ArticlePublisher preview available

Drying of peaches by a combination of convective and microwave methods

Authors:
To read the full-text of this research, you can request a copy directly from the authors.

Abstract and Figures

The aim of this work is to study a method to extend the storage life of peaches reducing energy and time consumption and ensuring food quality. The conventional method of hot air dying presents many drawbacks, whereas the microwave drying usually leads to overheating and textural damage. Thus, in this work, a combination of convective and microwave methods, more specifically a two‐stage drying process with an initial convective air drying followed by a microwave drying (microwave finishing), was studied for the drying of peaches. Peaches dried at 70°C for various times, 200, 278, 355, 433, and 510 min, were then dried in a microwave oven at powers of 300, 500, and 800 W. Drying rates were examined, whereas dry peaches were characterized for their color, antioxidant capacity, shrinkage, and rehydration ability under optimized conditions for the situations with and without pretreatment with ascorbic acid. Mass transfer of water was described by nine empirical models and by the diffusional approach. The shrinkage of peach tissue during microwave finishing was evaluated and diffusion coefficients were assessed with shrinkage considered. The microwave finishing reduced the drying time by 89 ± 40%, while a smaller shrinkage was observed, with better rehydration characteristics. Practical applications Peaches are important commodities in terms of global agricultural production. As peach is a perishable product with a short shelf‐life, the food industry has been forced to find methods, such as drying, that extend its storage life by months. The conventional method of hot air dying presents many disadvantages. Last decades, microwave drying proposed an alternative way to improve the quality of dehydrated products. However, microwave is rarely used alone as a drying method and is usually combined with other drying techniques. The main goal of this work is to study an innovative method to extend the storage life of peaches reducing energy and time consumption and ensuring food quality.
This content is subject to copyright. Terms and conditions apply.
ORIGINAL ARTICLE
Drying of peaches by a combination of convective and
microwave methods
Theodora Chatzilia | Kyriakos Kaderides | Athanasia M. Goula
Department of Food Science and Technology,
School of Agriculture, Forestry and Natural
Environment, Aristotle University,
Thessaloniki, Greece
Correspondence
Athanasia M. Goula, Department of Food
Science and Technology, School of Agriculture,
Forestry and Natural Environment, Aristotle
University, 541 24 Thessaloniki, Greece.
Email: athgou@agro.auth.gr
Abstract
The aim of this work is to study a method to extend the storage life of peaches
reducing energy and time consumption and ensuring food quality. The conventional
method of hot air dying presents many drawbacks, whereas the microwave drying
usually leads to overheating and textural damage. Thus, in this work, a combination
of convective and microwave methods, more specifically a two-stage drying process
with an initial convective air drying followed by a microwave drying (microwave fin-
ishing), was studied for the drying of peaches. Peaches dried at 70C for various
times, 200, 278, 355, 433, and 510 min, were then dried in a microwave oven at
powers of 300, 500, and 800 W. Drying rates were examined, whereas dry peaches
were characterized for their color, antioxidant capacity, shrinkage, and rehydration
ability under optimized conditions for the situations with and without pretreatment
with ascorbic acid. Mass transfer of water was described by nine empirical models
and by the diffusional approach. The shrinkage of peach tissue during microwave fin-
ishing was evaluated and diffusion coefficients were assessed with shrinkage consid-
ered. The microwave finishing reduced the drying time by 89 ± 40%, while a smaller
shrinkage was observed, with better rehydration characteristics.
Practical applications
Peaches are important commodities in terms of global agricultural production. As
peach is a perishable product with a short shelf-life, the food industry has been
forced to find methods, such as drying, that extend its storage life by months. The
conventional method of hot air dying presents many disadvantages. Last decades,
microwave drying proposed an alternative way to improve the quality of dehydrated
products. However, microwave is rarely used alone as a drying method and is usually
combined with other drying techniques. The main goal of this work is to study an
innovative method to extend the storage life of peaches reducing energy and time
consumption and ensuring food quality.
KEYWORDS
diffusion coefficient, drying, microwave, peach, rehydration, shrinkage
1|INTRODUCTION
Peach (Prunus persica) is a member of the Rosaceae family and is char-
acterized as stone fruitdue to the fact that its seeds are found in a
hard endocarp. It is one of the most nutritionally fruits worldwide with
a significant amount of various polyphenols, carotenoids, vitamins
(provitamin A and vitamin C), fibers, and minerals (potassium) (Saidani
et al., 2017). Peaches are important products as far as their global
Received: 9 November 2022 Revised: 14 January 2023 Accepted: 28 January 2023
DOI: 10.1111/jfpe.14296
J Food Process Eng. 2023;46:e14296. wileyonlinelibrary.com/journal/jfpe © 2023 Wiley Periodicals LLC. 1of16
https://doi.org/10.1111/jfpe.14296
... Freeze-drying and vacuum drying are particularly effective in preserving product quality; however, their high energy consumption and prolonged processing times present significant drawbacks [9]. Alternative methods, such as microwave and infrared drying, offer faster moisture removal but require precise control to avoid uneven heating and potential quality degradation [12][13][14]. Convective drying is a widely utilized method in the food industry, balancing moisture removal with the retention of functional properties and enabling larger sample volumes to be processed efficiently [9,[14][15][16]. Nevertheless, the high fiber content and porous nature of raspberry pomace pose challenges, including uneven drying and potential quality degradation if the process is not properly optimized [4]. ...
... Alternative methods, such as microwave and infrared drying, offer faster moisture removal but require precise control to avoid uneven heating and potential quality degradation [12][13][14]. Convective drying is a widely utilized method in the food industry, balancing moisture removal with the retention of functional properties and enabling larger sample volumes to be processed efficiently [9,[14][15][16]. Nevertheless, the high fiber content and porous nature of raspberry pomace pose challenges, including uneven drying and potential quality degradation if the process is not properly optimized [4]. ...
... Although drying at 70 • C appears to provide a compromise between processing efficiency and moderate preservation of phenolic compounds and anthocyanins, the significant reductions in these compounds compared to freeze-dried samples highlight the need for further optimization. Incorporating techniques that reduce the drying time and thermal exposure, such as combining microwave-assisted drying with convective drying, could be an effective solution [14]. Although microwave drying can cause uneven heating if the parameters are not precisely controlled, integrating it with convective drying could reduce the overall heat exposure, potentially minimizing thermal degradation of sensitive compounds. ...
Article
Full-text available
This study aimed to transform raspberry pomace, a by-product of the berry industry, into a sustainable, fiber-rich functional ingredient using convective drying. Drying experiments were conducted at temperatures of 50, 60, 70, 80, and 90 °C to identify the optimal conditions that balance process efficiency and preservation of functional and bioactive properties. The best results were achieved at 70 °C, where a high drying rate (DR) of 0.46 kg H2O·kg−1 db·min−1, effective moisture diffusivity (Deff) of 1.53 × 10−10 m2·s−1, and activation energy (Ea) of 34.90 kJ·mol−1 were observed. The Page model accurately represented the drying behavior (R2 = 0.9965−0.9997). Total dietary fiber (TDF) content remained stable across temperatures (52.52–64.76 g·100 g−1 db), while soluble dietary fiber (SDF) increased by 43.40%, resulting in a solubility (SOL) of 71.8%, water-holding capacity (WHC) of 8.2 mL·g−1 db, and oil-holding capacity (OHC) of 3.0 mL·g−1 db. High retention of bioactive compounds was achieved at 70 °C, including phenolics (32.10 mg GAE·g⁻1 db) and anthocyanins (25.84 mg C3G·g−1 db), resulting in significant antioxidant activities (DPPH: 33.29 mg AAE·g−1 db, IC50 0.016 mg·mL⁻1; ABTS: 35.85 mg AAE·g−1 db, IC50 0.029 mg·mL⁻1). These findings demonstrated the potential of convective drying at 70 °C to efficiently transform raspberry pomace into a high-quality functional ingredient. This process promotes sustainable production and waste reduction in the berry industry.
... Additionally, microwave drying has the advantage of preserving the quality characteristics of the products including color, vitamins, minerals, and nutritional components [16]. However, microwave drying has some undesirable adverse efects due to overheating, thus textural damage on the fnal product can occur [17]. Tose features result in limited application of the method. ...
... Te limitations associated with applications of hot air and microwave drying methods alone can be efectively solved by taking advantage of their combined applications. A dual-stage drying approach consisting of convective air drying and microwave drying has been demonstrated to enhance product quality while reducing both time and energy consumption [17,18]. Convective air drying primarily targets surface water removal, whereas microwave energy facilitates the extraction of internal moisture content [19]. ...
... In particular, the integration of microwave pretreatment followed by hot air drying has been investigated in several studies on fruit and vegetables. Tese studies have consistently shown that this combined approach results in reduced drying times while maintaining high product quality, characterized by improved visual appeal and reduced nutrient degradation [17,21,30,37,38]. Terefore, the selection of an optimal drying temperature range between 60 and 80°C was assumed to reduce processing time while maintaining quality attributes. ...
Article
Full-text available
Citrus fruits, regarded as a prominent fruit crop, are cultivated extensively around the globe and orange (Citrus sinensis L.) is a widely cultivated popular member of the citrus family. Dried oranges have gained recognition as a healthy snack option among consumers and worldwide markets due to the absence of additional ingredients such as sugar and chemicals, whilst yet containing significant natural beneficial components. The drying method is very intriguing due to its ability to facilitate the efficient production, packaging, storage, and transportation of dried oranges at a cost-effective price. In this study, the effects of microwave pretreatment (Mpt) (90 W, 30 min) on hot air drying (HTAD-MW) (60, 70, and 80°C) were investigated, along with the effects on the drying kinetics, rehydration capacity, and quality properties of the orange snack including phenolic compounds (vanillic acid, gallic acid, epicatechin, hesperidin, naringenin, chlorogenic acid, sinapic acid, and o-coumaric acid), antioxidant capacities (with DPPH, FRAP, and CUPRAC methods), and ascorbic acid contents. For modeling the kinetics of orange snack drying in all tests, logarithmic, Wang and Singh’s, diffusion approach, two term, and Wang and Sing’s models performed best. Hot air drying (HTAD) at 70°C applied orange snacks showed the lowest △E ∗ ab value, and the color values were close to those of fresh orange slices. The levels of total and individual phenolics, antioxidant capacity (AC), and ascorbic acid (AA) in dried orange snacks were found to be significantly lower ( p < 0.05) than in the fresh orange slices. Results also showed that HTAD-MW-applied orange snacks contained more total phenolic (TP) content, individual phenolic content, and AC but lower AA than HTAD-applied samples. The highest amount of phenolic compound was hesperidin for fresh and dried orange snacks. The method that best preserves the TP content and AC of dried orange snacks was found at the drying condition of HTAD-MW at 60°C. As a conclusion, it was suggested that the use of microwave and hot air combination is a promising method to introduce a new functional healthy snack to the dried product market with high quality.
... As the microwave power increased, there were improvements in the temperature gradients and surface evaporation rates, leading to an acceleration in the diffusion of moisture from the interior to the surface. These outcomes align with the results of other studies that linked higher microwave power to reduced drying times [42,45]. ...
... This combination of vacuum drying assisted by condensation is a highly effective method for preserving the color of dried apples. Ref. [45] evaluated the color change of peaches under a combination of convective and microwave methods and they claimed that increasing the temperature considerably affected the color of the samples. Similarly Ref. [32] used microwave drying and combined microwave-convective drying for drying blueberry fruit and assessed the effect of increasing the power on the color and some chemical aspects of blueberry fruit. ...
Article
Full-text available
One of the challenges in the drying process is decreasing the drying time while preserving the product quality. This work aimed to assess the impact of pulsed electric field (PEF) treatment with varying specific energy levels (15.2–26.8 kJ/kg) in conjunction with a microwave vacuum dryer (operating at energy levels of 100, 200 and 300 W) on the kinetics of drying apple slices (cv. Gravenstein). The findings demonstrated a notable reduction in the moisture ratio with the application of pulsed electric field treatment. Based on the findings, implementing PEF reduced the drying time from 4.2 to 31.4% compared to the untreated sample. Moreover, two mathematical models (viz. Page and Weibull) and two machine learning techniques (viz. artificial neural network and support vector regression) were used to predict the moisture ratio of the dried samples. Page’s and Weibull’s models predicted the moisture ratios with R2 = 0.958 and 0.970, respectively. The optimal topology of machine learning to predict the moisture ratio was derived based on the influential parameters within the artificial neural network (i.e., training algorithm, transfer function and hidden layer neurons) and support vector regression (kernel function). The performance of the artificial neural network (R2 = 0.998, RMSE = 0.038 and MAE = 0.024) surpassed that of support vector regression (R2 = 0.994, RMSE = 0.012 and MAE = 0.009). Overall, the machine learning approach outperformed the mathematical models in terms of performance. Hence, machine learning can be used effectively for both predicting the moisture ratio and facilitating online monitoring and control of the drying processes. Lastly, the attributes of the dried apple slices, including color, mechanical properties and sensory analysis, were evaluated. Drying apple slices using PEF treatment and 100 W of microwave energy not only reduces drying time but also maintains the chemical properties such as the total phenolic content, total flavonoid content, antioxidant activity), vitamin C, color and sensory qualities of the product.
... Microwave Drying. As previously described by Chatzilia et al. [28], the three coriander fractions were dried in a microwave oven (Model R-3556M, 2450 MHz, Sharp Electronics Ltd., UK) at 800 W power. First of all, before drying, moisture content of each fraction was determined; after that, 500 g of each fraction was processed until the leaves, flowers, and seeds were totally dried, spreading them uniformly on a glass microwave oven plate. ...
... The traditional hot air dying procedure has a lot of drawbacks. Microwave drying has provided a different approach in recent decades to enhance the quality of dried goods [28]. Present results were found in accordance with the earlier results of Shahwar et al. [37], when they compared coriander seeds and leaves for proximate analysis and reported significantly high amounts of ash, fat, fiber, and protein contents in seeds. ...
Article
Full-text available
The coriander plant (Coriandrum sativum L.) is well known for its antibacterial and antioxidant properties since it contains a considerable number of bioactive compounds. This property encourages the use of coriander in food because it has many health benefits and preserves food longer. The current study’s objective was to demonstrate the extraction of coriander’s three fractions (leaves, flowers, and seeds) using microwave drying and ultrasonic assistance, in order to identify its distinct functional components. After microwave drying, the highest amounts of ash, fat, fiber, and protein with values 6.39±0.04, 10.10±0.05, 10.14±0.06, and 13.10±0.03%, respectively, were observed in coriander seeds. Among macro- and microminerals analyzed, contents of Ca and Mg were found highest in coriander leaves, with values 689±0.14 and 412±0.04 mg/100 g, respectively, whereas Fe, Zn, and Mn were found highest in seeds with values 15.46±0.02, 3.92±0.02, and 1.29±0.02 mg/100 g. Ultrasonic-assisted ethanolic extracts of microwave-dried coriander leaves presented significantly high (p<0.05) total phenolic contents (253.45±0.12 mg gallic acid equivalent/100 g), total flavonoid contents (98.15±0.09 mg quercetin equivalent/100 g), and total antioxidant activity (47.32±0.04 mg trolox/100 g), followed by seeds, while flowers presented lowest values. Significantly high (p<0.05) antimicrobial activities were exhibited from extracts of coriander seeds, followed by leaves. It was concluded that leaves, flowers, and seeds of coriander all were rich source of nutritional components and bioactives, and microwave drying and ultrasonic-assisted extraction were proved useful techniques for maximum retention of these contents in powders and ethanolic extracts, respectively.
... The drying process is applied to peach products for off-season consumption. Peach products are dried by different methods such as hot air, natural drying, freeze drying, far-infrared, microwave, hot air-microwave combined method, and sun drying, and there are many articles discussing the effects on different parameters [14][15][16][17]. According to the literature study, no studies were found on drying peach by EHD, hot air and EHD-hot air methods. ...
Article
Full-text available
This study aimed to investigate drying times mathematical models and assess the color, rehydration capacity, and microstructure of dried peach using electrohydrodynamic (EHD), hot air, and electrohydrodynamic-hot air (EHD-hot air) drying methods. Peach samples were subjected to drying with two different air temperatures (50 and 55 °C) and electric field (EF, 6.67 and 10 kV cm−1) under constant air velocity (1.5 m s−1). The longest drying durations were obtained in the EHD method (720 and 600 min), followed by hot air (290 and 260 min) and EHD-hot air method (120, 140, 170, and 200 min), respectively. The drying curves were best described by the Midilli et al. and Logarithmic models. The L* values of the samples subjected to hot air drying were found to be lower than those obtained through other methods. No significant effect of the electric field on rehydration capacity was observed. The study revealed that increased temperature and electric field led to surface cracks on the peach. The study highlights the compatibility of the EHD method with the hot air method, suggesting its potential application within the drying industry. From these findings, it was seen that the EHD-hot air combination method could be an alternative to the hot air method in the food industry by reducing the drying time of peaches and considering that the color parameters are generally better than the hot air method.
... The heat transfer process in providing the necessary energy for moisture evaporation is a crucial factor in the drying process. In general, the method of heat transfer to a moist body can be divided into three categories: a) drying by convection, b) drying by conduction, and c) drying by radiation [18]. ...
Article
Full-text available
This study investigated the moisture changes in Haj Kazemi peach slices during drying in a thin-layer dryer at five temperature levels (40, 50, 60, 70, and 80°C), three levels of inlet air velocity (1, 1.5, and 2 m/s), and three slice thicknesses (2, 4, and 6 mm). The relative moisture content during drying was calculated, and an adaptive neuro fuzzy inference system (ANFIS) was used to predict the drying process of peach slices. The results indicated that slice thickness had a greater impact on drying time than air velocity. Moreover, an almost direct relationship was observed between changes in slice thickness and drying time. The effective moisture diffusivity coefficient in peach slices increased with an increase in slice thickness, temperature, and air velocity and ranged from 9.57 × 10^-10 to 4.33 × 10^-9 m^2/s under different experimental conditions. The calculated activation energy for drying peach slices under experimental conditions ranged from 16.74 to 20.48 kJ/mol. The designed model for simulating the drying conditions was based on an adaptive neuro fuzzy inference system (ANFIS) with input and output membership functions of triangular and linear shapes and a hybrid learning algorithm. The model could simulate the drying process with a correlation coefficient of 0.979.
Article
Full-text available
Currently, approximately 34% of fruit is lost and wasted in emerging economies due to inefficient post-harvest processes, technological shortcomings, lesser valorization of surpluses, and byproducts. Peach (Prunus persica L.) is a fruit with a good yearly growth rate but higher postharvest losses in Colombia. One way to take advantage of this type of product is through the application of drying processes that increase its shelf life and its inclusion in the food chain. Refractance Window Drying (RWD) is a fourth generation drying technique implemented by the food industry in the last few decades and has been applied to several dehydrated food products. This study compared the effects of different drying methods on the physical and sensory properties of peaches surplus. Treatments consisted of (i) peaches were sliced (1, 2, and 3 mm thickness) and dried using RWD at 86°C, (ii) peach pulp mixed with maltodextrin (MD) (0.12–0.33 kg of MD/kg of sample) and RWD (RWD-MD), and (iii) conventional oven drying (OD) at 60°C (3 mm thick) dried for 24 h. The study found that the drying method significantly (p < 0.05) affected the texture, color, and general taste of peaches. The results showed that processing treatments combined with different drying conditions affected the physical properties of the peach. RWD in slices reduced water content to 0.05 kg H2O/kg in 40 min, showing fewer effects on color attributes. A surface response analysis on RWD showed good correlations for water activity (R² = 0.8652–0.9894) and moisture content (R² = 0.7048–0.9826). A higher diffusion coefficient (1.63 × 10⁻⁶ m² s⁻¹) was observed for RWD in slices with 3 × 10⁻³ m of thickness; however, for RWD-MD, differences in diffusion coefficients were present for the lowest MD addition (0.12 kg/kg), vitamin C was not detected on the dried slices, and higher concentration of β-carotene (175.88 μg/100 g) was found on the thinner slices. Principal component analysis showed that RWD in the slices was the most suitable drying process, followed by OD. Sensory analysis showed good acceptability for RWD slices after 30 days of storage.
Article
Full-text available
In light of large scale production of Salvia officinalis L. and its complex storage and delivery chain, the efficient preservation process is required. At this moment, the most popular preservation method is drying, therefore a comprehensive experiment to evaluate the influence of multiple drying techniques on sage was conducted. Convective drying at 40, 50 and 60 °C, vacuum-microwave drying with powers 240, 360 and 480 W and combined drying consisting of convective pre-drying at 50 °C followed by vacuum-microwave finish-drying with power 360 W were applied. To evaluate the effect of particular procedures chemical analyses were performed, namely evaluation of changes in bioactive volatile constituents, odour-active compounds and various groups of non-volatile bioactive constituents of sage. The obtained results shown, that to receive the product with expected quality, it is necessary to identify the designation of the product before treatment, since particular groups of phytochemicals react differently during drying.
Article
Full-text available
Modeling the thin-layer drying of foods is based on describing the moisture ratio versus time data by using a suitable mathematical model or models. Several models were proposed for this purpose and almost all studies were related to the application of these models to the data, a comparison and selecting the best-fitted model. A careful inspection of the existing drying data in literature revealed that there are only a limited number of curves and, therefore, the use of some models, especially the complex ones and the ones that require a transformation of the data, should be avoided. These were listed based on evidence with the use of both synthetic and published drying data. Moreover, the use of some models were encouraged, again based on evidence. Eventually, some suggestions were given to the researchers who plan to use mathematical models for their drying studies. These will help to reduce the time of the analyses and will also avoid the arbitrary usage of the models.
Article
Full-text available
Drying is removing a large portion of the water contained in a product in order to considerably reduce the reactions which leads to deterioration of the products. In less developed countries where industry is not very important there is a general feeling that drying is an easy operation and not too much input is needed and anybody can do it. Drying of foods is a complex business and a mere translation from other fields is not often advisable. Drying plays an important role in food and agricultural industries and is the oldest method of preservation. The main feature of this process consists on lowering the water content in order to avoid or slow down food spoilage by microorganism. This review focuses upon conventional and new drying techniques and their advantages, limitations and applications.
Article
Full-text available
Ultrasound-assisted osmotic dehydration was evaluated as a method for supplementing potato with unused chokeberries phenolics. Sodium chloride and maltodextrin were used as osmoactive solutes, and the cubes were treated with different osmotic solution concentrations (15–30%, w/w) and sodium chloride concentrations (0–12%, w/w) under different temperatures (20–45 °C) for different times (30, 60, 120, 180, 240, and 300 min). Samples treated with ultrasonic osmotic dehydration showed about 10–37% higher water loss than those dehydrated under simple agitation, and this percentage was found highly correlated with the increase of potato cells cross-section area achieved by ultrasounds. The final total phenolic content in the osmo-treated potato cubes was between 0.08 and 1.34 mg/g, and it was very close to that of the richest fruits and vegetables. In addition, mass transfer of water, solids, and total phenolics were characterized by the diffusional approach. The shrinkage of potato tissue during the treatment was evaluated, and diffusion coefficients were assessed more accurately by the analytical solution of the Fick’s law with shrinkage considered. The present study concluded that osmotic dehydration is a feasible technology for impregnation of functional ingredients into foods. Graphic Abstract
Article
Full-text available
Drying is known as the best method to preserve fruits, vegetables, and herbs, decreasing not only the raw material volume but also its weight. This results in cheaper transportation and increments the product shelf life, limiting the food waste. Drying involves the application of energy in order to vaporize and mobilize the moisture content within the porous products. During this process, the heat and mass transfer occurs simultaneously. The quality of dehydrated fruits, vegetables, and aromatic herbs is a key problem closely related to the development and optimization of novel drying techniques. This review reports the weaknesses of common drying methods applied for fruits, vegetables, and aromatic herbs and the possible options to improve the quality of dried products using different drying techniques or their combination. The quality parameters under study include color, bulk density, porosity, shrinkage, phytochemicals, antioxidant capacity, sugars, proteins, volatile compounds, and sensory attributes. In general, drying leads to reduction in all studied parameters. However, the behavior of each plant material is different. On the whole, the optimal drying technique is different for each of the materials studied and specific conditions must be recommended after a proper evaluation of the drying protocols. However, a novel or combined technique must assure a high quality of dried products. Furthermore, the term quality must englobe the energy efficiency and the environmental impact leading to production of sustainable dried products.
Article
This research work explored the effect of microwave output power on the drying characteristics, moisture diffusion, drying efficiency, and specific energy consumption. Banana blossom was cut into 3 mm thickness and was dried as monolayers at five different power levels (160, 320, 480, 640, and 800W). After drying powdered banana sample was analyzed for colour attributes and functional characterization. Eight different mathematical models were investigated and the Page model was the best‐fitted model for all samples with the maximum R2 values of 0.99359 (P‐160W), 0.99505 (P‐320W), 0.99344 (P‐480W), 0.99160 (P‐640W), 0.99192 (P‐800W). The drying time was minimizing from 40 to 10 min as the microwave output powers increase from 160 to 800W. The drying constant (k) is enhanced as microwave power increases. The effective diffusivity of banana blossoms varied from 4.428×10‐7 to1.171×10‐7 m2/s and the activation energy was estimated as 7.96 W/g. Maximum energy consumption was found to be 7.74 MJ/kg water at 160 W whereas minimum energy consumption was minimum (5.74 MJ/kg water) at the microwave power of 640 W. Energy efficiency increases with increasing microwave output power. Applied microwave output power was a critical aspect of all colour parameters of the banana blossom powder. Powdered banana blossom dried at 640W showed the highest lightness L* of 54.43±0.46 with redness (a*) of 4.19±0.03, and yellowness (b) of 10.71±0.29. The highest water solubility index was 53.30±0.59 % for the sample dried at 640W and oil absorption capacity( g/g) and foaming capacity (ml) were varied from 1.76±0.07 to 2.93 g/g and 1.67±0.58 to 4.53±0.57 ml.
Article
In this study, microwave drying characteristics of black mulberry were studied at microwave power levels of 90, 180 and 360 W. Obtained experimental drying results were applied to seven mathematical models of Aghbashlo et al., Henderson and Pabis, Jena and Das, Logaritmic, Midilli and Kucuk, Page and Weibull. The best model was selected as Midilli and Kucuk based on the highest coefficient of determination (R²) (0.994861–90 W, 0.999824–180 W, 0.998747–360 W) and the lowest χ² (0.000575–90 W, 0.000027–180 W, 0.000255–360 W) and Root Mean Square Error (RMSE) (0.022427–90 W, 0.004275–180 W, 0.011899–360 W) values compared to other models. According to drying times, the best drying condition was seen on 360 W power. The effective moisture diffusivity (Deff) values were calculated using the Fick’s second law’s spherical coordinate approximation and were found between 4.79 × 10⁻⁸ and 2.60 × 10⁻⁷ m²/s. The activation energy (Ea) was calculated using modified form of Arrhenius equation and found as 13.15 kW/kg.
Article
The preservation of herbs during post-harvest operations is crucial in maintaining their potency. The preservation of Malaysian rosemary (Rosmarinus officinalis L.) was investigated by determining the effect of various drying processes on active volatile components and their respective bioactivities. The drying processes included convective drying at 50, 60, and 70 °C; freeze-drying; vacuum-microwave drying (VMD) at 240, 360, and 480 W; and combination of convective pre-drying (CPD) for 30, 60, and 120 min followed by vacuum-microwave finish drying (VMFD) at 360 W. Complete moisture removal was achieved the fastest by VMD at the highest wattage. Semi-theoretical models, namely, modified Henderson–Pabis, Page, and modified Page had the best prediction accuracy of drying kinetics with the highest R² (>0.9704) and the lowest RMSE (<0.0565). Sixty-seven compounds were identified from fresh and dried rosemary leaves with camphor (1.45 g kg⁻¹ DW), α-pinene (1.64 g kg⁻¹ DW), and α-terpineol (1.79 g kg⁻¹ DW) as the dominant volatiles. The highest volatile percentage, phenolic content, and antioxidant activities were determined from convective-dried leaves at 60–70 °C, whereas the best anti-diabetic and anti-aging effects were detected from freeze-dried leaves. Non-identified compounds probably have a substantial contribution to the bioactivities of freeze-dried leaves. VMD at 480 W was the most efficient method with the least energy consumption. The sequential method of CPD-VMFD performed moderately among the investigated processes in all aspects. Future studies should further improve the drying processes and investigate the nonvolatile fraction of dried rosemary.
Article
Piper umbellatum L. possesses diuretic, antimalarial, vermifuge, and anti-inflammatory properties, in addition to having essential oil in its leaves. Presuming that substances and essential oils in medicinal plants can be altered when they are subjected to various drying conditions, this study aimed to evaluate kinetic drying as well as the composition of essential oil from P. umbellatum L. leaves. The drying process was completed using four temperatures (40 °C, 50 °C, 60 °C, and 70 °C) and two drying air velocities (0.4 and 0.7 m s⁻¹), being the drying process stopped when the moisture content of leaves was equal to 0.11 ± 0.01 dry basis (d.b.). The essential oil of the leaves was determined by hydrodistillation. The chemical components were analyzed by GC–MS. The Midilli model was the only one who represented satisfactorily product drying curves and the rise of temperature and drying air velocity resulted in the increase of the drying rate and in decreasing the content of essential oil from leaves. In total, 28 chemical substances were identified in the essential oil, with piperitone, dillapiole, and myrcene being the majorities. The obtained data indicated that the drying process maintain the quality patterns of the essential oils from the leaves; a slight alteration in the compound percentage was also observed.
Article
The strong physical effects of ultrasound can change the state of water in food. In order to study the effect of ultrasound on the microwave drying of apple slices, an ultrasonic online-assisted microwave vacuum drying (UOAMVD) device was designed. The curves of moisture content versus drying time, the change in dielectric constant and dielectric loss factor, and the flow characteristics of water molecules were obtained during microwave vacuum drying (MVD), microwave vacuum drying with the apple slices pretreated by ultrasound (MVDPU), and UOAMVD, was measured by a vector network analyzer and a low-field nuclear magnetic resonance and imaging analyzer. The differences in color and microporous structure of the different dehydrated products were determined. Compared with MVD and MVDPU, apple slices that underwent UOAMVD had a higher drying rate and improved drying uniformity, and the dielectric constant was significantly reduced. In addition, the color of the UOAMVD dehydrated samples was the closest to that of fresh apple slices, whereas the microporous structure was not obvious and there was granular starch overflow. UOAMVD significantly improved the microwave drying efficiency and quality of apple slices. This work provides a reference for enhancing the application of ultrasonic microwave combination drying.