Food Sci Biotechnol (2019) 28(5):1465–1474 https://doi.org/10.1007/s10068-019-00588-7 Effects of hot air, microwave and vacuum drying on drying characteristics and in vitro bioaccessibility of medlar fruit leather (pestil) Senem Suna1 Received: 13 November 2018 / Revised: 11 February 2019 / Accepted: 18 February 2019 / Published online: 4 March 2019  The Korean Society of Food Science and Technology 2019 Abstract The effects of microwave (90 W and 180 W), northern parts of Iraq and Iran. In Turkey, 4352 tons of hot air (60 and 70 C) and vacuum (60 and 70 C with 200 medlar were harvested in 2017 according to Turkish Sta- and 300 mbar) drying methods on drying characteristics, tistical Institute (Akbulut et al., 2016, TUIK, 2018). Medlar total phenolic content, antioxidant capacity, color and is a potential source of ascorbic acid and natural antioxi- in vitro gastrointestinal digestion of medlar pestil were dants as well as including phenolics like chlorogenic acid, investigated. Medlar showed a good potential for pestil rutin and p-coumaric acid. Medlar fruits could be eaten raw production while being the most applicable in microwave or consumed in the form of jam, jelly, marmalade, wine, treatments. For drying kinetics, five thin-layer drying liquer and pickle. Fruits are likewise utilized in the therapy models were applied and the Page and Modified Page were of constipation and evacuation of kidney and bladder the best fitted models. L*, b*, chroma and hue angle stones. Fruit leather (pestil) is a traditional product formed decreased while a* generally increased in dried pestils. by the addition of sucrose and starch into the pulp and the Dried samples showed a general decrement in phenolics dehydration of fruit pulp into leathery sheets. As a result of and antioxidant capacity. According to in vitro gastroin- the increasing awareness of consumers in healthy food testinal digestion, intestinal phase of all the samples consumption, demand for value-added products has raised resulted with an increment in phenolics, FRAP and DPPH and pestil gained importance as being an economic source compared to undigested extracts. In conclusion, different of natural fruits with several nutrients (Chen and Marty- drying methods may affect the release of phenolics and nenko, 2018; Jaturonglumlert and Kiatsiriroat, 2010; Lee antioxidant capacity, while leading to increased bioacces- and Hsieh, 2008; Ruiz et al., 2014; Tontul and Topuz, sibility during intestinal digestion. 2017). Polyphenols are of great importance being in this group not only with health beneficial effects but also their Keywords Medlar  Pestil  Drying kinetics  In vitro intake and bioaccessibility. Bioaccessibility is defined as gastro intestinal digestion the quantity of nutrient delivered from food matrix. In this topic, the bioaccessibility of polyphenols are affected from molecular interactions between phenolics and other com- Introduction ponents, release from the food matrix and the chemical state of the compound as they are ingested as complex Mespilus germanica L., which is a member of Rosaceae mixtures. Besides, mechanical and thermal treatments may family, is commonly known as medlar. It is indigenous in result with the enhancement in digestibility and bioacces- southeastern Europe, Anatolia, Crimea, Caucasia and the sibility of nutrients (Lemmens et al., 2010). Drying of food is a complex thermal process including simultaneous heat and mass transfer in the product. & Senem Suna Advantages of thermal processing incorporate enzyme and syonak@uludag.edu.tr microbial inactivation, shelf life prolongation, enhanced 1 Department of Food Engineering, Faculty of Agriculture, digestibility and bioavailability of nutrients and antioxi- Bursa Uludag University, 16059 Nilüfer, Bursa, Turkey dants as well as the negative effects like loss of desirable 123 1466 S. Suna nutrients. To obtain a high quality dried product, drying Preparation of pestil method and time comes as the most important factors. In this shed of light, thin layer drying models are used for the Medlar fruits were washed, peeled, pitted and homoge- development of the system performance as well as allow- nized with a domestic blender (Beko, Turkey). Soluble ing the determination of the best operational conditions solid content (Brix) of the puree was 23 Bx. Freshly specific to different food or products (Sampaio et al., prepared puree (51%), distilled water (37%) and sucrose 2017). (10%) were boiled in an open kettle at constant stirring Evaluation of drying methods used in food industry then wheat starch (1.6%) and ascorbic acid (0.4%) were displays that, hot air drying is the quite common and added to the paste to obtain 42 Bx. Boiling was carried effective method, even though it has some disadvantages out for 15 min on average. Final brix of the mixture was such as the drying time continuation and low energy arranged according to similar studies like 40–50 Bx and effectiveness (Arslan and Ozcan, 2010). As an elective 50–55 Bx in pomegranate (Tontul and Topuz, 2017) and technique, vacuum drying is utilized at decreased pres- mango fruit leathers (Pushpa et al., 2006) respectively. sures, empowering food to be dried at lower temperatures. Afterwards, cooked medlar mixture (approximately 100 g) With this strategy, less oxidation responses happen because was evenly spread on a 10 9 10 cm square plastic mold of the nonappearance of air, while the sensorial properties stated on the greaseproof paper with a thickness of 4 mm of the dried foods are kept up. Microwave drying is another and dried under several conditions in hot air, microwave option with different focal points, such as a higher drying and vacuum drying techniques. After the each treatment, rate, homogeneous energy conveyance on the material and pestil samples were pulled from the surface, packaged with preferable process control. On the contrary, it may lead to a low density polyethylene film and stored at room tem- unequal warming and conceivable textural harm besides its perature until analyzed. high installation costs (Arslan and Ozcan, 2010; Maskan, 2001). Drying procedure There are so many literature about pestil production studied with diverse kinds of fruits, however, medlar has Three different methods (hot air, microwave and vacuum been evaluated with using advanced drying techniques for drying) were applied to the pestils and the drying experi- the first time. Besides, there are several scientific reports ments were carried out in triplicate. Hot air drying treat- about mathematical modelling of drying of several fruit ments were performed with a cabinet type laboratory dryer and vegetables and revealing the phenolic content and (Yucebas Machine Analytical Equipment Industry Y35, antioxidant capacity. To the best of the knowledge, this Izmir, Turkey) with the technical features of 220 V, research was the first in which drying kinetics of medlar 50–60 Hz, 200 W. The temperature and relative humidity fruit leather were studied with thin layer models and both in the dryer was measured by temperature sensor (± 2 C) the bioaccessibility of phenolic content and antioxidants and relative humidity sensor (± 2%). Drying was per- were reported via an in vitro digestion model. The first aim formed at temperatures of 60 and 70 C and a constant of this research was to produce a natural high quality 20% relative humidity. 50 g of pestil (10 9 10 cm square) medlar pestil and reveal the best drying parameters via with a thickness of 4 mm was placed on the greaseproof mathematical modelling of drying kinetics. The second aim paper as a thin layer. The temperatures were applied in was to determine the effects of different drying processes accordance with previous reports (Jaturonglumlert and on total phenolic content and antioxidant capacity and Kiatsiriroat, 2010; Pushpa et al., 2006; Tontul and Topuz, monitore their changes in the in vitro gastrointestinal track. 2017). All along drying, the samples were removed at intervals and weighed ahead being returned to the dryer. Pestil samples were weighed at 15 min intervals for 3 h Materials and methods and the loss of moisture was determined by weighing the plate using a digital balance (Mettler Toledo, MS3002S) Materials measuring to the accuracy of 0.01 g. Drying experiments were completed between 115 and 175 min depending on Mature medlar fruits were harvested on January 15, 2018 in the temperature. Bursa Turkey and left to storage at 4 ± C for a week to Microwave drying experiments were conducted in a get ripened and softened. Width and length of the fruits domestic microwave oven (Bosch, HMT72G420, Munich, were measured respectively as 3.10 ± 0.23 and Germany) with the technical features of 230 V–50 Hz and 3.58 ± 0.19 cm with a vernier caliper. maximum output of 800 W. The dimensions of the microwave cavity were 520 9 479 9 341 cm in size and it was consisted of a rotating glass plate of 315 mm diameter 123 Influence of drying methods on drying kinetics and bio accessibility of medlar pestils 1467 at the base of the oven. Drying treatments were performed where Mt and Mt?dt are the moisture contents at t and at 90 and 180 W microwave power levels. 50 g of pestil t ? dt (g water/g dry base) respectively, and t is drying samples stated on greaseproof paper were put on a rotating time (min). glass plate in the microwave oven. Drying was applied Root mean square error (RMSE) gives deviation between 16 and 60 min depending on the microwave between the estimated and experimental amounts for the power level. During drying, the rotating glass plate was models. The higher correlation coefficient (R2), and removed from the microwave oven at 5 and 1 min intervals reduced RMSE, Chi square (v2), were used to determine respectively at 90 and 180 W and weighed using a digital the goodness of fit model in the hot air, microwave and balance (Mettler Toledo, MS3002S) measuring to accuracy vacuum drying curves of pestil samples. These parameters of 0.01 g. can be determined with the subsequent equations: The vacuum drying experiments were carried out in a " # vacuum dryer (Memmert VO400, Germany, 49 L volume) XN   1=21 2 at 60 and 70 C; 200 and 300 mbar. The temperature and RMSE ¼ MRexp;i MRpre;i ð3ÞN vacuum levels were determined according to the literature i¼1   then 50 g of samples stated on the greaseproof paper were PN 2 2 i¼1 MRexp;i MRpre;i used (Paul and Das, 2018). The moisture loss of samples v ¼ ð4Þ N  n during drying was recorded at 15 min intervals for 4 h. Duration of drying process was recorded between 85 and where MRexp,i is the experimentally dimensionless mois- 230 min depending on the vacuum pressure. ture ratio for test i, MRest,i is the estimated dimensionless Moisture analyzer (Sartorius MA150, Germany) was moisture ratio for test i, N is the number of observation and used for the determination of moisture content of pestils. n is the number of constants in the model (Arslan and Drying experiments were all continued until the moisture Ozcan, 2010). content decreased to almost 0.08 g water/g dry base (initial moisture 1.49 g water/g dry base) and during drying Physicochemical analyses treatments all of the samples were weighed for a maximum duration of 10 s. Color analysis Mathematical modelling of drying curve Color of medlar pestils were determined by using a chroma meter (Konica Minolta CR-5, Bench-top, Japan). L*, a*, b* Five thin-layer mathematical drying models were utilized values were displayed as lightness, redness and yellowness. to choose the best model for portraying the drying curve of Chroma and hue angle were calculated from these values pestils. This models name and references were given (Mujumdar, 2000). respectively as Page MR = exp(-ktn) (Sarsavadiva et al., 1999), Modified Page MR = exp [(-kt)n] (Overhults Extraction of polyphenols et al., 1973), Logarithmic MR = a exp(-kt) ? c (Arslan and Ozcan, 2010), Lewis MR = exp(-kt) (Doymaz, 2006) Initial (undigested) extracts of medlar pestils were prepared and Handerson and Pabis MR = a exp(-kt) (Westerman according to Vitali et al. (2009). et al., 1973). The moisture ratio (MR) and drying rate of pestils In vitro bioaccessibility throughout drying were calculated using the consequent equations: In vitro digestion of medlar pestils was performed  according to Minekus et al. (2014). Samples were passed¼ M MeMR ð1Þ through a two-step gastrointestinal digestion stages as Mi Me stomach and intestinal phases. where MR is moisture ratio, M is the moisture content at a specific time (g water/g dry base), Mi corresponds to initial Total phenolic content moisture content (g water/g dry base), Me is the equilib- rium moisture content (g water/g dry base). Total phenolic content was determined by Folin–Ciocalteu  spectrophotometric method (Spanos and Wrolstad, 1990)Mtþdt Mt Drying rate ¼ ð2Þ and the results were expressed as mg gallic acid equiva- dt lents per 100 g dry weight (R2 = 0.9835). 123 1468 S. Suna Antioxidant capacity 180 W had the shortest one with 15 min. Microwave dry- ing spared the time by causing fast dissipation of water Antioxidant capacity of the medlar pestils was measured (Arslan and Ozcan, 2010; Zheng et al., 2012). In hot air with 2-diphenyl-1-picrylhydrazyl (DPPH) (Katalinic et al., drying, the time required to reduce the moisture was found 2006) Copper(II) reducing antioxidant capacity (CUPRAC) higher at 60 C with 175 min than 70 C with 115 min at a (Apak et al., 2008) and Ferric Reducing Antioxidant Power constant drying air with 20% relative humidity. Several (FRAP) (Benzie and Strain, 1996) methods. Trolox was authors reported that, increasing drying temperature speeds used as the calibration of the standard curves respectively up the drying process, thus shortens the drying time such as as R2 = 0.9929, R2 = 0.9987, R2 = 0.9993. The results in pomegranate (Tontul and Topuz, 2017) and rose hip were given as lmol Trolox equivalent (TE) per g dry leathers (Ruiz et al., 2014). Drying durations at 90 W and weight in all assays. 180 W were recorded as 60 min and 15 min respectively (Fig. 1A). These results explained that drying duration at Sensorial analysis 180 W was 75% less than the samples dried at 90 W. Furthermore in vacuum drying, treatments at 60 C Sensorial properties like color, appearance, taste, chewi- (125 min for 200 mbar and 230 min for 300 mbar) resulted ness and overall acceptability were analyzed. A 9-point with longer durations than 70 C (85 min for 200 mbar and hedonic scale varying from ‘‘like extremely (9)’’ to ‘‘dis- 115 min for 300 mbar). In the light of these data, incre- like extremely (1)’’ was used for the evaluation of the ment of the microwave power and temperature prompted samples (Lim, 2011). an impressive decrease in the drying durations. In vacuum drying technique, drying time decreased as the vacuum Statistical analysis increased (Fig. 2C). Furthermore, increase in both vacuum and temperature allowed decrease in the drying time by JMP software package version 8.0 (SAS Institute Inc. NC, accelerating moisture migration from the center to the 27513) was used for statistical evaluation. When significant outside. Identical behaviour was reported at vacuum drying differences were observed (p\ 0.05), the least significant of potato slices (Song et al., 2009) and hot air drying of and difference (LSD) test was used to determine the differences apples (Vega-Gálvez et al., 2012). among means in triplicate. The calculated drying rates of pestils were depicted in Fig. 2. Drying rates ranged from 0.01 [g water/g dry matter (min)] for experiments at 60 C–200 mbar vacuum to 0.15 Results and discussion [g water/g dry matter (min)] for the experiments at a microwave power level of 180 W. The drying rate of Drying characteristics of medlar pestils pestils raised with increasing temperature and power for both in hot air and microwave drying. Besides, drying rate Moisture ratio of the pestil samples obtained by Page’s accelerated with the increasing vacuum pressure and tem- equation as a function of drying time was shown in Fig. 1. perature. In microwave drying, a constant-rate period was The moisture ratio decreased considerably with increasing observed and constant rate varied from 0.6 to 1.4 (g water/g drying time as expected. Drying technique significantly dry matter) for a microwave power level of 90 W. For the affected total drying duration in order to obtain the final power of 180 W, a decrement was seen after a very short moisture content. Vacuum drying at 60 C–300 mbar had acceleration at the beginning. The rate of pestil drying with the longest duration with 230 min while microwave of hot air and vacuum methods generally decreased, and the Fig. 1 Moisture ratio of pestil samples versus drying time at microwave (A), hot air drying (B) and vacuum drying (C) conditions 123 Influence of drying methods on drying kinetics and bio accessibility of medlar pestils 1469 Fig. 2 Drying rate curves for pestils versus the moisture content at different microwave (A) hot air drying (B) and vacuum drying (C) drying process took place in a falling rate period (Wang (Table 2). While vacuum-70 C–200 mbar treated pestils et al., 2007) (Fig. 2B, C). Our results were in agreement had the nearest yellow color compared to non-dried sample with the study of strawberry fruit leather (Lee and Hsieh, (30.49 ± 0.22), hot air-60 C dried pestils were deter- 2008). mined as the least yellow samples (16.11 ± 0.98). Micro- wave dried samples showed lighter and yellower color Modelling of drying curves when compared to hot air, as a result of short drying period. Besides, in microwave drying, samples showed higher The statistical results of dried pestils obtained from dif- lightness and yellowness value with higher power, because ferent models including drying model coefficients, R2, of the lesser exposure to maillard and nonenzymatic RMSE and v2, were illustrated in Table 1. The R2, RMSE browning reactions amid drying. The red and yellow color and v2 values varied from 0.8820 to 0.9995, 0.001676 to of pestils is ascribed to the nearness of carotenes. In 0.111869 and 0.000048 to 0.155179, respectively. The addition to maillard reaction, the expansion of a value may suitable drying methods with the highest value of R2 and be because of the decomposition of pigments (Maskan, the lowest values of RMSE and v2 were determined from 2001). Page and Modified page models in all cases. Chroma value, which was used to perceive the color intensity, was significantly (p\ 0.05) the highest in non- Color properties dried sample. Vacuum 70 C–200 mbar treatment showed the second highest result (35.82 ± 0.45) while the lowest General color of pestils was depicted as yellowish orange value (24.48 ± 1.19) was determined from hot air-60 C. and L* was found statistically significant (p\ 0.05) In compliance with chroma, non-dried mixture resulted (Table 2). Non-dried mixture showed the highest L* and with the highest amount, and the second highest and the stated in the same group with 200 mbar vacuum treatments lowest values of hue angle were calculated from the same at 70 C and 60 C. When compared to non-dried mixture, treatments (Table 2). Consequently, vacuum drying had the L* value was significantly affected by different drying best color properties. This was associated with vacuum treatments (p\ 0.05) and resulted with a 1.51–30.83 77% conditions, in which the damp material is dried under sub- decrease. Additionally, L* of pestils were raised with atmospheric pressures, counteracted color damages and increasing microwave power resulting with a lighter color. permitted to be in higher quality than conventional air At the point when high powers were utilized, drying was process at atmospheric pressure (Krokida and Maroulis, performed in a shorter time so color was more substantially 1999). saved (Pushpa et al., 2006). Furthermore, pestils dried with hot air presented darker color as a result of the exposure to Effects of different drying methods on total high temperature all along the time of drying. polyphenolic content and antioxidant capacity The highest a* values were found to be significantly the in the in vitro gastrointestinal tract same in vacuum drying (300 mbar) at 70 and 60 C with 20.71 ± 0.17 and 20.38 ± 0.36 respectively. Compared to The initial total phenolic content of the mixture before the fresh sample, a* increased with vacuum 300 mbar drying was determined as being the highest with treatments at 60 and 70 C whereas this value reduced in 396.62 mg GAE/100 g dw (p\ 0.05). Phenolic content hot air (60 C) and vacuum 60 C–200 mbar treatments. after drying was affected by the method (p\ 0.05) with a b* value was significantly the highest in non-dried mixture decrease ranging from 50.59% (hot air-60 C) to 60.65% 123 1470 S. Suna Table 1 Statistical results obtained from the modeling of medlar pestils Model name Applications Model coefficients R2 RMSE v2 Page Hot air 60 C n = 1.2299, k = 0.0054 0.9918 0.002510 0.000968 Hot air 70 C n = 1.1233, k = 0.0132 0.9970 0.003635 0.000152 Vacuum 60 C–200 mbar n = 1.2667, k = 0.0058 0.9968 0.003588 0.000173 Vacuum 70 C–200 mbar n = 1.2124, k = 0.0117 0.9887 0.007801 0.000596 Vacuum 60 C–300 mbar n = 0.793, k = 0.0215 0.9953 0.035260 0.026401 Vacuum 70 C–300 mbar n = 1.1606, k = 0.0120 0.9983 0.002785 0.000089 Microwave-90 W n = 1.5652, k = 0.0056 0.9967 0.004170 0.000267 Microwave-180 W n = 1.7027, k = 0.031 0.9995 0.001775 0.000054 Modified page Hot air 60 C n = 1.2299, k = 0.0143 0.9981 0.002510 0.000096 Hot air 70 C n = 1.1233, k = 0.0212 0.9970 0.003635 0.000152 Vacuum 60 C–200 mbar n = 1.2667, k = 0.0171 0.9968 0.003588 0.000173 Vacuum 70 C–200 mbar n = 1.2124, k = 0.0256 0.9887 0.007801 0.000596 Vacuum 60 C–300 mbar n = 0.7930, k = 0.0079 0.9952 0.035260 0.026401 Vacuum 70 C–300 mbar n = 1.1606, k = 0.0638 0.9983 0.081725 0.077285 Microwave-90 W n = 1.5652. k = 0.0364 0.9967 0.004170 0.000267 Microwave-180 W n = 1.6930, k = 0.1296 0.9994 0.001676 0.000048 Logarithmic Hot air 60 C k = 0.0265, a = 1.4861 0.9541 0.045217 0.034554 Hot air 70 C k = 0.0347, a = 1.2778 0.9581 0.040614 0.022268 Vacuum 60 C–200 mbar k = 0.0321, a = 1.5084 0.8927 0.055795 0.047086 Vacuum 70 C–200 mbar k = 0.0394, a = 1.213 0.9365 0.042717 0.022354 Vacuum 60 C–300 mbar k = 0.0220, a = 1.3341 0.9662 0.024239 0.013257 Vacuum 70 C–300 mbar k = 0.0355, a = 1.3150 0.9536 0.042756 0.024679 Microwave-90 W k = 0.0803, a = 1.7878 0.9303 0.071605 0.086652 Microwave-180 W k = 0.3085, a = 2.2436 0.8820 0.090909 0.155179 Lewis Hot air 60 C k = 0.0165 0.9909 0.012723 0.002279 Hot air 70 C k = 0.0233 0.9922 0.111869 0.001267 Vacuum 60 C–200 mbar k = 0.0202 0.9643 0.017957 0.003901 Vacuum 70 C–200 mbar k = 0.0297 0.9619 0.021268 0.003694 Vacuum 60 C–300 mbar k = 0.0072 0.9858 0.041929 0.035259 Vacuum 70 C–300 mbar k = 0.0251 0.9875 0.013446 0.001830 Microwave-90 W k = 0.0480 0.9528 0.030132 0.012787 Microwave-180 W k = 0.1730 0.9259 0.028986 0.013503 Henderson and Pabis Hot air 60 C k = 0.0176, a = 1.1388 0.9958 0.011970 0.002201 Hot air 70 C k = 0.0245, a = 1.1100 0.9957 0.013836 0.002215 Vacuum 60 C–200 mbar k = 0.0220, a = 1.2462 0.9784 0.024603 0.008138 Vacuum 70 C–200 mbar k = 0.0327, a = 1.2045 0.9732 0.032325 0.010240 Vacuum 60 C–300 mbar k = 0.0059, a = 1.2278 0.9893 0.081752 0.141925 Vacuum 70 C–300 mbar k = 0.0268, a = 1.1539 0.9932 0.018471 0.003948 Microwave-90 W k = 0.0555, a = 1.3710 0.9781 0.032637 0.016365 Microwave-180 W k = 0.2127, a = 1.5595 0.9691 0.039872 0.027515 RMSE root mean square error, R2 correlation coefficient (microwave-90 W) (Table 3). The lowering effect of dry- to the results of total antioxidant capacity, a general ing on phenolics can be ascribed to the degradation and decrement both in CUPRAC (0.31–57.34%), DPPH oxidation during heat treatment (Qu et al., 2010). Similar (53.39–57.32%) and FRAP (54.37–56.83%) assays was decrement was reported in blueberry and rose hip leathers determined in undigested extracts. Microwave-180 W (Chen and Martynenko, 2018; Ruiz et al., 2014). According (125.77 ± 6.00) was found significantly (p\ 0.05) higher 123 Influence of drying methods on drying kinetics and bio accessibility of medlar pestils 1471 Table 2 Color values of medlar pestil samples Drying processes L* a* b* Chroma Hue angle Non-dried mixture 49.52 ± 0.00a 18.52 ± 0.01de 34.14 ± 0.01a 38.84 ± 0.02a 61.52 ± 0.02a Hot air-60 C 34.25 ± 1.27c 18.42 ± 0.73e 16.11 ± 0.98f 24.48 ± 1.19f 41.15 ± 0.61e Hot air-70 C 35.36 ± 0.25c 19.34 ± 0.25cd 18.92 ± 0.27f 27.06 ± 0.36e 44.37 ± 0.20d Microwave-90 W 35.51 ± 0.96c 18.94 ± 0.60cde 19.01 ± 0.51f 26.84 ± 0.47e 45.12 ± 1.35d Microwave-180 W 42.03 ± 0.36b 19.61 ± 0.72bc 24.54 ± 0.78g 31.42 ± 1.06d 51.38 ± 0.15c Vacuum 60 C–200 mbar 48.28 ± 1.28a 18.27 ± 0.47e 28.87 ± 0.19c 34.12 ± 0.29c 57.76 ± 0.51b Vacuum 70 C–200 mbar 48.77 ± 0.63a 18.80 ± 0.49cde 30.49 ± 0.22b 35.82 ± 0.45b 58.34 ± 0.48b Vacuum 60 C–300 mbar 42.75 ± 0.44b 20.38 ± 0.36ab 26.07 ± 0.28d 33.10 ± 0.19c 51.98 ± 0.72c Vacuum 70 C–300 mbar 41.93 ± 0.05b 20.71 ± 0.17a 26.18 ± 0.16d 33.38 ± 0.21c 51.65 ± 0.19c a–gDifferent letters in the same column display significant difference (p\ 0.05) than other samples in CUPRAC assay with the nearest (65.15–85.24%) and DPPH (10.19–18.71%) compared to result to non-dried mixture. DPPH analysis of the pestils undigested extracts. In agreement with current data, greater were found statistically significant (p\ 0.05). Microwave- total phenolic content from intestinal phase than stomach 90 W (6.87 ± 0.01), vacuum 70 C 300 mbar phase and initial extracts in tomato sauce using the same (6.81 ± 0.07) and vacuum 60 C 300 mbar (6.78 ± 0.01) in vitro digestion method was reported (Tomas et al., revealed the highest results as well as showing no signifi- 2018). Moreover, Oliveira and Pintado (2015) determined cant differences (p[ 0.05). In FRAP analysis, microwave- an increase in antioxidant capacity of strawberry and peach 90 W (23.19 ± 0.54) was significantly (p\ 0.05) higher yoghurt in the intestinal phase compared to non-digested than those of the other samples with the lowest decrement extracts, which is consistent with current DPPH analysis. (54.37%) compared to non-dried mixture. This study supported that the bioaccessible phenolics Ruiz et al. (2014) reported trolox equivalent antioxidant increased during intestinal digestion. This situation was capacity (TEAC) of hot-air dried rose hip leathers in explained previously that, by the entrance in the colon average as 24 and 17 lmol TE/g dm (dry matter) respec- phenolics could be catabolized by human gut microbiata tively in 60 C and 70 C treatments. Additionally TEAC into low molecular compounds allowing them to be of rose hip leathers were presented as 33 and 21 lmol TE/g absorbed throughly (González-Sarrı́as et al., 2017). In dry matter in vacuum drying at 60 C and 70 C. These general, current data showed that applied drying methods results were in accordance with CUPRAC analysis being and treatments (microwave: 90 W and 180 W, hot air: 60 higher in hot air drying at 60 C than 70 C (Table 3) and and 70 C, vacuum: 60 and 70 C with 200 and 300 mbar) the mean interval of current data. Chen and Martynenko may have an influence on the release of total phenols and (2018) reported DPPH results of dried blueberry leather antioxidant capacity, therefore, on the bioaccessible frac- between 59.19 and 71.92 lmol TE/g dm in freeze and tion. Moreover, both undigested (initial) and in vitro forced-air dried samples. digested pestil samples measured by CUPRAC and FRAP The effect of in vitro digestion on total phenolic content methods were found to be higher than DPPH assay. Results and total antioxidant capacity of the pestils was presented of CUPRAC could be attributed to the properties of the in Table 3. During stomach phase, changes in phenolics of reagent being selective and stable as well as the Cu(I) ion all the samples were statistically significant (p\ 0.05). emerging as a product of the CUPRAC cannot then act as a Generally for all the treatments except for microwave prooxidant (Apak et al., 2008). Besides, lower results of (90 W and 180 W) and vacuum 200 mbar (60 C and DPPH can be explained with the method’s characteristics, 70 C), results were decreased in stomach phase compared which targets sterically hindered radicals than biologically to initial values. Additionally a declining trend was active short-lived ones (Schaich et al., 2015). observed after simulated gastric digestion in CUPRAC, DPPH and FRAP (p\ 0.05) in accordance with Tomas Sensorial properties et al. (2018) both in these three assays. Remarkably, total phenolic content from intestinal phase was higher than Pestils dried at 70 C with a vacuum of 200 mbar had the stomach phase and initial extracts in all of the samples. highest color scores (Table 4). 60 C–200 mbar resulted Intestinal phase of all the samples resulted with an incre- with the highest values of appearance and taste criterias. ment in total phenolic content (49.42–97.15%) FRAP While the chewiness of pestils were found the highest in 123 1472 S. Suna Table 3 Changes in the total Analysis Initial Stomach phase Intestinal phase phenolic content and total antioxidant capacity of pestil TPC samples during simulated a a a in vitro digestion Non-dried mixture 396.62 ± 3.84 366.83 ± 4.53 672.79 ± 21.03 Hot air-60 C 195.94 ± 1.07b 168.38 ± 4.56d 292.78 ± 7.50d Hot air-70 C 186.73 ± 7.61bc 172.81 ± 6.16cd 318.35 ± 7.98bc Microwave-90 W 156.06 ± 9.31g 167.26 ± 6.15d 307.68 ± 5.25bcd Microwave-180 W 159.25 ± 2.07fg 174.96 ± 4.78cd 309.84 ± 4.43bc Vacuum 60 C–200 mbar 168.11 ± 2.93ef 180.30 ± 6.64bc 293.27 ± 7.49d Vacuum 70 C–200 mbar 181.37 ± 9.42cf 188.23 ± 6.48b 304.46 ± 7.26cd Vacuum 60 C–300 mbar 187.74 ± 7.39bc 166.19 ± 8.30d 305.15 ± 7.69cd Vacuum 70 C–300 mbar 173.86 ± 1.27de 170.92 ± 5.68cd 323.52 ± 3.00b CUPRAC Non-dried mixture 126.16 ± 24.11a 46.55 ± 9.99f 57.73 ± 8.34c Hot air-60 C 96.10 ± 9.72b 93.41 ± 5.24ab 64.85 ± 7.18c Hot air-70 C 70.22 ± 8.58b 89.42±5.83bc 95.55 ± 4.84a Microwave-90 W 69.14 ± 8.13c 48.80 ± 5.65ef 35.50 ± 3.69d Microwave-180 W 125.77 ± 6.00a 101.93 ± 6.20a 82.28 ± 9.60b Vacuum 60 C–200 mbar 98.19 ± 7.40b 62.77 ± 6.42d 84.19 ± 8.38ab Vacuum 70 C–200 mbar 98.40 ± 8.30b 80.96 ± 6.87c 69.28 ± 9.98c Vacuum 60 C–300 mbar 55.49 ± 9.19c 37.48 ± 7.55f 25.80 ± 6.68d Vacuum 70 C–300 mbar 53.81 ± 5.94c 60.59 ± 6.36de 33.23 ± 3.75d DPPH Non-dried mixture 14.74 ± 0.03a 12.95 ± 0.11a 15.47 ± 0.23a Hot air-60 C 6.51 ± 0.12d 5.82 ± 0.10c 7.43 ± 0.12bcde Hot air-70 C 6.67 ± 0.07c 5.75 ± 0.06c 7.35 ± 0.15cde Microwave-90 W 6.87 ± 0.01b 5.88 ± 0.11bc 7.76 ± 0.43b Microwave-180 W 6.29 ± 0.01e 5.86 ± 0.13bc 7.27 ± 0.18de Vacuum 60 C–200 mbar 6.30 ± 0.06e 5.55 ± 0.02d 7.18 ± 0.09e Vacuum 70 C–200 mbar 6.47 ± 0.01d 6.04 ± 0.09b 7.68 ± 0.15bc Vacuum 60 C–300 mbar 6.78 ± 0.01b 5.91 ± 0.20bc 7.56 ± 0.18bcd Vacuum 70 C–300 mbar 6.81 ± 0.07b 5.85 ± 0.09bc 7.51 ± 0.09bcde FRAP Non-dried mixture 50.83 ± 0.40a 46.00 ± 0.65a 80.41 ± 0.85a Hot air-60 C 22.93 ± 0.22bc 20.25 ± 0.04b 39.39 ± 0.52cde Hot air-70 C 22.79 ± 0.50bcd 20.18 ± 0.57b 39.94 ± 1.13bcd Microwave-90 W 23.19 ± 0.54b 20.44 ± 0.26b 38.30 ± 0.18e Microwave-180 W 22.29 ± 0.46cd 20.92 ± 0.28b 41.29 ± 0.92b Vacuum 60 C–200 mbar 21.94 ± 0.62d 20.14 ± 0.40b 39.23 ± 1.49de Vacuum 70 C–200 mbar 22.31 ± 0.28bcd 20.92 ± 0.48b 40.71 ± 0.72bc Vacuum 60 C–300 mbar 22.92 ± 0.85bc 19.95 ± 0.47b 39.76 ± 0.35cd Vacuum 70 C–300 mbar 22.94 ± 0.45bc 20.30 ± 0.29b 39.41 ± 0.19cde TPC (total phenolic content) and total antioxidant capacity (CUPRAC, DPPH, FRAP) is expressed as mg of GAE (gallic acid equivalent) per 100 g dw and lmol of TE (Trolox equivalent) per g dw respectively Different letters in the same column display significant difference (p\ 0.05) hot air-60 C, the second highest scores were obtained had the lowest scores of all the criterias and the increased from vacuum (200 mbar) treatments at 60 C and 70 C. microwave power resulted with lower sensorial scores Similarly, overall acceptances of pestils were found as the (Pushpa et al., 2006). The results of sensorial analysis best in vacuum (200 mbar) treatments at 60 C and 70 C. showed that, although microwave-180 W had the lowest Additionally, drying at microwave with a power of 180 W 123 Influence of drying methods on drying kinetics and bio accessibility of medlar pestils 1473 Table 4 Sensorial properties of medlar pestils Drying processes Color Appearance Taste Chewiness Overall acceptability Hot air-60 C 6.50 ± 1.76b 7.50 ± 1.22a 7.83 ± 1.47a 8.33 ± 0.51a 7.66 ± 1.21a Hot air-70 C 7.66 ± 0.51ab 7.33 ± 0.81a 7.00 ± 1.54ab 7.66 ± 0.51abc 7.50 ± 0.83a Microwave-90 W 4.00 ± 2.00c 4.16 ± 1.83b 6.16 ± 0.98bc 7.00 ± 0.63cd 5.66 ± 0.81b Microwave-180 W 3.66 ± 1.86c 3.33 ± 2.16b 4.66 ± 1.50c 6.50 ± 0.83d 5.16 ± 0.75b Vacuum 60 C–200 mbar 8.00 ± 1.54ab 8.66 ± 0.81a 8.16 ± 0.98a 8.16 ± 1.16ab 8.16 ± 0.98a Vacuum 70 C–200 mbar 8.50 ± 1.22a 8.00 ± 1.54a 8.00 ± 1.26a 8.16 ± 1.16ab 8.16 ± 1.32a Vacuum 60 C–300 mbar 7.00 ± 0.89ab 7.33 ± 0.81a 7.00 ± 1.26ab 7.33 ± 0.81bcd 7.50 ± 0.54a Vacuum 70 C–300 mbar 6.66 ± 1.03b 7.33 ± 0.81a 7.50 ± 1.51ab 7.66 ± 0.81abc 7.66 ± 1.03a a–dDifferent letters in the same column display significant difference (p\ 0.05) scores, all of the samples resulted in acceptable properties Lee G, Hsieh F. 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