Open Access Article
Samandeep
Kaur
*a,
Vikrant
Singh
b,
Parmjit S.
Panesar
*c and
Harish K.
Chopra
c
aSchool of Engineering and Technology, National Forensic Sciences University, Gandhinagar-382007, Gujarat, India. E-mail: saman95deep@gmail.com
bGraphic Era (Deemed to be University), Dehradun-248002, Uttarakhand, India
cSant Longowal Institute of Engineering and Technology, Longowal-148106, Punjab, India. E-mail: pspanesarrr@yahoo.com
First published on 22nd September 2025
The extraction of dietary fiber (DF) from kinnow by-products offers a valuable opportunity for waste valorization and the development of functional food ingredients. This study compared conventional extraction methods (hot water, ethanol, and alkali extraction) with microwave-assisted extraction (MAE) to evaluate differences in fiber yield and functional, structural, and thermal properties. Among conventional methods, alkali extraction provided the highest fiber recovery, but MAE achieved comparable or higher yields with significantly reduced extraction time and lower chemical input. MAE-extracted dietary fiber exhibited superior functional properties, including water-holding capacity (7.78–9.12 g g−1), oil-holding capacity (4.68–5.36 g g−1), and glucose adsorption capacity (3.55–4.24 mmol g−1), higher than those of fibers obtained via conventional methods. FTIR analysis confirmed that MAE-extracted fibers retained key functional groups, such as hydroxyl, carboxyl, and glycosidic linkages, indicating the preservation of cellulose, hemicellulose, and pectin structures. XRD analysis showed that both peel and pomace fibers exhibited semi-crystalline structures, with pomace fibers showing slightly higher crystallinity, reflecting compositional differences between the two by-products. DSC analysis demonstrated good thermal stability in MAE-extracted fibers, with insoluble dietary fiber (ISDF) exhibiting higher thermal resistance than soluble dietary fiber (SDF). Overall, MAE proved to be a sustainable, efficient alternative for dietary fiber extraction, enhancing functionality while promoting kinnow by-product valorization.
Sustainability spotlightThis study valorizes kinnow peel and pomace, agro-industrial citrus waste, through optimized conventional and microwave-assisted extraction of dietary fiber, contributing to waste reduction and circular bioeconomy. By converting underutilized by-products into high-value functional ingredients, the work promotes sustainable food processing and supports the UN Sustainable Development Goals, particularly SDG 12 (Responsible Consumption and Production) and SDG 3 (Good Health and Well-being). The use of microwave-assisted extraction also emphasizes energy efficiency, aligning with SDG 7 (Affordable and Clean Energy). This research fosters eco-innovation by integrating waste valorization, clean processing, and health-oriented food design. |
Conventional methods such as hot water extraction (HWE), ethanol extraction (EtOH-E), and alkali extraction (NaOH-E) are widely used for extracting dietary fiber from plant materials. Hot water extraction is a simple and commonly applied method; however, it often requires prolonged high temperatures, which can degrade polysaccharides and lower fiber yields and functionality.6 Ethanol extraction aids in separating fiber from soluble sugars but requires large solvent volumes and multiple rinsing steps, limiting its practicality for large-scale operations.7 Alkali extraction, which employs sodium hydroxide to disrupt cell walls and enhance fiber release, often results in higher yields than water or ethanol methods. However, alkali treatment can modify fiber structure and may leave chemical residues, raising concerns for food applications.8 To overcome these limitations, microwave-assisted extraction (MAE) has emerged as a green and sustainable alternative for extracting bioactives and dietary fiber from plant materials. Microwave technology works by inducing dipole rotation in the solvent, leading to rapid volumetric heating that breaks cell walls and enhances solubilization.9 Unlike conventional heating, which relies on surface heat conduction, microwaves penetrate directly into the sample matrix, resulting in uniform and faster heating. This localized heating effect can also increase intracellular pressure, cause cell rupture, and release fiber and bioactive compounds more efficiently.1,10 The effects of microwave processing on various plant materials, particularly grains like barley, oat, millet, chickpea, and soybean, have been extensively studied. These studies have demonstrated that microwave treatment can alter starch crystalline structures, increase gelatinization temperature, and improve thermal stability and edible quality.11,12 Although these findings pertain to starch systems, they illustrate how microwave energy can modify plant carbohydrates in general, including the cellulose, hemicellulose, and pectin fractions that constitute dietary fiber. Such effects could similarly enhance fiber solubilization, conversion of ISDF to SDF, and preservation of functional properties during dietary fiber extraction.
Despite these promising advantages, comparative studies directly evaluating the efficiency, functional properties, and structural integrity of dietary fiber extracted using conventional versus microwave-assisted techniques remain limited, particularly for kinnow peels and pomace. Therefore, this study aims to compare conventional extraction methods (hot water, ethanol, and alkali) with microwave-assisted extraction (MAE) for dietary fiber recovery from kinnow by-products. The comparison will focus on dietary fiber yield, functional, structural, and thermal properties. It is hypothesized that microwave-assisted extraction will enhance dietary fiber recovery while preserving structural integrity and improving functional properties due to its efficient cell wall disruption, reduced thermal degradation, and shorter processing time. By addressing these research gaps, this study contributes to the broader goal of valorizing citrus processing waste into high-value functional ingredients, thereby promoting sustainability and reducing food processing waste.
| Extraction method | Solvent used | Temperature (°C) | Time (min) | Centrifugation (rpm/min) | Advantages | Limitations |
|---|---|---|---|---|---|---|
| Hot water extraction (HWE) | Water | 100 | 5 | 5000/10 | No chemical solvent, simple | High temperature may degrade polysaccharides |
| Ethanol extraction (EtOH-E) | 80% ethanol | Room temp. | ∼10 | 5000/10 | Effective for sugar removal | Requires solvent recovery |
| Alkali extraction (NaOH-E) | NaOH (50 mM) | 45 | 30 | 5000/30 | High fiber yield, breaks cell walls | May alter fiber composition |
| Microwave-assisted extraction (MAE) | Water | 50 | 9 | 5000/15 | Shorter extraction time, better yield | Equipment required |
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10 w/v) and heated at 100 °C for 5 min. The suspension was subsequently centrifuged (5000 rpm, 10 min) to separate the fiber-rich precipitate from the solubilized sugars (glucose, fructose, and sucrose). To ensure complete removal of residual sugars, the precipitate was washed five times with water at 40 °C and centrifuged under the same conditions. The fiber concentrate was oven-dried and stored under refrigeration for further analysis.
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10 w/v) and incubated to facilitate the solubilization of sugars. The suspension was centrifuged at 5000 rpm for 10 min, and the fiber-rich residue was rinsed twice with ethanol. The final fiber precipitate was filtered, oven-dried at 40 °C, and stored under refrigerated conditions.
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10 w/v; 50 mL) in a round-bottom flask and subjected to microwave irradiation at 300 W for 30 min. After the microwave treatment, the suspension was centrifuged at 5000 rpm for 15 min, separating the insoluble dietary fiber (pellet) from the soluble fraction. For ISDF, the precipitate was washed, oven-dried, and stored for further analysis, whereas for SDF, the supernatant was mixed with four times its volume of 95% ethanol and left undisturbed for 12 h to precipitate soluble fiber. The precipitate was collected by centrifugation (5000 rpm, 10 min), dissolved in distilled water, and subjected to rotary evaporation for ethanol removal. The purified fiber was oven-dried and stored.
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Chemical extraction methods, particularly alkali and ethanol extraction, demonstrated higher efficiency in dietary fiber recovery. According to Tejada-Ortigoza et al.,8 chemical treatments enhance water extractability and fiber release from plant cell walls. Alkaline extraction resulted in the highest fiber yield, followed by ethanol extraction and hot water extraction. The superior efficiency of ethanol extraction over hot water extraction may be attributed to its effectiveness in disrupting non-fibrous components, particularly in fruits and vegetables with lower starch, intracellular proteins, and polyphenol content.16,17
Alkaline extraction is particularly effective due to its ability to disrupt hydrogen and covalent bonds within the plant matrix, facilitating polysaccharide release. The presence of hydroxyl ions in the alkali solution enhances fiber solubilization by breaking hydrogen bonds, thereby increasing extraction efficiency.8 However, despite its high yield, alkali extraction has significant drawbacks, including potential chemical modifications in fiber structure, the need for pH neutralization, and residual chemical contamination risks.
Although thermal and chemical extraction methods are widely used, they are associated with certain limitations, including high energy consumption, extended extraction time, and the use of toxic solvents. These challenges highlight the need for green extraction techniques, which offer higher efficiency, reduced environmental impact, and improved fiber functionality. Green extraction methods, such as microwave-assisted extraction (MAE), have emerged as promising alternatives that overcome these limitations by reducing processing time, minimizing chemical usage, and improving fiber recovery rates.
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1 to 80
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1). The effect of these parameters on the yield of insoluble dietary fiber (ISDF) and soluble dietary fiber (SDF) was assessed for both kinnow peels and pomace as presented in Fig. 1 and 2, respectively.
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| Fig. 1 Effect of (a) microwave power, (b) extraction time, and (c) liquid to solid ratio on yield of dietary fiber from kinnow peels during microwave-assisted extraction. | ||
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| Fig. 2 Effect of (a) microwave power, (b) extraction time, and (c) liquid to solid ratio on yield of dietary fiber from kinnow pomace during microwave-assisted extraction. | ||
For kinnow peels, microwave power significantly influenced the extraction efficiency. The yield of both ISDF and SDF increased with power levels up to 400 W, beyond which a decline was observed. The reduction in dietary fiber content at higher power settings (600–800 W) can be attributed to the degradation of polysaccharides and simple sugars due to excessive heat exposure.18 A similar trend was noted for extraction time, where a peak in dietary fiber yield was observed at 6–9 min, followed by a decline at longer durations. Prolonged microwave exposure likely led to thermal degradation of fiber components, reducing the overall recovery of both ISDF and SDF.19 The liquid-to-solid ratio also played a crucial role in fiber extraction, with fiber yield increasing as LSR increased up to 50
:
1, likely due to enhanced mass transfer and improved solubilization of fiber components. However, further increases in LSR beyond this threshold had a negligible impact on extraction efficiency, indicating that an excess solvent volume does not significantly enhance fiber recovery.
For kinnow pomace, a similar pattern was observed (Fig. 2), with dietary fiber yield being significantly influenced by microwave power, extraction time, and LSR. The highest fiber yield was obtained at 450 W, LSR of 50
:
1, and an extraction time of 9 min. Beyond these optimized conditions, fiber yield declined, reinforcing the hypothesis that excessive microwave power and prolonged extraction time lead to degradation of soluble fiber fractions.20 The effect of LSR followed a similar trend to that of kinnow peels, where fiber yield increased with increasing solvent volume up to an optimal point but showed no further improvements at higher LSR values.
The results indicate that MAE is a highly efficient technique for dietary fiber extraction, offering shorter extraction times, reduced solvent usage, and improved fiber recovery compared to conventional techniques. Unlike hot water and ethanol extraction, which require prolonged heating and multiple rinsing steps, MAE facilitates rapid cell wall disruption through localized heating, enhancing fiber solubilization while minimizing structural degradation.20 These advantages establish microwave-assisted extraction as a superior alternative to conventional methods for dietary fiber extraction from kinnow by-products, highlighting its potential for large-scale food and nutraceutical applications.
The superior performance of MAE can be attributed to its ability to efficiently disrupt plant cell walls through rapid, uniform heating. Unlike conventional thermal treatments, which rely on external heat transfer, microwave energy penetrates the plant matrix, generating localized heating that facilitates better diffusion of fiber components into the solvent. This mechanism enhances fiber solubilization while minimizing thermal degradation of polysaccharides. Additionally, the shorter processing time in MAE reduces exposure to high temperatures, preserving the structural and functional integrity of dietary fiber. The results indicate a significant improvement in fiber yield with MAE compared to conventional methods. As observed in Fig. 3, the TDF content in kinnow peels and pomace extracted using MAE was 43.58% and 40.52%, respectively, which is notably higher than those obtained using alkali (34.59% and 28.98%), ethanol (38.42% and 34.34%), and hot water extraction (28.9% and 27.52%). Similarly, the MAE-extracted fiber exhibited higher SDF and ISDF contents, demonstrating its effectiveness in dietary fiber recovery. These findings highlight the advantages of microwave-assisted extraction over conventional methods, particularly in achieving higher fiber yields with reduced processing time and minimal chemical usage. The enhanced efficiency of MAE suggests its potential as a sustainable and scalable alternative for dietary fiber extraction from kinnow by-products in food and nutraceutical applications.
In the present study, the functional properties of dietary fiber obtained using different extraction techniques, i.e., hot water, ethanol, alkali treatments, and MAE, were compared (see Table 2). For MAE-extracted fibers, WHC ranged from 7.78 ± 0.10 g g−1 in pomace to 9.12 ± 0.11 g g−1 in peel, while OHC varied between 4.68 ± 0.06 g g−1 (pomace) and 5.36 ± 0.07 g g−1 (peel). These values are comparable to those reported for other citrus fibers, such as lemon peel (WHC = 8.24–25.28 g g−1, OHC = 3.80–5.00 g g−1)15 and orange fibers (WHC = 8.64–12.28 g g−1, OHC = 2.69–3.52 g g−1).22 Likewise, the swelling capacities of grapefruit, lemon, and lemon albedo fibers (5.16–6.50 mL g−1)23 aligned well with the values observed for kinnow fibers. The relatively higher values obtained for peel compared to pomace across all properties may be attributed to the greater pectin and soluble fiber content in peel, along with a more intact porous microstructure, as observed in SEM analysis. In contrast, pomace fibers consist of a heterogeneous mixture of collapsed parenchymal tissues and vascular residues.
| Extraction method | WHC (g g−1) | OHC (g g−1) | GAC (mmol g−1) at 10 mmol L−1 | GAC (mmol g−1) at 200 mmol L−1 |
|---|---|---|---|---|
| a The values are presented as mean ± SD. | ||||
| Kinnow peels | ||||
| Hot water | 12.00 ± 0.15 | 5.50 ± 0.07 | 2.60 ± 0.03 | 20.00 ± 0.28 |
| Ethanol | 7.50 ± 0.09 | 4.50 ± 0.06 | 2.00 ± 0.03 | 17.50 ± 0.22 |
| Alkali | 21.50 ± 0.32 | 6.50 ± 0.08 | 2.90 ± 0.04 | 23.00 ± 0.30 |
| MAE | 9.12 ± 0.11 | 5.36 ± 0.07 | 2.24 ± 0.03 | 19.11 ± 0.25 |
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| Kinnow pomace | ||||
| Hot water | 10.00 ± 0.13 | 5.00 ± 0.06 | 1.70 ± 0.02 | 18.00 ± 0.23 |
| Ethanol | 6.80 ± 0.08 | 4.00 ± 0.05 | 1.20 ± 0.02 | 14.50 ± 0.19 |
| Alkali | 17.00 ± 0.23 | 6.00 ± 0.08 | 1.90 ± 0.03 | 19.50 ± 0.25 |
| MAE | 7.78 ± 0.10 | 4.68 ± 0.06 | 1.34 ± 0.02 | 15.75 ± 0.20 |
Notable differences emerged when compared with other extraction methods. Hot water extraction produced fibers with moderately higher hydration-related properties, with peel fibers exhibiting WHC of 12.00 ± 0.15 g g−1 and GAC of 2.60 ± 0.03 mmol g−1 (10 mmol L−1), while pomace fibers showed WHC of 10.00 ± 0.13 g g−1. This enhancement can be explained by the solubilization of pectic substances during hot water treatment, which increases fiber swelling and water retention.23 Ethanol-treated fibers, on the other hand, showed reduced functional properties, with peel WHC dropping to 7.50 ± 0.09 g g−1 and pomace to 6.80 ± 0.08 g g−1, likely due to removal of soluble polysaccharides and phenolics that normally contribute to swelling and glucose binding. Alkali treatment resulted in the most pronounced improvements, with peel fibers showing WHC of 21.50 ± 0.32 g g−1, OHC of 6.50 ± 0.08 g g−1, and GAC of 2.90 ± 0.04 mmol g−1 at 10 mmol L−1. Pomace fibers also improved substantially (WHC 17.00 ± 0.23 g g−1), reflecting the strong de-esterification of pectin and partial removal of lignin and hemicellulose during alkali treatment, which exposes hydrophilic carboxyl and hydroxyl groups and enhances swelling and glucose-binding sites.24
GAC, another important functional property, reflects the fiber's ability to bind glucose in the intestinal tract, contributing to the potential reduction of postprandial glucose levels. In this study, the GAC of MAE-extracted fibers ranged from 1.34 ± 0.02 to 2.24 ± 0.03 mmol g−1 at a 10 mmol L−1 glucose concentration, increasing to 15.75 ± 0.20 to 19.11 ± 0.25 mmol g−1 at a 200 mmol L−1 glucose concentration, demonstrating that GAC is directly proportional to glucose concentration. These values are consistent with previous findings on citrus peel fibers, where GAC ranged from 3.68 to 5.14 mmol g−1 at lower glucose concentrations, rising to 18.5 to 23.3 mmol g−1 at higher glucose concentrations.25,26 This suggests that MAE-extracted kinnow dietary fiber exhibits a strong glucose-binding capacity, further supporting its in vitro hypoglycemic potential.
Overall, the comparative analysis suggests that MAE yields functional properties that are intermediate between those of hot water and alkali extraction. While alkali treatment dramatically improves WHC and GAC by chemically deconstructing cell wall polymers, MAE achieves competitive functionality without the use of harsh reagents, aligning better with sustainable and clean-label processing approaches. Ethanol treatment, although useful for purification, diminishes functional values by reducing soluble fractions. Thus, MAE-extracted kinnow peel and pomace fibers represent a balanced option, offering good WHC, OHC, and GAC while maintaining eco-friendly processing advantages.
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| Fig. 4 FTIR plot of (a) kinnow peel and its dietary fiber, and (b) kinnow pomace and its dietary fiber, extracted using microwave-assisted extraction. | ||
In the spectra of raw peels and pomace, a broad absorption band between 3200 and 3400 cm−1 was evident, corresponding to the O–H stretching vibrations of hydroxyl groups from cellulose, hemicellulose, and pectin, as well as bound water associated with the fiber matrix.27 This band is a hallmark of plant-based cell wall materials and was still visible in the MAE-extracted fibers, although the peak shape became sharper and slightly more defined, indicating disruption of the cell wall and exposure of additional hydroxyl groups. A prominent peak near 2925 cm−1, attributed to C–H stretching of methyl and methylene groups in the polysaccharide backbone,28 was observed in both raw and extracted samples, though with somewhat reduced intensity in pomace fibers compared to peel fibers, consistent with lower lipid and wax content in pomace.
In the carbonyl region, the raw peel showed a clear absorption around 1730–1750 cm−1, assigned to C
O stretching of esterified carboxyl groups in pectin and hemicellulose.15 This band was weaker in raw pomace and further decreased in intensity after MAE, particularly in pomace fibers, reflecting partial de-esterification and solubilization of pectin during extraction. Meanwhile, the band around 1600–1630 cm−1, which corresponds to the C
C stretching vibrations of lignin as well as absorbed water molecules,29 was present in all samples but appeared relatively more pronounced in pomace, consistent with its higher lignin fraction.
The fingerprint region (1200–1000 cm−1) was dominated by strong absorptions attributed to C–O stretching vibrations of the glycosidic bonds and pyranose rings of cellulose and hemicellulose. In raw samples, these peaks were broad, while in extracted fibers they appeared sharper and more intense, particularly around 1245 cm−1 and 1020–1050 cm−1, confirming the exposure of structural polysaccharides after MAE. A small but characteristic peak near 890 cm−1, associated with β-glycosidic linkages of polysaccharides, was also observed, reaffirming the carbohydrate nature of the matrix.11
Overall, comparison of raw and MAE-treated samples confirms that the main functional groups characteristic of dietary fiber, i.e., O–H, C–H, C
O, and C–O stretching bands, were preserved after extraction, while certain changes in peak intensity and sharpness reflect the structural modifications induced by MAE. Specifically, reduced ester C
O peaks and enhanced carbohydrate fingerprint bands demonstrate the partial removal of soluble pectin fractions and exposure of cellulose/hemicellulose domains. These findings indicate that MAE effectively disrupts the native matrix while maintaining the integrity of key polysaccharide structures necessary for desirable functional properties such as water-holding, oil-holding, and glucose adsorption capacity (Section 3.4.1). The observed profiles are consistent with earlier studies on citrus-derived dietary fiber, where similar spectral characteristics have been reported.15,22
The intensity of these peaks was higher in pomace-derived fibers compared to peel-derived fibers, indicating that pomace fibers exhibit a slightly higher degree of crystallinity. This may be attributed to the higher proportion of structural cellulose in pomace fibers, while peel fibers likely contain more amorphous pectin, hemicellulose, and phenolic compounds, which contribute to the broader background signal and lower overall crystallinity. The presence of broad peaks, particularly in the 10° to 30° range, suggests that both fiber samples contain a mixture of crystalline cellulose and amorphous polysaccharides, which is consistent with the heterogeneous composition of plant-derived dietary fiber.15,22
The semi-crystalline nature observed for both samples is a desirable property for functional dietary fiber applications, as the amorphous regions contribute to higher water and oil holding capacities by providing more accessible binding sites, while the crystalline regions enhance structural stability, allowing the fiber to retain its functionality during processing.31 The results indicate that microwave-assisted extraction did not cause extensive disruption of the natural cellulose crystalline regions, preserving the structural characteristics of the extracted fiber, which is advantageous for maintaining the desired functional and textural properties in food applications.
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| Fig. 5 DSC plot of dietary fiber obtained using microwave-assisted extraction of kinnow byproducts. Here Po = pomace, Pe = peels, SDF = soluble dietary fiber, ISDF = insoluble dietary fiber. | ||
The first thermal event, an endothermic peak occurring between approximately 60 °C and 120 °C, corresponds to the release of bound water and initial structural relaxation within the fiber matrix. This transition reflects the disruption of hydrogen bonds between bound water molecules and fiber components, particularly in the more hydrophilic SDF fraction, which exhibited a more pronounced response in this temperature range compared to ISDF. This observation is consistent with the higher water-holding capacity (WHC) measured for SDF (Section 3.4.1) and aligns with previous studies indicating that plant-derived fibers often contain hygroscopic components such as pectins, gums, and mucilages, which contribute to their water-binding properties.1 This endothermic peak, representing moisture loss and structural relaxation, is a critical indicator of fiber hydration behavior, which influences functional properties such as viscosity, gel formation, and syneresis control in food applications.
The second thermal event, occurring between 300 °C and 350 °C, corresponds to the exothermic decomposition of polysaccharide components, including cellulose, hemicellulose, and residual pectin or lignin fractions. The ISDF fractions from both peels and pomace exhibited higher thermal stability (delayed decomposition) compared to SDF, a difference attributed to the more ordered, crystalline structure of insoluble fibers relative to the amorphous polysaccharide fractions characteristic of soluble fibers. The slightly higher decomposition temperatures observed for peel-derived fibers (both SDF and ISDF) compared to pomace-derived fibers likely reflects compositional differences, with peel fibers containing a greater proportion of structural polysaccharides and lignin, while pomace fibers may have higher pectin content, which decomposes at lower temperatures.
These observations are consistent with reported DSC findings for other plant-derived fibers. For example, jackfruit peel cellulose exhibited an endothermic peak at 323.5 °C with an enthalpy change (ΔH) of 0.3152 mW mg−1, highlighting the thermal degradation of cellulose at elevated temperatures.32 Similarly, cellulose powder showed a lower-temperature endothermic peak around 74 °C with a ΔH of 72 J g−1, attributed to the release of loosely bound water.33 In contrast, ethyl cellulose displayed an exothermic decomposition peak at 334.46 °C with an enthalpy of 1.10 kJ g−1, reflecting the influence of chemical modification on its thermal behavior.34 Comparable exothermic peaks were reported for cotton cellulose (315 °C, ΔH = 7.65 J g−1) and raw banana fibers (350 °C, ΔH = 35.7 J g−1), with acid-treated banana fibers displaying a much lower endothermic peak at 113.7 °C, with a ΔH of 1279 J g−1, indicating extensive structural modification caused by acid treatment.35,36 These comparisons illustrate that the thermal properties of dietary fiber are highly dependent on source material, structural composition, and pre-treatment methods.
The thermal behavior observed for kinnow-derived dietary fiber in this study falls within the general range reported for other plant-derived fibers, reinforcing that microwave-assisted extraction preserves the thermal stability of both soluble and insoluble fractions. This thermal resilience, especially in the ISDF fraction, enhances the potential applicability of kinnow dietary fiber in thermally processed food products, such as baked goods, extruded snacks, and meat analogues, where maintaining fiber functionality under heat is essential.
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