Effects of high-pressure processing and conventional thermal processing on enzyme activities, antioxidant properties, and volatile metabolic profiling of “Phulae” pineapple purée
Received
14th October 2025
, Accepted 12th January 2026
First published on 5th February 2026
Abstract
This study investigated the effects of high-pressure processing (HPP) at 400 and 600 MPa (10 min, 25 °C) compared with conventional thermal processing (CTP; 10 min, 80 °C) on the quality of “Phulae” pineapple purée (Ananas comosus L. cv. Phulae). Untreated purée served as the control. HPP effectively preserved key quality parameters of the purée, including total soluble solids (13.5 °Brix) and color (L* 46.6–48.0; b* 21.3–22.0), with only slight deviations from the untreated samples (L* 49.4; b* 24.1). The vitamin C content was higher in the HPP-treated purée (216.9 mg kg−1) than in the CTP-treated purée (167.0 mg kg−1). The antioxidant capacity was enhanced in the HPP-treated purée, particularly with HPP at 400 MPa, with a total phenolic content of 73.8 g gallic acid equivalents/kg fresh weight (FW), 2,2-diphenyl-1-picrylhydrazyl (DPPH) radical scavenging activity of 2.3 mmol Trolox equivalents (TE)/kg FW, and ferric reducing antioxidant power (FRAP) of 4.7 mmol ascorbic acid equivalents/kg FW. 2,2′-Azino-bis-3-ethylbenzothiazoline-6-sulfonic acid (ABTS) radical scavenging activity was the highest in purée treated with HPP at 600 MPa (4.6 g Trolox equivalent antioxidant capacity/kg FW). HPP also preserved enzyme-related activities, including bromelain activity (3441.7–3733.3 casein digestion units/L) and hyaluronidase (HA) inhibition (78.8–79.9%). Moreover, nitric oxide (NO) radical inhibition was significantly reduced in CTP-treated purée, while HPP-treated samples retained higher inhibition levels (47.0 mmol TE per kg FW). Volatile compound analysis identified esters and terpenes, including their various subgroups, as the dominant contributors to the aroma profile. Based on principal component analysis, principal components 1 and 2 explained 60.4% and 25.3% of the total variance, respectively, accounting for a combined 85.7% of the variability in the dataset. HPP-treated purée clustered closely with the untreated purée, indicating a preserved aroma profile. These findings highlight that HPP is a promising non-thermal technique for maintaining the nutritional, functional, and sensory qualities, especially aroma, of fruit-based products.
Sustainability spotlight
High-pressure processing (HPP) is a sustainable, non-thermal alternative to conventional heat treatment for preserving “Phulae” pineapple puree. HPP retained vitamin C, phenolics, antioxidant activity, enzyme function, and natural aroma while reducing nutrient loss and energy consumption. By extending shelf life and minimizing the need for chemical preservatives, HPP supports cleaner production and reduces food waste, enhancing the value of local fruit resources. These outcomes contribute to SDG 2 (Zero Hunger) by improving food quality and nutrition, SDG 12 (Responsible Consumption and Production) through energy-efficient, low-waste processing, and SDG 13 (Climate Action) by promoting lower-carbon food technologies.
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1 Introduction
Pineapple (Ananas comosus L. Merr) is a tropical fruit noted for its sweet and sour flavor. It is an important commercial fruit that comes in a variety of cultivars and types1 from throughout the world. Pineapple contains abundant vitamin C, dietary fiber, bromelain, carotenoid, and phenolic compounds, which provide it with notable antioxidant activity and the ability to reduce the risk of health problems or diseases.2 The “Phulae” pineapple is a geographical indication (GI) product recognized for its sweet, crispy, and aromatic qualities, originates from the Nang-Lae Subdistrict, Chiang Rai province of Thailand and is classified under the Queen pineapple group.3 “Phulae” pineapples are harvested at peak ripeness and are primarily consumed fresh, with some being transported to local and export markets. Processing pineapples into purée adds value by extending shelf life and reducing postharvest losses. The global fruit purée market was valued at approximately USD 5.09 billion in 2024 and is projected to grow at a Compound Annual Growth Rate (CAGR) of 6.7% through 2030, driven by increasing demand for natural and minimally processed ingredients in beverages, bakery products, and infant foods.4 However, CTP can adversely affect sensory quality and degrade nutritional bioactive compounds. In response to consumer preference for clean-label, minimally processed fruit products with high nutritional value, non-thermal technologies such as pulsed ultraviolet light, irradiation, cold plasma, ultrasonication, and ozone treatment have gained increasing attention.5 Among these technologies, HPP is suitable for pineapple purée. Despite its higher cost, HPP ensures microbial safety while better preserving nutritional quality and the unique sensory attributes of “Phulae” pineapple. HPP is a non-thermal pasteurization method that applies high isostatic pressures (100–600 MPa) to inactivate spoilage and pathogenic microorganisms without the need for intense heat.6 Unlike CTP, HPP minimizes nutrient loss and quality deterioration and does not require additional energy for heat generation, making it a more energy-efficient preservation method.7 It has become increasingly popular as consumers seek minimally processed, safe, and wholesome food alternatives.8 In fruit-based products, sensory quality, particularly aroma, is a critical determinant of consumer acceptance. Pineapple aroma is primarily governed by a complex mixture of volatile compounds, including esters, lactones, terpenes, aldehydes, and sulfur-containing compounds, which collectively contribute to its characteristic fruity and sweet flavor profile.9 These volatile compounds are highly sensitive to processing conditions, especially thermal treatments, which can induce volatilization, degradation, or chemical transformation, leading to aroma loss or the formation of off-flavors. Consequently, preserving the native aromatic profile of pineapple during processing remains a significant technological challenge.10 Because HPP does not involve high temperatures, it preserves heat-sensitive nutrients such as vitamins, minerals, and enzymes, and ensures the retention of antioxidants and the integrity of essential fatty acids and bioactive compounds. Additionally, HPP can enhance the bioavailability of certain nutrients, making them more easily absorbed by the body. Previous studies have demonstrated the effectiveness of HPP in retaining bioactive compounds and antioxidant properties in kiwi berry juice, orange juice-milk, and strawberry purée.11–13 A study in pineapple juice treated with HPP at 500 MPa for 10 min retained its original color, antioxidant activity, bioactive compounds, and volatile compounds.14 Such findings highlight the potential of using HPP to process pineapple purée while retaining its nutritional and sensory quality. Overall, the nutritional benefits and functional potential of HPP are of great interest to consumers, researchers, and food manufacturers, as this non-thermal technology holds strong potential for preserving health-promoting compounds while ensuring food safety and quality.
The objective of this study was to evaluate the impact of HPP at two pressures (400 and 600 MPa) and CTP on the quality, enzyme activities, antioxidant properties, and volatile metabolic profiling of “Phulae” pineapple purée. Comprehensive analyses were conducted to evaluate changes in bioactive compounds (such as vitamin C and total polyphenols), antioxidant activity (including 2,2-diphenyl-1-picrylhydrazyl [DPPH], 2,2′-azino-bis-3-ethylbenzothiazoline-6-sulfonic acid [ABTS], and nitric oxide [NO] radical scavenging assays; the ferric reducing antioxidant power [FRAP] assay; and the oxygen radical absorbance capacity [ORAC] assay), enzyme activities (bromelain and hyaluronidase [HA]), and volatile compound profiles. These findings may help guide the selection of optimal processing technologies for maintaining both nutritional and sensory qualities in fruit-based products.
2 Materials and methods
2.1 Materials
“Phulae” pineapples were harvested at full maturity (i.e., with total soluble solids [TSS] of 13–15 °Brix) from the same orchard in Nang-Lae District, Chiang Rai Province, Thailand (19.95°N, 99.87°E, 390 m above sea level).
2.2 Chemicals
All chemicals and reagents used in this study were of analytical grade, unless otherwise specified. Standards and solvents, including ascorbic acid, the Folin–Ciocalteu phenol reagent, gallic acid, DPPH, Trolox (6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid), and 2,4,6-tris(2-pyridyl)-s-triazine (TPTZ), among others, were purchased from Sigma-Aldrich (St. Louis, MO, USA). Methanol, glacial acetic acid, and other solvents were purchased from RCI Labscan (Bangkok, Thailand). Distilled water was used throughout the experiments. All other chemicals were obtained from KemAus and QReC and used without further purification.
2.3 “Phulae” pineapple purée preparation
Fresh “Phulae” pineapples were washed with tap water, manually peeled, and cut into small pieces. To minimize enzymatic browning, the fruits were kept chilled (4 ± 2 °C) and processed rapidly. The sliced fruit was blended at 38
000 rpm for 30 s (Viva Collection HR2088/91, Philips, China). The purée (80 mL) was immediately packed into 100 mL screw-cap PET spouted pouches (8 × 12 cm) for further experimentation.
2.4 HPP
Eighty milliliters of purée was packed into a 100 mL screw-cap polyethylene terephthalate (PET) plastic spouted pouch (8 × 12 cm) and treated at 400 or 600 MPa for 10 min in a HPP apparatus (Bao Tou KeFa High Pressure Technology Co., Ltd, Baotou, China) with a capacity of 3.0 L at room temperature (25 °C). The purée were subjected to each HPP treatment. The fluid that transmitted pressure in this investigation was reverse osmosis water; the time spent applying or releasing pressure was not included in the treatment duration. The treated “Phulae” pineapple purée was analyzed immediately, with remaining samples stored at −20 °C until use.
2.5 CTP
There were two controls in this study: untreated purée and purée subjected to CTP at 80 ± 5 °C for 10 min. This condition was established based on our previous research and a preliminary study, which identified them as optimal for achieving consistent microbial inactivation and enzymatic stability.2 The purée was prepared for CTP. First, the purée was heated to 80 °C and held at that temperature for 10 min, then immediately cooled in an ice-water bath to stop the reaction. Subsequently, 80 mL of purée was packed into a 100 mL screw-cap PET plastic spouted pouch (8 × 12 cm). The treated “Phulae” pineapple purée was analyzed immediately, with the remaining samples stored at −20 °C until use.
2.6 Determination of physicochemical properties
2.6.1 Measurements of color parameters. The color parameters of “Phulae” pineapple purée were measured using a colorimeter (CM-600d, Konica Minolta, Tokyo, Japan). Samples (5 mL) were transferred into optically clear polypropylene (PP) bags (7.62 × 12.7 cm) and manually spread into a thin, uniform layer. To eliminate surface gloss interference from the packaging material, measurements were performed in Specular Component Excluded (SCE) mode. A white standard board was used for calibration. The color values are expressed based on the CIELAB color space as L*, a*, and b* values, where L* indicates lightness, a* represents the red-green coordinate, and b* denotes the yellow-blue coordinate.
2.6.2 Determination of the pH, total acidity (TA), and TSS. The pH was measured by using a pH meter (Mettler-Toledo, Bangkok, Thailand), which was calibrated with standard buffer solutions (pH 4.0 and 7.0) before use. A digital hand refractometer (ATAGO, Tokyo, Japan) was used to measure TSS (°Brix). TA was measured by using an acidity meter (ATAGO, Tokyo, Japan).
2.7 Determination of bioactive compounds
2.7.1 Determination of the vitamin C content. The vitamin C (ascorbic acid) content was calculated with slight modifications according to a previous study.15 Each sample was homogenized in a solution of 5% meta-phosphoric acid, followed by centrifugation at 12
000×g and 4 °C for 15 min. The supernatant was filtered through Whatman no. 4 filter paper. Four milliliters of the extracted sample was combined with 2 mL of 0.02% indophenol, 4 mL of 2% thiourea, and 2 mL of 2% 2, 4-dinitrophenylhydrazine solution; this mixture was incubated at 37 °C for 3 h. Next, 1 mL of 85% H2SO4 was added, and the absorbance at 540 nm was measured using a microplate reader (Multiskan Go, Thermo Fisher Scientific, Tokyo, Japan). The data are presented as mg ascorbic/kg extract.
2.7.2 Determination of the total phenolic content (TPC). The TPC was determined based on a published colorimetric assay that uses the Folin–Ciocalteu phenol reagent,16 with some modifications. One gram of the sample extract was diluted in 9 mL of distilled water; then, 1250 µL of the diluted solution was transferred to tubes containing an equal volume of 10% (v/v) Folin–Ciocalteu reagent. Subsequently, 1000 µL of 7.5% (w/v) sodium carbonate solution was added, and the mixture was agitated. The samples were incubated at room temperature for 60 min. Then, the absorbance at 765 nm was measured using a microplate reader (Multiskan Go, Thermo Fisher Scientific, Tokyo, Japan). The polyphenol concentration in samples was determined using a standard curve of gallic acid with a range of 20–100 µg mL−1. The TPC is presented as grams of gallic acid equivalents (GAE)/kg fresh weight (FW).
2.7.3 DPPH radical scavenging assay. The DPPH radical scavenging assay was performed as described previously.17 One gram of the sample was diluted in 19 mL of distilled water. Fifty microliters of the diluted extract was mixed with 1950 µL of 60 µM DPPH radical in methanol. The reaction was vortexed and incubated at room temperature in the dark for 30 min. Then, the absorbance at 517 nm was measured using a microplate reader (Multiskan Go, Thermo Fisher Scientific, Tokyo, Japan), with methanol as a blank. The control and standard were subjected to the same procedures as the sample except that, for the control, only distilled water was added and, for the standard, the extract was replaced with 0–500 µM Trolox. The percentage inhibition was calculated from the absorbance of the control (Ac) and the sample (As). The calibration curve was prepared with the Trolox concentration (µM) and percent inhibition. The DPPH radical scavenging activity is expressed as mmol TE per kg FW.
2.7.4 FRAP assay. The FRAP assay was performed as described in a previous publication.18 Four-hundred microliters of the sample was mixed with 2.6 mL of FRAP solution, which was prepared by mixing 300 mM acetate buffer (pH 3.6), 10 mM TPTZ in 40 mM HCl, and 20 mM FeCl3 in a ratio of 10
:
1
:
1 (v/v/v). The mixture was incubated at 37 °C for 30 min. Then, the absorbance at 595 nm was measured using a microplate reader (Multiskan Go, Thermo Fisher Scientific, Tokyo, Japan). Ferrous sulfate equivalent was used as a standard, and distilled water served as the blank.
2.7.5 ABTS radical scavenging assay. The ABTS radical scavenging assay was performed as described previously,19 with slight modifications. Two stock solutions, 7.4 mM ABTS˙+ and 2.6 mM potassium persulfate were combined in equal parts and incubated at room temperature for 12 h in the dark to generate the working solution. This solution was prepared fresh prior to each test. The absorbance of the working solution at 734 nm was measured using a spectrophotometer, and the solution was diluted to reach an absorbance of 1.17 ± 0.02. Next, 1 mL of the working solution was mixed with 60 mL of methanol. For the assay, 150 µL of the pineapple purée was mixed with 2850 µL of the working solution. The mixture was incubated in the dark for 2 h and then measured. The absorbance was measured at 734 nm using a microplate reader (Multiskan Go, Thermo Fisher Scientific, Tokyo, Japan). A standard curve was prepared with Trolox; it was linear in the concentration range of 25–600 mM. If the sample returned an absorbance outside of this range, it was diluted so that it fell within the linear range. The ABTS radical scavenging activity is expressed as Trolox equivalents (TE)/kg FW.
2.7.6 ORAC assay. The ORAC assay was performed as published previously,20,21 with some modifications. Briefly, a stock fluorescein solution (Stock #1) was prepared by dissolving 0.0225 g of fluorescein in 50 mL of 0.075 M phosphate buffer (pH 7.0). A secondary stock solution was obtained by diluting 50 µL of Stock #1 in 10 mL of phosphate buffer. Subsequently, 320 µL of the secondary solution was diluted in 20 mL of phosphate buffer, from which 200 µL was dispensed into each well of a black 96-well plate. Thus, the final fluorescein concentration was 14 µM per well, equivalent to 7.5 nmol of fluorescein. For the assay, 20 µL of standard Trolox (6.25, 12.5, 25, and 50 µM) was prepared in 0.075 M phosphate buffer (pH 7.0) and added to the designated wells; the plate was incubated at 37 °C for 10 min. Then, 75 µL of AAPH (2,2′-Azo-bis(2-amidinopropane) dihydrochloride) was added to each well, and the plate was incubated at 37 °C for 2 h. The fluorescence intensity at 37 °C was recorded using a SpectraMax mini plate reader equipped with SoftMax Pro 7.2 software (Molecular Devices San Jose, California, United States). Readings were taken at 485 nm (excitation) and 535 nm (emission) every 2 min for a total duration of 90 min. The area under the curve (AUC) was determined from the fluorescence intensity data using the following equation:
ORAC is expressed as mmol TE per kg sample.
2.8 NO radical scavenging assay
The NO radical scavenging activity was analyzed as published22 previously with some modifications. In brief, NO radicals are generated from the interaction between oxygen in the sample and aqueous sodium nitroprusside (SNP) and quantified via the Griess–Illosvoy reaction, which measures nitrite ions (NO2−). First, 800 µL of 10 mM SNP and 40 µL of diluted purée were mixed and incubated at room temperature for 150 min. Then, 200 µL of the solution was transferred to a fresh tube, and 400 µL of 0.33% sulfanilamide in 20% glacial acetic acid was added; the mixture was incubated at room temperature for 5 min. Next, 400 µL of 0.1% N-(1-naphthyl) ethylene-diamine dihydrochloride was added, and the mixture was incubated at room temperature for 30 min. The absorbance at 540 nm was measured with a microplate reader (Multiskan Go, Thermo Fisher Scientific, Tokyo, Japan). The standard curve was generated from Trolox (0.2–0.5 mg mL−1). The results are presented as mmol TE per kg FW.
2.9 Determination of HA inhibition
HA inhibition was measured as described in previous publications.23,24 One hundred microliters of HA (type IV-S, derived from bovine testes; Sigma-Aldrich) was diluted in buffer to a final concentration of 5 mg mL−1 and incubated at 37 °C. Subsequently, 200 µL of compound 48/80 (Sigma-Aldrich) was added to the buffer at a final concentration of 0.5 mg mL−1 and incubated at 37 °C for 20 min. Freeze-dried samples were reconstituted in distilled water, vortexed, and centrifuged at 10
000 rpm for 10 min; added to the reaction mixture; and incubated at 37 °C for 20 min. Hyaluronic acid sodium salt (extracted from rooster comb; Wako, Osaka, Japan) was added to a final concentration of 0.4 mg mL−1, and the mixture was incubated at 37 °C for 40 min. To terminate the reaction, 200 µL of 0.4 M NaOH and 200 µL of borate buffer (pH 8.0) were added, and the mixture was boiled in water for 3 min before being rapidly cooled on ice. Subsequently, 3000 µL of p-dimethylaminobenzaldehyde (Wako) solution was introduced, followed by incubation at 37 °C for 20 min. The absorbance at 585 nm was measured using a SpectraMax mini plate reader equipped with SoftMax Pro 7.2 software (Molecular Devices San Jose, California, United States), and HA inhibition (%) was calculated.
2.10 Determination of enzyme activity
Bromelain activity was determined by quantifying the low-molecular-weight digestion products, which are soluble in trichloroacetic acid (TCA), resulting from its proteolytic action. The assay was performed based on a previous publication.25 It was conducted using 5 mL of 0.75% casein prepared in anhydrous disodium phosphate buffer (50 mM, pH 7, with the pH adjusted by gradually adding 0.1 N HCl). The solution was preincubated at 37 °C for 10 min before introducing the enzyme, which had been diluted to a final volume of 1 mL using an activating buffer (20.7 mM L-cysteine in 6 mM disodium ethylenediaminetetraacetic acid, pH 7). The proteolytic reaction was terminated after 10 min by adding 5 mL of 30% (w/v) TCA, and the mixture was incubated at 37 °C for 30 min. Then, the solution was cooled to room temperature and filtered twice using Whatman no. 42 filter paper. The absorbance of the resulting filtrate was measured at 280 nm using an ultraviolet-visible (UV-Vis) spectrophotometer (U-2900, Hitachi High-Technologies Corporation, Tokyo, Japan). The enzymatic activity was quantified based on a standard calibration curve of absorbance versus the tyrosine concentration; it is presented as casein digestion units (CDU) per liter.
2.11 Determination of volatile compounds
Headspace solid phase microextraction (SPME) combined with gas chromatography-mass spectrometry (GC-MS) was performed as described previously,14 with slight modifications, to extract and analyze the volatile compounds. Five grams of pineapple purée was added to 20 mL headspace glass vials. The volatile compounds present in the headspace were absorbed to an SPME fiber (Supelco, Bellefonte, PA, USA) coated with 50/30 µm divinylbenzene/carboxen/polydimethylsiloxane (DVB/CAR/PDMS) for 30 min at 40 °C. The gases were extracted and then thermally desorbed in the injection inlet of a GC-MS system (7890A/5975C, Agilent Technologies Co., Ltd, Santa Clara, CA, USA) for 6 min at 270 °C. The samples were injected in splitless mode. A HP-5MS capillary (30 m × 0.25 mm × 0.25 µm; Agilent Technologies) was used to separate volatile chemicals. The carrier gas was helium, with a constant flow rate of 1.0 mL min−1. The oven temperature was initially set at 40 °C for 2 min, increased to 220 °C at 5 °C min−1, increased to 260 °C at 10 °C min−1, and then maintained at 260 °C for 2 min. The mass spectra were obtained using electron impact ionization mode, with the ion source operating at 230 °C. ChemStation software (Agilent Technologies) was used for peak area integration and to visualize chromatograms. n-Alkanes (C8–C20) obtained from Sigma–Aldrich, Germany were also run. The volatile components were tentatively identified by comparing the mass spectra of the samples with the retention index (RI), authentic references, and the data system library (NIST 20). The RI was calculated from the following formula:
where tR, tRz, and tR(z + 1) are the elution time of the unknown compound, the n-alkane that eluted just before the unknown compound, and the n-alkane that eluted just after the unknown compound, respectively; and z is the number of carbon atoms in pre-eluted hydrocarbon RI.
2.12 Statistical analysis
Data are presented as the mean ± standard deviation (SD) of three independent batches, with each analysis performed in triplicate. The data were also subjected to analysis of variance (ANOVA) followed by Duncan's multiple range tests using IBM SPSS Statistics 20.0 (IBM Corp., Armonk, NY, USA). P < 0.05 was considered to indicate a statistically significant difference. The principal component analysis (PCA) was calculated for volatile composition. The concentration data were log-transformed and Pareto-scaled before being analyzed with MetaboAnalyst 6.0 (https://www.metaboanalyst.ca, accessed on August 12, 2024).
3 Results and discussion
3.1 Effect of HPP on physicochemical properties
Untreated “Phulae” pineapple purée had a pH of 3.96 ± 0.01, TSS of 13.54 ± 0.01 °Brix, and TA of 0.44%, consistent with data from the literature.26 These baseline values were used to assess the impact of HPP and CTP on “Phulae” pineapple purée. The TSS of the untreated control and HPP-treated purées did not differ significantly (P > 0.05) (Table 1). Moreover, there was no significant difference between HPP treatment at 400 and 600 MPa. These findings suggest that HPP may not significantly impact soluble solids, similar to the findings from passion fruit purée.27 However, TSS and TA increased significantly (P < 0.05) in the CTP-treated purées compared to the untreated purées (Table 1). The increase in TSS during CTP was primarily attributed to the dehydration of the purée. The thermal energy applied during CTP likely facilitated moisture evaporation, thereby concentrating the soluble solids.28 This physical concentration effect is a dominant factor, although it may be partially supplemented by biochemical reactions, such as the hydrolysis of complex polysaccharides into soluble sugars during heating.29 This explanation is further supported by a comparison with mango smoothies, where TSS and pH remained stable under HPP. The stability observed in the mango study highlights that without dehydration, the intrinsic chemical changes in such fruit matrices are insufficient to significantly alter TSS, confirming that the elevation observed in this study is a specific result of the dehydration effect inherent to the CTP process.30 The pH decreased significantly (P < 0.05) in the CTP-treated and HPP-treated purées compared with the untreated control purées. Finally, the TA tended to increase in all treated purées compared with the untreated control purée. This increase could be due to the disruption of cellular membranes by heat and/or high pressure, leading to the release of organic acids from within the cells, which in turn increases the acid concentration and slightly decreases the pH.31
Table 1 Changes in pH, TSS, TA, and color parameters (L*, a*, b*) of “Phulae” pineapple purée treated by CTP and HPPa
| Treatments |
pH |
TSS (°Brix) |
TA |
L* |
a* |
b* |
| Different letters in the same column indicate a significant difference (p < 0.05) among treatments. CTP, conventional thermal processing at 80 °C for 10 min; HPP-400, high-pressure processing at 400 MPa for 10 min; HPP-600, high-pressure processing at 600 MPa for 10 min; TA, total acidity; TSS, total soluble solids; L*, lightness; a*, redness; b*, yellowness. |
| Untreated |
3.96 ± 0.01a |
13.54 ± 0.11b |
0.44 ± 0.02c |
49.41 ± 0.39a |
−2.41 ± 0.23a |
24.11 ± 1.10a |
| CTP |
3.94 ± 0.01b |
14.36 ± 0.23a |
0.51 ± 0.03a |
45.08 ± 0.78d |
−2.34 ± 0.21a |
19.69 ± 0.89c |
| HPP 400 |
3.92 ± 0.01c |
13.51 ± 0.12b |
0.48 ± 0.01b |
46.63 ± 0.81c |
−2.40 ± 0.21a |
22.04 ± 0.87b |
| HPP 600 |
3.92 ± 0.01c |
13.61 ± 0.14b |
0.46 ± 0.00b |
48.02 ± 0.83b |
−2.71 ± 0.15b |
21.27 ± 0.90b |
Regarding the color parameters, treatment with HPP, especially at 600 MPa, minimized color changes in the pineapple purée compared with CTP (Fig. 1). HPP provided better preservation of the lightness (L*) and yellowness (b*) values, indicating less color alteration. This effect may be partly attributed to the high sugar content of pineapple purée. During thermal processing, sugars promote non-enzymatic browning via caramelization and Maillard reactions. Furthermore, in non-thermal processes like HPP, high sugar concentrations can exert a protective effect on browning-related enzymes.32 Our finding is consistent with the results observed for strawberry and blackberry purées,33 where HPP also resulted in minimal color deviations.34 This result is also similar to a previous study that showed that HPP retained the original color of mango smoothies.30 On the other hand, CTP caused more pronounced color shifts in the purée, particularly a reduction in b* values, signifying a shift toward a more yellow hue. This was likely due to the alteration of pigments by heat and the precipitation of insoluble particles.2
 |
| | Fig. 1 The appearance of the purées after the treatments. CTP, conventional thermal processing at 80 °C for 10 min; HPP-400, high-pressure processing at 400 MPa for 10 min; HPP-600, high-pressure processing at 600 MPa for 10 min. | |
3.2 Effect of HPP on bioactive compounds
3.2.1 Effect of HPP on the vitamin C content. The vitamin C content of the untreated purée was 216.9 mg kg−1 FW, consistent with values previously reported for “Phulae” pineapple.26 Compared with the untreated treatment, vitamin C decreased by 11.5% to 191.9 mg kg−1 FW after HPP and by 23.0% to 167.0 mg kg−1 FW after CTP (Fig. 2). Since ascorbic acid is highly thermolabile, the application of heat during CTP accelerates its oxidative degradation into dehydroascorbic acid, which can further irreversibly hydrolyze into 2,3-diketogulonic acid, leading to a loss of nutritional value.35 In contrast, HPP limits this kinetic degradation by operating at lower temperatures. The slight loss observed during HPP may be attributed to the presence of residual dissolved oxygen in the purée or the activation of oxidative enzymes like ascorbate oxidase during the initial stages of processing. These results align with previous findings where HPP better preserved the nutritional integrity including vitamin C of fruit products compared to traditional pasteurization.36
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| | Fig. 2 The effects of different processing on (A) the vitamin C content, (B) the total phenolic content, (C) DPPH radical scavenging activity, (D) FRAP, (E) ABTS radical scavenging activity, and (F) ORAC in “Phulae” pineapple purée. ABTS, 2,2′-azino-bis-3-ethylbenzothiazoline-6-sulfonic acid; AAE, ascorbic acid equivalents; CTP, conventional thermal processing at 80 °C for 10 min; DPPH, 2,2-diphenyl-1-picrylhydrazyl; FW, fresh weight; GAE, gallic acid equivalents; HPP-400, high-pressure processing at 400 MPa for 10 min; HPP-600, high-pressure processing at 600 MPa for 10 min; ORAC, oxygen radical absorbance capacity; TE, Trolox equivalents. | |
3.2.2 Effect of HPP on the TPC and DPPH radical scavenging. Treatment with HPP at 400 MPa significantly increased the TPC (73.78 g GAE per kg) and the DPPH radical scavenging activity (2.29 mmol TE per kg FW) compared with the untreated purée. After CTP, the TPC decreased but the DPPH radical scavenging activity increased compared with the untreated purée. It is possible that heat treatment led to the formation of new antioxidant compounds, like those from the Maillard reaction, or helped release certain bound antioxidants. Antioxidant activity does not just depend on how many phenolic compounds are present, but also on the types of antioxidants and how active they are.37 The higher TPC and DPPH radical scavenging activity indicates that this treatment better preserves the antioxidant capacity, consistent with previous findings.14,16 In mandarin juice treated with HPP, there was enhanced retention of carotenoids, flavonoids, ascorbic acid, total polyphenols, and antioxidant capacity as measured by FRAP in the bioaccessible fractions.38 These results highlight HPP as a promising alternative to CTP for preserving the nutritional and antioxidant properties of pineapple purée.
3.2.3 Effect of HPP on FRAP. FRAP was significantly higher (P < 0.05) in the HPP-treated pineapple purée compared with the untreated and CTP-treated purées. There was little difference between the purées subjected to HPP at 400 or 600 MPa, which suggests that increasing the pressure beyond 400 MPa might not boost antioxidant activity. The increased antioxidant capacity in HPP samples is likely due to the pressure-induced release of bound phenolic compounds from the fruit matrix, which enhances the ability to reduce ferric ions (Fe3+) to ferrous ions (Fe2+).18 This shift in antioxidant potential is significant because it shows that HPP is more than a preservation method; it also serves as a functional enhancement tool. The reduced FRAP in the CTP-treated purée compared with the untreated purée highlights how thermal processing can negatively impact bioactive compounds. While HPP facilitates the release of antioxidants by disrupting cellular compartments without high thermal energy, CTP causes the oxidative degradation of heat-labile molecules like vitamin C and certain flavonoids, which are major contributors to the reducing power of pineapple.29
3.2.4 Effect of HPP on ABTS radical scavenging activity. ABTS radical scavenging activity was significantly higher (P < 0.05) in purée treated with HPP at 600 MPa (4.55 g TE per kg FW) compared to all other treatments, including the untreated one. This enhancement is primarily attributed to the high-pressure-induced permeabilization of plant cell walls and membranes, which increased the mobility and release of matrix-bound phenolic compounds. HPP at 600 MPa provides sufficient mechanical energy to disrupt the pectin-cellulose network, thereby increasing the extractability of sequestered antioxidants.32 The lower ABTS radical scavenging in the other sample may be due to the limited release of phenolic compounds or the degradation of existing antioxidants. These findings are consistent with a previous study that demonstrated the effectiveness of HPP in enhancing the overall antioxidant capacity of various fruits and vegetables.39
3.2.5 Effect of HPP on ORAC. The ORAC ranged from 25.5 to 36.6 mmol TE per kg sample across all treatments, with no significant difference (P > 0.05). Thus, neither CTP nor HPP had a major impact on the ORAC. These findings are consistent with previous studies reporting that pineapple contains relatively stable antioxidants, including phenolic compounds and vitamin C, which may be moderately resistant to processing-induced degradation.39 Moreover, while heat can degrade some sensitive antioxidants, it may also enhance the extractability of bound phenolic compounds, potentially balancing out losses. Similarly, HPP is known to preserve antioxidant activity in many fruits due to minimal thermal damage and short processing times.40
3.3 Effect of HPP on NO radical scavenging activity
The NO radical scavenging activity did not differ significantly (P > 0.05) between the untreated purée (47.0 mmol TE per kg FW) and the HPP-treated purée (47.0 mmol TE per kg FW), indicating that HPP preserves the compounds responsible for NO scavenging. In contrast, CTP-treated purée showed the lowest activity (27.4 mmol TE per kg FW; Fig. 3A), possibly due to the heat-induced degradation of bioactive compounds. These assays are commonly used as preliminary indicators linked to inflammatory pathways; however, they are based on in vitro chemical measurements and do not directly reflect physiological anti-inflammatory effects in vivo. This decline is likely attributed to the thermal degradation of heat-sensitive bioactive compounds, such as bromelain and phenolic antioxidants, which possess the functional groups necessary for electron or hydrogen atom transfer to NO radicals.41 Consistently, previous studies have demonstrated that HPP retains the stability of phenolic acids and vitamin C, which are key contributors to the NO scavenging capacity in fruit matrices.14 The lack of significant change in NO radical scavenging activity for HPP supports the notion that HPP provides a gentler processing mechanism compared with heat treatment, and thus it may preserve these anti-inflammatory compounds.
 |
| | Fig. 3 The effects of different processing on (A) NO radical scavenging activity, (B) HA inhibition, and (C) bromelain activity in “Phulae” pineapple purée. CDU, casein digestion units; CTP, conventional thermal processing at 80 °C for 10 min; FW, fresh weight; HA, hyaluronidase; HPP-400, high-pressure processing at 400 MPa for 10 min; HPP-600, high-pressure processing at 600 MPa for 10 min; NO, nitric oxide; TE, Trolox equivalents. | |
3.4 Effect of HPP on HA inhibition
The untreated purée showed 77.1% HA inhibition. Following CTP treatment, this activity was significantly (P < 0.05) reduced to 58.0% (Fig. 3B). This substantial decline in inhibitory potential is largely attributed to the thermal sensitivity of bromelain and other bioactive proteases, where heat-induced unfolding of the protein structure disrupts the active sites responsible for HA interaction.42 In contrast, HPP at 400 and 600 MPa preserved HA inhibition effectively (78.8–79.9%), showing no significant degradation compared to the untreated. Bromelain is known for its ability to inhibit HA activity, which plays a role in its anti-inflammatory and anti-metastatic effects.43 Heat can denature bromelain, significantly reducing its bioactivity,42 whereas HPP has been reported to preserve its molecular conformation and enzymatic function.44 These findings are consistent with previous studies emphasizing the advantages of HPP over heat treatments in retaining enzyme activity and biofunctional properties in fruits.45,46 They suggest that HPP, a non-thermal preservation technique, better retains the functional integrity of bioactive compounds responsible for HA inhibition, likely due to minimal structural damage to proteins and enzymes.
3.5 Effect of HPP on enzyme activity
Bromelain activity in untreated purée was 3483.3 CDU/L, serving as the baseline for this study. Following CTP treatment, activity declined significantly (P < 0.05) to 2025 CDU/L, representing a loss of nearly 40% compared to the control (Fig. 3C). This reduction is primarily attributed to the thermal denaturation of bromelain's protein structure, where high temperatures disrupt the hydrogen bonds and hydrophobic interactions necessary for retaining its active site conformation.44 In contrast, HPP-treated samples (3441.7–3733.3 CDU/L) showed no significant difference from the untreated samples, highlighting HPP's ability to preserve enzymatic function. The stability of bromelain under high pressure can be explained by the fact that HPP primarily affects large molecular weight components through volume contraction but often leaves low-energy covalent bonds intact, thus retaining the enzyme's catalytic integrity.44 One study indicated that HPP treatment can significantly enhance the in vivo fibrinolytic activity of fruit-derived bromelain, thereby increasing the functional value and market potential of pineapple-based products.47 When interpreted alongside HA inhibition data, it becomes evident that the retention of bromelain activity under HPP conditions directly contributes to the preservation of pineapple's bioactive potential.
3.6 Effect of HPP on volatile compounds
Principal component analysis (PCA) was performed to examine the effects of treatments on the volatile compound composition. As illustrated in the score plot (Fig. 4) and the corresponding biplot (Fig. 5), the first two principal components (PC1 and PC2) accounted for 60.4% and 25.2% of the total variance, respectively. The samples were categorized based on their volatile profiles. The PCA revealed significant differences between the treatments, indicating that the processing methods impacted the aroma profile of the pineapple purée (Table 2). A total of 18 volatile compounds were detected in the pineapple purée, predominantly esters and terpenes. These findings are consistent with a previous study that reported esters are the most common volatile compounds in pineapple.9 The untreated purée (green circles) exhibited the highest concentration of methyl propionate (35.2%), a compound responsible for sweet, rum-like, fruity odors. This is consistent with consumer preferences for fresh pineapple flavor.32 In contrast, the CTP-treated purée (red circles) showed a marked reduction in methyl propionate (4.5%) and a substantial increase in methyl 2-methylbutanoate (59.0%). The latter ester has an ethereal, fruity, and pineapple-like aroma. The change in volatile compounds indicates that although CTP can boost some pleasant fruity aromas, it may also reduce others, which could affect the overall flavor profile of the pineapple purée.
 |
| | Fig. 4 The score plot obtained from principal component analysis. CTP, conventional thermal processing at 80 °C for 10 min; HPP-400, high-pressure processing at 400 MPa for 10 min; HPP-600, high-pressure processing at 600 MPa for 10 min. | |
 |
| | Fig. 5 The biplot obtained from principal component analysis (PCA), with 18 metabolites labeled 1–18. See Table 2 for the identity of each metabolite. CTP, conventional thermal processing at 80 °C for 10 min; HPP-400, high-pressure processing at 400 MPa for 10 min; HPP-600, high-pressure processing at 600 MPa for 10 min. | |
Table 2 Identification of volatile compounds in “Phulae” pineapple puréea
| No. |
Compounds |
Odor description |
Classification |
CAS no. |
RI |
Peak area (%) |
| Untreated |
CTP |
HPP 400 MPa |
HPP 600 MPa |
| CAS no., chemical abstracts service number; CTP, conventional thermal processing; HPP, high-pressure processing; RI, retention index. |
| 1 |
Methyl propionate |
Sweet, rum-like, fruity |
Ester |
554-12-1 |
611 |
35.24 |
4.54 |
19.06 |
36.40 |
| 2 |
Isovaleric acid |
Sweaty, cheesy, rancid |
Carboxylic acid |
90 435-18-0 |
651 |
3.31 |
1.58 |
0.85 |
0.10 |
| 3 |
Butanoic acid, 2-methyl-, methyl ester |
Ethereal, fruity, tutti-frutti, pineapple-like |
Ester |
868-57-5 |
689 |
36.97 |
59.02 |
45.43 |
23.88 |
| 4 |
Butanoic acid, 2-methyl-, ethyl ester |
Fruity, juicy, tropical |
Ester |
7452-79-1 |
856 |
1.92 |
0.03 |
2.08 |
0.80 |
| 5 |
Hexanoic acid, methyl ester |
Fruity, pineapple-like |
Ester |
106-70-7 |
931 |
0.43 |
— |
— |
— |
| 6 |
Beta-myrcene |
Earthy, spicy, citrusy, piney, evergreen |
Monoterpene |
123-35-3 |
998 |
0.47 |
— |
0.75 |
0.75 |
| 7 |
1-Pentanone, 1-(4-methylphenyl) |
Raspberry-like |
Ketone |
1671-77-8 |
1033 |
0.04 |
— |
— |
— |
| 8 |
D-limonene |
Citrusy |
Monoterpene |
5989-27-5 |
1036 |
0.53 |
0.66 |
0.93 |
0.85 |
| 9 |
3-Carene |
Sweet, pungent |
Monoterpene |
13 466-78-9 |
1055 |
4.48 |
6.84 |
8.66 |
9.23 |
| 10 |
Beta-ocimene |
Floral, green, herbal |
Monoterpene |
13 877-91-3 |
1056 |
8.78 |
14.35 |
19.29 |
18.80 |
| 11 |
Alpha-phellandrene |
Pepper, mint, and fruity |
Monoterpene |
99-83-2 |
1067 |
0.03 |
— |
— |
— |
| 12 |
Nonanal |
Rose-orange |
Aldehyde |
124-19-6 |
1112 |
— |
— |
0.56 |
0.63 |
| 13 |
Octanoic acid, methyl ester |
Fruity, orange-like, pineapple-like |
Ester |
111-11-5 |
1123 |
6.30 |
9.93 |
— |
— |
| 14 |
Octanoic acid, ethyl ester |
Fruity, orange-like, pineapple-like |
Ester |
106-32-1 |
1132 |
0.13 |
— |
— |
— |
| 15 |
Isoledene |
Woody, musky |
Terpene |
95 910-36-4 |
1224 |
0.12 |
— |
— |
— |
| 16 |
Decanoic acid, methyl ester |
Fruity, orange-like |
Ester |
110-42-9 |
1233 |
0.04 |
— |
— |
— |
| 17 |
Copaene |
Woody, spicy |
Terpene |
3856-25-5 |
1289 |
1.13 |
1.19 |
— |
— |
| 18 |
Cis-muurola-3,5-diene |
Woody, earthy, herbal |
Terpene |
1 000 365-95-4 |
1297 |
0.03 |
1.85 |
1.64 |
3.06 |
The purée subjected to HPP at 400 MPa (dark blue circles) showed intermediate values for both methyl propionate (19.1%) and methyl 2-methylbutanoate (45.4%), which suggests that HPP at 400 MPa at least partially preserves the pineapple purée aroma profile. In contrast, the purée subjected to HPP at 600 MPa (light blue circles) showed a higher concentration of methyl 2-methyl butanoate (23.9%) but a lower concentration of methyl propionate (36.4%) compared with untreated purée. This indicates that while high pressure (600 MPa) may enhance some fruity aromas, it may not fully retain the original volatile character of the untreated pineapple purée. The HPP treatments also led to the release of monoterpenes, such as β-myrcene and limonene (Table 2), which are associated with citrusy and piney aromas. These compounds were present only in the HPP-treated purée, suggesting that HPP might contribute to a more complex and diverse aroma profile. The biplot reveals a clear separation between treatments based on their volatile profiles. The HPP-treated samples were characterized by a high abundance of fresh-fruity esters, such as methyl octanoate, methyl 2-methylbutanoate, and methyl propionate, which were positioned far from the origin and clustered near the HPP group along PC1. These compounds acted as the primary drivers differentiating HPP samples from the CTP group. “Phulae” pineapple contains around 30 volatile chemicals, including esters, terpenes, aldehydes, ketones, and hydrocarbons. Esters such as hexanoic acid methyl ester, butanoic acid 2-methylmethyl ester, and octanoic acid methyl ester are key components contributing to the pineapple flavor.48 The observed changes in the specific volatile compounds likely contribute to the sensory differences between pineapple purée subjected to the different processing treatments. For example, while HPP can preserve or enhance certain fruity and citrusy aromas, CTP may result in the reduction of desirable volatiles, thus altering the overall aroma profile. Further research into consumer perception of these aroma changes would be valuable to optimize processing techniques to achieve an ideal balance between aroma preservation and shelf-life extension.
4 Conclusion
In conclusion, HPP offers significant advantages over CTP in preserving the overall quality and nutritional integrity of “Phulae” pineapple purée. As a non-thermal technology, HPP more effectively retained key physicochemical properties, including pH, total soluble solids, and color. It also demonstrated superior retention of sensitive nutritional and functional components. Specifically, HPP increased the vitamin C content by approximately 22–25% and bromelain activity by 80–95% compared with CTP, highlighting its effectiveness in preserving thermolabile nutrients and enzymes. Furthermore, antioxidant capacity assessed through FRAP, DPPH, and ABTS radical scavenging assays was significantly improved in HPP-treated purée, especially at higher pressure levels. HPP also helped preserve volatile aromatic compounds, particularly esters and terpenes, which are essential for the fresh and fruity aroma profile of pineapple. HPP-treated purée showed higher in vitro chemical activities, including a 54% increase in NO radical scavenging and a 30% increase in HA inhibition.
The results indicate that HPP is a technical alternative to thermal processing for “Phulae” pineapple purée as it retains the fruit's characteristic bioactive profile and aromatic compounds. These findings provide a basis for the implementation of high-pressure technologies in the production of minimally processed fruit products where retaining natural nutritional value is prioritized. Therefore, further studies using cellular or animal models are recommended to substantiate definitive biological claims, along with investigations into shelf-life stability and long-term bioactivity retention.
Author contributions
Supapich Chalumput: methodology, formal analysis, data curation, writing – original draft, writing – review & editing; Prinya Wongsa, Phunsiri Suthiluk, Daisuke Hamanaka, and Matchima Naradisorn: conceptualization, investigation, project administration, resources, supervision; Sutthiwal Setha: conceptualization, methodology, formal analysis, investigation, writing – review & editing.
Conflicts of interest
There are no conflicts to declare.
Data availability
The authors confirm that the data supporting the findings of this study are available within the article.
Acknowledgements
This research was also supported by Mae Fah Luang University under the National Science, Research, and Innovation Fund (NSRF) 2023 [grant 662A04020]. The authors would like to thank Mae Fah Luang University, Chiang Rai, Thailand, and Kagoshima University, Japan, for providing research facilities. The authors thank Professor Satoru Kondo for his kind advice on manuscript preparation and language editing support.
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