanidins [(+)-catechin, (−)-epicatechin, procyanidin A and procyanidin B], also including β-sitosterol, α-tocopherol, cyanidin-3-glucoside, perseitol, chlorophyll a and b, lutein and volemitol (Wang et al., 2010; Rodríguez-Carpena et al., 2011; Kosińska et al., 2012; López-Cobo et al., 2016; Figueroa et al., 2018; Melgar et al., 2018; Tremocoldi et al., 2018; Araújo et al., 2021; Figueroa et al., 2021; Ramos-Aguilar et al., 2021; Rodríguez-Martínez et al., 2021; Trujillo-Mayol et al., 2021; Rojas-García et al., 2022; Martínez-Gutiérrez, 2023). Furthermore, several studies have demonstrated that the extract derived from the avocado peel antioxidant and antimicrobial properties (Raymond Chia and Dykes, 2010; Kosińska et al., 2012; Melgar et al., 2018; Tremocoldi et al., 2018; Figueroa et al., 2021; Ferreira and Santos, 2022). Additionally, it exhibits neuroprotective effects (Ortega-Arellano et al., 2019), which makes this by-product another alternative for obtaining phenolic compounds that are of interest to the food, pharmaceutical and cosmetic industries. Particularly, the food industry can use it as a nutraceutical or functional food ingredient, while promoting the utilization of avocado waste, a latent concern of the circular economy (Nyakangi et al., 2023).

The extraction of phenolic compounds from avocado Hass peel can be obtained using non-conventional technologies such as microwave-assisted extraction, ultrasound-assisted extraction, pressurized liquid extraction, and two-phase aqueous system (Del Castillo-Llamosas et al., 2021). These technologies have advantages (green, economical, processes can be completed quickly with high reproducibility, lower solvent consumption that minimizes environmental impact, higher extract purity and lower energy consumption) (Chemat et al., 2019), however, these technologies are expensive and require specialized equipment, therefore conventional methods such as maceration are still preferred in industry (Martínez-Gutiérrez, 2023), due to the combination of simplicity (easy manual handling), basal pressure (ambient conditions) and possibly mild temperature (Gil-Martín et al., 2022). Regarding the obtaining of phenolic compounds from Hass variety avocado peel by maceration, studies were conducted using fixed extraction parameters and organic solvents such as 80% methanol (Kosińska et al., 2012; López-Cobo et al., 2016; Figueroa et al., 2018, 2021), 80% acetone (Widsten et al., 2014; Figueroa et al., 2018, 2021), 70% acetone (Saavedra et al., 2017), acetone/water/acetic acid (70:29.7:0.3, v/v/v/v) (Wang et al., 2010), ethyl acetate, acetone/water (70:30 v/v) or methanol/water (70:30 v/v) (Rodríguez-Carpena et al., 2011), methanol with 0.10% trifluoroacetic acid (Ramos-Aguilar et al., 2021) and also using generally recognized as safe (GRAS) such as absolute ethanol (Raymond Chia and Dykes, 2010; Ferreira and Santos, 2022), 95% ethanol (Bowen et al., 2018), 80% ethanol (Melgar et al., 2018; Tremocoldi et al., 2018; Figueroa et al., 2021; Trujillo-Mayol et al., 2021), 60% ethanol (Rojas-García et al., 2022), 20% ethanol (Figueroa et al., 2021), boiled water (Calderón-Oliver et al., 2016), in order to characterize the individual and total compounds, and also to evaluate the biological activity of the obtained extracts.

A study carried out by Melgar et al. (2018) demonstrated a high recovery yield of phenolic compounds from Hass variety avocado peel (227.9 mg/g extract) was obtained by conventional methods using 80% ethanol as solvent. However, extraction parameters were not evaluated and the effect of ethanol concentration, temperature and solvent/solid ratio on the maximum recovery of phenolic compounds is unknown. Hence, it was hypothesized that the correct application of ethanol concentration, temperature and solvent/solid ratio would increase the total phenolic and flavonoids contents in Hass avocado peel extracts over a 60-min extraction period by maceration and, consequently, the antioxidant capacity would also increase. In this particular solid–liquid extraction method the most important parameters that impact the extraction efficiency and the minimization of loss of these compounds are the solvent concentration, the solvent:feed (S/F) ratio and the temperature (Spigno et al., 2007; Bucić-Kojić et al., 2009; Chuen et al., 2015; Drosou et al., 2015; Papoutsis et al., 2016). Within this context, the aim of this study was to assess the effect of process variables (ethanol concentration, temperature and S/F ratio) on the global yield of extraction (GY), total phenolic content (TPC), total flavonoid content (TFC), and antioxidant capacity (DPPH) of avocado Hass peel extract at two stages of maturity. Furthermore, the quantification of phenolic compounds was conducted using HPLC-DAD and the determination of antioxidant capacity (ABTS and FRAP) was performed on extracts with higher yields at both stages of maturity.

2. Materials and methods

2.1. Standards and reagents

Gallic acid, Folin–Ciocalteu’s phenol reagent, calcium carbonate, quercetin, sodium nitrite, aluminum chloride, sodium hydroxide, trolox (6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid), potassium persulfate, sodium acetate trihydrate, hydrochloric acid, glacial acetic acid, ferric chloride hexahydrate, DPPH (2,2-diphenyl-1-picrylhydrazyl), ABTS (diammonium salt of 2,2-azinobis (3-acid) ethylbenothiazoline-6-sulfonic acid), TPTZ (2,4,6tripyridyl-s-triazine) were purchased from Sigma-Aldrich (St. Louis, MO, United States). Other regents such as ethanol and methanol were analytical grade and were manufactured from Spectrum Chemicals (New Brunswick, NJ, United States).

2.2. Raw material and characterization

The avocado fruits of the Hass, known for their export quality, were harvested from La Calera Agricola farm (Alto Laran, Chincha, Peru). The fresh fruits were rinsed followed by disinfection with Kuma Nat solution (5 mL/L) for 3 min. Subsequently the fruits were left to drain. A portion of the treated fruits was stored in a ripening chamber (CLIMACELL EVO, Germany) at 28°C for a period of 3 days, while another portion was stored for 6 days. In order to separate the peel from the pulp and seed, the two distinct stages of maturation were individually subjected to manual processing. The dry matter content of the pulp was subsequently determined using the methodology proposed by Salameh et al. (2022). The present study investigated the dry matter (dm) content of avocado pulp following storage for 3 and 6 days. Results indicated that unripe avocados (UA) had a dm content of 22.57%, while ripe avocados (RA) had a significantly higher DM content of 27.30%. To remove any pulp residues, the peels were washed and then chopped into small fragments and conditioned in a dehydrator (Excalibur 4526T220FW-60, United States) and dried at 45°C for 24 h. The dehydrated peels were crushed (Bosch MMR08R2, Gerlingen, DEU) followed by sifting (Bertel, Caieiras, BR), the average particle diameter was determined in triplicate in accordance with the ASAE (1997), and was found to be 0.50 ± 0.01. The dried crushed peels were subsequently stored in a frost-free freezer (Indurama RI-279D, China) at −18°C until further use.

2.3. Experimental design

The experimental design was conducted with three independent variables and their respective ranges: ethanol concentration (EtOH, X₁: 40, 60, and 80%, v/v), temperature (T, X₂, 40°C, 50°C, and 60°C), and S/F ratio (X₃, 5, 10, and 15 mL/g, v/m). The duration of the extraction process was set at 60 min. All these parameters were considered in accordance with the outcomes of preliminary experiments. The experimental design used in this study was the Box-Behmken design (BBD), which consisted of 12 independent variable runs (runs 1–12) and three replicates at the central point (designated as runs 13–15). The BBD used three factors and three level as observed in Table 1. The relationship between the independent variables and the answers was modeled using a second-order polynomial equation (Eq. 1):

where Y is the response variable (GY, TPC, TFC, DPPH), X’s are the extraction parameters, and β’s are the coefficients. To fit the experimental data to the model equation, DESIGN-EXPERT 11.0 software (Trial version, Stat-Ease Inc., Minneapolis, MN, United States) was used.

2.4. Solvent extraction via maceration

For each extraction, a volume of 9 mL of ethanol solution with varying concentrations (EtOH, %, v/v) was used for the S/F ratio according to the experimental design (Table 1). The dried crushed peel of either UA or RA was added to a tube according to the S/F ratio. Subsequently, EtOH was added to the same tube and each extraction temperature (Table 1) was controlled using a water tank (Biobase, WT- 42, Shandong, China) for 60 min. Then, the extract was obtained via filtration using Whatman No. 4 filter paper, and the solvent of the extract was evaporated under vacuum condition (KANKUN, R-1010, Shanghai, China). The recovered extract was weighed and stored in a frost-free freezer (Indurama RI-279D, China) at −18°C until further analysis.

The GY was calculated by the ratio of the dry extract mass to dried crushed UA or RA peel mass on dry basis, according to Eq. 2.

2.5. Total phenolic content (TPC) and total flavonoid content (TFC)

The analysis of the total phenolic content was performed according to the methodology described by Cornelio-Santiago et al. (2019) with the following modifications. Test tubes were filled with 500 μL of each diluted extract, 250 μL of Folin–Ciocalteu 1 N, and left to stand for 5 min in the dark. Next, each tube received 1,250 μL of 7.5% Na₂CO₃, and the tubes were allowed to stand for 120 min in the dark. The absorbance of the samples and gallic acid (0–60 mg/L) were measured using a spectrophotometer at 760 nm (Genesys 50 UV–VIS Thermo Fisher, United States) and results were represented as mg of gallic acid equivalents (GAE)/g peel dry weight (dw).

For the analysis of total flavonoid content, some adjustments were made to the method described by Zhishen et al. (1999) as follows. In test tubes, 250 μL of each diluted extract was added, followed by 1,250 μL of distilled water, then 75 μL of 5% NaNO₂ was added, was left to stand in the dark for 6 minutes. Each tube received 150 μL of 10% AlCl₃.6H₂O, and then left 5 min in the dark. Next, 500 μL of 1 M NaOH and distilled water were added to each tube to a final volume of 2,500 μL. Finally, using a spectrophotometer (Genesys 50 UV–VIS Thermo Fisher, United States), the absorbances of the samples and quercetin (0.2–1.2 mg/mL) were measured at 510 nm and results were represented as mg of quercetin equivalent (QE)/ g peel dry weight (dw).

2.6. Determination of antioxidant capacity by DPPH, ABTS, and FRAP

The following adjustments were made based on the methodology proposed by Brand-Williams et al. (1995) for DPPH analysis. To create a stock solution, 2 mg of DPPH was dissolved in 100 mL of reagent grade methanol. Subsequently, this solution was diluted with methanol until an absorbance range of 0.9 ± 0.02 at 515 nm, thereby yielding a solution suitable for practical use. Test tubes were filled with 150 μL of each diluted extract, 2,850 μL of working solution, and allowed to stand for 30 min in the dark. The methodology used to assess the antioxidant capacity using ABTS was proposed by Re et al. (1999). The ABTS reagent was dissolved in water at a concentration of 7 mM and combined with 2.45 mM potassium persulfate in a 1:1 ratio. The mixture was kept in the dark at room temperature for 16 h allowing the formation of the radical cation ABTS (ABTS ⁺). Methanol was used to dilute the solution of ABTS ⁺ to an absorbance of 0.70 ± 0.02 at 734 nm. Test tubes were filled with 150 μL of each diluted extract, 2,850 μL of diluted ABTS^•+ solution and allowed to stand in the dark for 30 min. The FRAP method described by Benzie and Strain (1996) was prepared by combining 5 mL of a 10 mM TPTZ solution with 5 mL of a 10 mM TPTZ solution. FeCl₃.6H₂O 20 mM and 50 mL of 0.3 mM acetate buffer (pH 3.6). Test tubes were filled with 150 μL of each diluted extract, 2,850 μL of FRAP reagent, then left to stand in the dark for 30 min. Finally, the absorbances were measured at 515, 734 and 593 for DPPH, ABTS and FRAP, respectively, in a spectrophotometer (Genesys 50 UV–VIS Thermo Fisher, United States) and the results were calculated from a standard curve of Trolox (0.1–0.4 μM) and expressed as μmol of Trolox Equivalent (TE)/g peel dry weight (dw).

2.7. Determination of phenolic compounds by high performance liquid chromatography with diode array detection (HPLC-DAD)

The HPLC-DAD was used to determine phenolic compounds in accordance with the methodology proposed by Ramos-Escudero et al. (2021). The analysis was carried out with a High-Performance Liquid Chromatograph Chromaster with a diode array detector (Hitachi High-Technologies, Tokyo, JP). The separation of the analytes was performed using a LiChrospher® 100 RP-18 end-capped, 5 μm, 4.6 × 250 mm cartridge column (Millipore, Darmstadt, Germany). The injection volume was 20 μL, the flow was 1 mL/min, and the column was kept at a constant temperature of 30°C. The solvent elution used a mixture of methanol:acetonitrile (50:50 v/v) as mobile phase B and 0.5% orthophosphoric acid in water as mobile phase A. The following gradient system was used to elute the analytes (solvent B percentages are shown; the difference in the mobile phase corresponds to the mobile phase A): Starting with 5% (B), the elution progressed to 30% (B) after 25 min, 38% (B) after 35 min, 38% (B) after 40 min, 45% (B) after 45 min, 52.2% (B) after 50 min, and 100% (B) after 55 min. It was then kept at 100% (B) for 5 min to clean the column. The execution of the chromatogram lasted 60 min. Chromatograms were obtained at a wavelength of 280 nm. The identification of phenolic compounds was carried out by comparing the retention times of the extracts and the standard of phenolic compounds. The quantification of phenolic compounds in the extracts was calculated through the corresponding peak areas by external standardization, and the results were expressed in mg per Kg peel dw.

2.8. Statistical analysis

The statistical analysis of the outcomes obtained from the Box-Behmken design (BBD) was statistically analyzed using DESIGN-EXPERT 11.0 (trial version, Stat-Ease Inc., Minneapolis, MN, United States). To assess the efficacy of the model, various statistical measures were employed, including value of p, F-value, test for lack of fit, R², and Adj.R² were used by ANOVA. Furthermore, Student’s t-test using SPSS software (ver. 24.0; SPSS Inc., Chicago, IL, United States) was used to evaluate the antioxidant capacity, phenolic compound profile, and validity of predicted and experimental data of extracts with higher extraction yield in unripe and ripe avocado. For each evaluation, three replicates of the study results were used to calculate the mean and standard deviation, and a 95% confidence level was used in all analyses.

3. Results and discussion

3.1. Analysis of the effects of the factors in the experiments

The effects of varying concentration of ethanol were investigated (X₁, 40, 60, and 80% (v/v)) on several variables (GY, TPC, TFC, and DPPH). A significant effect (p < 0.05) of ethanol concentration was observed in GY and TFC in UA (Table 2), while TPC, TFC and DPPH were significant (p < 0.05) in RA (Table 3). Different concentrations of ethanol have impact on extraction yields due to the reduction of the solvent dielectric constant, causing an increase in both the solubility and diffusivity of the solute. This phenomenon was also observed by Park et al. (2012) and Garcia-Castello et al. (2015). Conversely, the highest extraction outcomes of TFC, TFC and DPPH were observed at an ethanol concentration of 40%, as shown in Table 4. Close values were found by Araújo et al. (2021)) who reported that a solution of approximately 42.58% ethanol is suitable for the extraction of phenolic compounds in avocado Hass. In contrast to the utilization of a pure solvent, it is possible to achieve superior extraction yields with excellent antioxidant capacity using a dissolvent mixed with water (Rodríguez-Carpena et al. (2011). Nevertheless, high ethanol concentrations may cause denaturation, dehydration and collapse of plant cells, which would likely be reflected in extraction yields (Garcia-Castello et al., 2015).

The extraction effectiveness and the quality of the target chemicals compounds are both significantly affected by temperature. This study also evaluated the effects of temperature (X₂, °C) on GY, TPC, TFC and DPPH. It was observed that UA had a significant influence (p < 0.05) on both TPC and TFC (Table 2). Conversely, RA only presented TFC effect (Table 3). According to Mustafa and Turner (2011), the use of thermal energy enhances the efficiency of extraction by modifying cellular structures, due to a reduction in the surface tension of the solvent and an increase in its viscosity (Vergara-Salinas et al., 2012; Jovanović et al., 2017), which would be reflected in an increase in the permeability of the cell membrane, rupture of the interactions between secondary metabolic products and the matrix; augmentation of solubility and mass transfer. Increase temperature during the extraction process may cause bioactive compounds degradation, resulting in a loss of their biological activity, as reported by Cengiz et al. (2021) and Yusoff et al. (2022). In the present investigation it was observed that at a temperature of 50°C the best outcomes were obtained in terms of TPC, TFC and DPPH. However, as the temperature was raised to 60°C the level of these compounds decreased (Table 1).

The S/F ratio is a significant parameter that effects on the extraction efficiency of bioactive compounds (Guiné et al., 2019). In this research, the effects of S/F (X3, mL/g) on GY, TPC, TFC and DPPH were evaluated. There were significant differences (p < 0.05) on GY, TPC and DPPH in UA, while in RA it had effect on GY, TPC and TFC, the results can be seen in Tables 2, 3. The higher the S/F, the greater the concentration gradient difference between the outside and the inside of the plant cell, facilitating the solvent to penetrate into the center of the plant cells and dissolve the phenolic compounds to be extracted (Nguyen and Phan, 2023). This was observed in the Figures 1, 2 indicate that an increase in the S/F from to 5 to 15 mL/g. This is the first research on avocado Hass peels that evaluates the effect of S/F ratio on extraction efficiency. It examined the highest values in TPC, TFC and DPPH in UA were achieved with the S/F ratio of 15:1 (Table 1). On the other hand, the S/F ratio has been studied in custard apple (Annona squamosa L.) peel (Nguyen and Phan, 2023), as well as in ground berries by Cacace and Mazza (2003) and seeds by Al-Farsi and Lee (2008).

Figure 1

Figure 2

3.2. Effect of experimental design on response variables by Box-Behmken Design (BBD)

Extraction parameters, namely ethanol concentration (X₁, %), temperature (X₂, °C) and S/F ratio (X₃, mL/g) were evaluated by BBD for the GY, TPC, TFC and DPPH for UA and RA. The extraction yields obtained are presented in Table 1, while Tables 2, 3 provide the results of the analysis of variance (ANOVA) of the regression model coefficients.

The regression models for GY demonstrate a good fit to the experimental data, as evidenced by the low value of ps (p < 0.05), the lack of fit is found to be non-significant (p > 0.05), and excellent coefficient of determination (R²) values (R² > 0.98). The use of response surface plots facilitated the visualization of the significance of individual extraction variables on GY in UA (Figures 1A1–A3) and RA (Figures 2A1–A3). Positive linear term coefficients (X₁ and X₃) and negative quadratic term coefficients (X₁² and X₃²) in Tables 2, 3 indicated that yields increased with the increase of ethanol concentration and S/F ratio, reaching a maximum. However, it is noteworthy that this relationship reaches a peak, further increments in ethanol concentration and S/F ratio did not result in additional yield enhancements. On the other hand, interaction terms (X₁X₃, X₂X₃) significant (p < 0.05), imply that there was a strong interaction between these two characteristics in the GY.

Upon evaluation of the TPC, it was observed that the second order model in UA and RA were significant (p < 0.05), indicating that the TPC variation is well described by the model used. This assertion is supported by the high R² values (R² ≥ 0.92), the absence of a significant lack of fit (p > 0.05) and the low coefficient of variation (CV < 2.11%). Detailed information can be observed in Tables 2, 3. The response surface plots also facilitate the visualization of individual variables in the total phenolic content (TPC) for both UA (Figures 1B1–B3) and RA (Figures 2B1–B3). The linear terms (X₂ and X₃) exhibited positive coefficients in UA, indicating a direct correlation with TPC, while the negative coefficients of the quadratic terms (X₂²) indicated an inverse relationship with TPC. Conversely, interaction terms (X₁X₃,) were significantly affected by the TFC of each other. In the context of RA, the positive linear terms coefficients (X₁ and X₃) and the negative quadratic terms (X₁² and X₃²) exhibited a similar pattern as the UA. On the other hand, interaction terms (X₂X₃) show that the TPC was considerably impacted by these two variables in relation to one another.

Figure 1 displays the regression coefficients and RSM plots for the extraction variables c₁, c₂, and c₃ for UA. Similarly, Figure 2 presents the regression coefficients and RSM plots for the extraction variables C1–C3 for RA. The visual representations aid in the comprehension and analysis of each extraction variable. The data presented in Table 2 indicates that for UA, the coefficients of the following terms were negative: (X₁), (X₂² and X₃²) and (X₁X₃, and X₂X₃,) having an indirect relationship with the TFC. Furthermore, the change in the temperature (X₂) positively affects TFC. In contrast, with respect to RA, the negative coefficients (X₁, X₂ and X₃ and X₁²) decrease the extraction of TFC, on the contrary (X₂², X₁X₂, and X₂X₃) positively influence the extraction of TFC.

The statistical analysis of DPPH revealed that the second order model in UA and RA exhibited significant results (p < 0.05). This suggests that the DPPH variation is well described by the model employed. Similarly, the results demonstrate a strong correlation between the variables, as evidenced by the high values of R² (R² ≥ 0.92) and low coefficient of variation (CV < 2.11%), indicating a good fit to the proposed model. This can be that observed in the UA graphs (Figures 1D1–D3) and RA graphs (Figures 2D1–D3). When analyzing the UA, the positive coefficients (X₃) positively influence the extraction of DPPH. On the other hand, the negative quadratic terms (X₂² and X₃²) have a negative effect on the DPPH. In contrast, upon analyzing, the regression coefficients of the RA, it is observed that they are negative (X₁, X₁², X₂², X₃²), thereby suggesting that they have a negative influence on the DPPH. When evaluating the coefficients of the interaction (X₂X₃), it is evident that the interaction between temperature and the S/F ratio have a positive influence on DPPH. The subsequent equations, namely Eq 3 and Eq 4, can be used to calculate the condition with the highest extraction yield for TPC and DPPH in ripe avocado peels.

where the test variables (ethanol concentration, temperature, and S/F ratio, respectively) are X₁, X_2, and X₃, respectively.

3.3. Validation of the model equations

Validation experiments were performed with the levels obtained for the subsequent extraction of individual responses. The experimental values are presented in Table 4. It should be noted that the experimental values in UA (TFC, TPC, and DPPH) and RA (DPPH) were higher than predicted, while in RA (TFC and TPC) they were slightly lower. These results could be associated with the fact that the raw material used for validation presented different initial values of these bioactive compounds, which was also observed by Bengardino et al. (2019). Despite these differences between the values, it should be noted that the values found experimentally reaffirm the usefulness of this tool (BBD) together with the desirability function (d) that presented a value d = 0, 92 in UA and a value of d = 1 in RA, considered as “satisfactory” by Lazic (2006), which could be verified because it maximized TFC, TPC and DPPH in UA; as well as DPPH in RA. The values obtained under the conditions suggested in the extraction are the best solution considering the responses obtained. In fact, this tool (BBD) has been used in other studies that observed similar effects (Chen et al., 2018; Kushwaha et al., 2018; Bengardino et al., 2019; Alam et al., 2021).

3.4. Antioxidant capacity

In this study, three antioxidant capacity techniques, based on free radical scavenging capacity (DPPH, ABTS) and reducing capacity (FRAP), were used to evaluate the antioxidant properties of unripe and ripe avocado extracts obtained with the highest extraction parameter combinations as shown in Table 4. The findings of this research demonstrate that the values of DPPH, FRAP and ABTS exhibit a statistically higher (p < 0.05) in unripe avocado in comparison to ripe avocado. Likewise, the present values of UA as RA exhibit higher values than those previously published by Tremocoldi et al. (2018), who reported 310 μmolTE/g to DPPH and 791,5 μmol TE/g to ABTS in ethanol extracts of avocado Hass peels. However, the present values are lower than those reported by Araújo et al. (2021), who obtained 233.85 mg TE/g dry extract for DPPH and 949 mg TE/g dry extract for ABTS. In addition, Morais et al. (2015) observed that avocado peels exhibited a greater antioxidant capacity, as determined by the FRAP assay, when compared to peels from various other tropical fruits such as pineapple, papaya, passion fruit, banana, melon, and watermelon.

Table 5 presents different values depending on the technique used to assess the antioxidant capacity, with ABTS exhibiting the highest value (1006.21 μmol TE/g peel dw). Upon conducting a comparison of antioxidant activity methods, it was observed that the FRAP method exhibited a 1.78-fold increase in activity as compared to the DPPH method. This discrepancy since the reduction procedures are divergent for each method being the main cause of the disparity between them. For instance, the DPPH method bases on the content of phenolic compounds by measuring the reduction of molybdenum/tungsten salts by phenolic groups. The FRAP methodology bases on the reduction of the antioxidant de Fe³⁺ to Fe²⁺. The method ABTS ⁺ bases on the quantification of the discoloration of the radical ABTS ⁺, resulting from its interaction with hydrogen or electron donating species. These findings suggest that the radical structure, reaction processes, and types of phenols may influence the antioxidant efficacy of avocado extracts. This study provides new information on the high antioxidant capacity of ethanol extracts from avocado Hass peels at two distinct stages of maturity. Since the ethanolic extract of UA presents high antioxidant properties (ABTS, FRAP, DPPH) which makes this attribute interesting to the food and pharmaceutical industry.

3.5. Comparison of the total content of phenolic compounds in unripe and ripe avocado peels

Figure 3 shows the profile of phenolic compounds found in UA and RA peels, and Table 6 lists the peak properties (phenolic compound type, molecular formula and mass spectral data) of the nine compounds that were discovered by comparison of their retention time (RT). All phenolic substances showed statistically significant differences (p < 0.05) between UA and RA. Three acids were detected; peak 1 gallic acid (RT = 5.66 min), peak 4 chlorogenic acid (RT = 15.77 min) and peak 6 syringic acid (RT = 17.70 min). Chlorogenic acid has also been identified by Martínez-Gutiérrez (2023) in ethanol extracts of avocado peels with a value of 7.2 ± 0.3 mg/100 g d.m, the aforementioned value is lower than that found in the present investigation for AU with 8.37 mg/100 g.d.m. Additionally, three hydroxybenzoic acids were also found, peak 2 with RT = 9.15 was characterized as 3,4-dihydroxybenzoic acid, peak 5 vanillic acid (RT = 16.147 min). Moreover, vanillin, identified as a monohydroxybenzoic acid, was found in peak 7 with a retention time of 18.85 min. The presence of vanillin was also reported by De la Torre-Carbot et al. (2005) in avocado oil. Two hydroxycinnamic acids were detected in peak 8 ferulic acid (RT = 23.69 min) and in peak 9, 2-hydroxycinnamic acid (RT = 28.30 min). These last two phenolic acids have not been previously described in ethanol extracts of Hass avocado peels.

Figure 3

In peak 3 (Table 6; Figure 3) was founded 4-hydroxyphenylacetic acid (RT = 13.20 min); it is a monocarboxylic acetic acid in which one of the methyl hydrogens is substituted by a 4-hydroxyphenyl group. This acid is the major phenolic compound present in both UA and RA with 3,257,86 and 2624.39 mg/Kg, respectively. The 4-hydroxyphenylacetic acid is used to treat lung diseases, and it is used as an inhibitor to alleviate hypoxia and hypertonicity (Ng et al., 2003; Liu et al., 2014), due to the high antioxidant capacity that can decrease free radicals and the high concentration of hydroxyl groups it produces (Kosińska et al., 2012; Zhou et al., 2018). It can also be used as an intermediate for the synthesis of a β-receptor blocking agent (Thakur et al., 2018), as a natural antioxidant and a potential substitute to replace some synthetic antioxidant food additives.

The phenolic chemical profile (chlorogenic acid, gallic acid, 3,4-dihydroxybenzoic acid, syringic acid, vanillin, vanillic acid and ferulic acid) discovered in this study is consistent to other studies that have covered the phenolic profile in avocado peels (De La Torre-Carbot et al., 2005; Figueroa et al., 2018; Martínez-Gutiérrez, 2023). It is noteworthy to acknowledge that a number of compounds, such as 2-hydroxycinnamic acid and 4-hydroxyphenylacetic acid, have been identified for the first time in this research within the ethanolic extract derived from avocado Hass peels. Furthermore, it is crucial to remember that the cultivar., climate conditions, growing region, stage of fruit maturity, precipitation pattern, and fruit genetics collectively have an impact on the composition of phytochemical components found in avocado peels (Araújo et al., 2021).

4. Conclusion

The results showed that, for all tests, ethanol concentration, temperature and S/F ratio significantly (p < 0.05) influenced the GY, TPC, TFC and antioxidant capacity (DPPH) of the extracts obtained from unripe and ripe Hass avocado peel and the unripe avocado peel extracts obtained using 40% ethanol, 49.3°C, S/F ratio (14.3 mL/g) and 60 min exhibited the highest values of TPC (44.24 mg GAE/g peel dw), TFC (786.08 mg QE/g peel dw) and antioxidant capacity against DPPH (564.82 μmTE/g peel dw), ABTS (804.40 μmTE/g peel dw) and FRAP (1006.21 μmTE/g peel dw). Through HPLC-DAD analysis, vanillic acid and 4-hydroxyphenylacetic acid are the main phenolic compounds found in avocado peel extracts. Unripe avocado extract could be a viable candidate to validate its functionality and use in the pharmaceutical, cosmetic industries, as well as to substitute synthetic antioxidants in the food industry due to their significant amounts of TPC, TFC, and antioxidant capacity.

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