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Quality of ‘Royal Gala’ cut apple during osmotic dehydration

Qualidade de maçã Royal Gala cortada durante a desidratação osmótica

Abstract

The present work aimed to evaluate quality parameters of ‘Royal Gala’ apple cubes during osmotic dehydration (OD). We investigated the following OD conditions: osmotic agent, pressure, and temperature. The osmotic agent, being lower after OD with sorbitol than sucrose solutions, mainly influenced the water activity of the product. The color changes increased with increased temperature and were higher in vacuum experiments than at atmospheric pressure. In general, we recommend OD at 25 °C and atmospheric pressure for the preservation of the total phenolic content (TPC) and antioxidant activity (AA) of apple cubes during the process. Peleg’s model was found to provide the best fit of TPC and AA data.

Keywords:
Osmotic agent; Pressure; Vacuum; Sorbitol; Sucrose; Water activity; Color; Total phenolic content; Antioxidant activity; Mathematical models

Resumo

O objetivo do presente trabalho foi avaliar parâmetros de qualidade de cubos de maçã Royal Gala durante o processo de desidratação osmótica (DO). As condições de operação da DO investigadas foram: o agente osmótico, a pressão e a temperatura. A atividade de água do produto foi influenciada principalmente pelo agente osmótico, sendo menor após DO com soluções de sorbitol do que de sacarose. Alterações de cor aumentaram com o incremento da temperatura e foram maiores nas experiências a vácuo do que à pressão atmosférica. Em geral, DOs a 25 °C e à pressão atmosférica são recomendadas para a conservação do teor em fenóis totais (TFT) e da atividade antioxidante (AA) dos cubos de maçã durante o processo. O modelo de Peleg permitiu o melhor ajuste dos dados experimentais de TFT e AA.

Palavras-chave:
Agente osmótico; Pressão; Vácuo; Sorbitol; Sacarose; Atividade da água; Cor; Teor em fenóis totais; Atividade antioxidante; Modelos matemáticos

1 Introduction

In 2015, more than 95% Brazilian apple orchards cultivated Gala apples, including ‘Royal Gala’ (Ávila et al., 2015Ávila, S., Ito, V., Denardi, F., Nogueira, A., & Wosiacki, G. (2015). Brazilian apple production twenty years later. Fruit Processing, 1, 24-28.). In order to present a longer shelf life, sometimes it is beneficial that the fruits undergo pre-treatment, such as osmotic dehydration (OD). This process is becoming popular in the food industry because it improves the sensorial and nutritional properties of foods, with a reduced loss of aroma in semi dried and dried food stuffs (Khan, 2012Khan, M. R. (2012). Osmotic dehydration technique for fruits preservation: A review. Pakistan Journal of Food Sciences, 22, 71-85.).

OD consists of immerging a fruit or vegetable in a hypertonic solution of salt, alcohol, starch or concentrate sugar, which has a higher osmotic pressure than the food. The osmotic pressure is the driving force for the mass transfer of water and solutes between the food and the osmotic solution (Ramya & Jain, 2017Ramya, V., & Jain, N. K. (2017). A review on osmotic dehydration of fruits and vegetables: An integrated approach: osmo-dehydration of fruits and vegetables. Journal of Food Process Engineering, 40(3), 1-22. http://dx.doi.org/10.1111/jfpe.12440
http://dx.doi.org/10.1111/jfpe.12440...
; Shi & Le Maguer, 2002Shi, J., & Le Maguer, M. (2002). Osmotic dehydration of foods: Mass transfer and modeling aspects. Food Reviews International, 18(4), 305-335. http://dx.doi.org/10.1081/FRI-120016208
http://dx.doi.org/10.1081/FRI-120016208...
). Osmotically dehydrated products have a water activity in the range of 0.90-0.95. Normally, these products require further processing in order to extend their shelf life.

Sucrose is the most used osmotic agent in the OD of fruits due to its effectiveness, convenience and desirable flavor (Ahmed et al., 2016Ahmed, I., Qazi, I. M., & Jamal, S. (2016). Developments in osmotic dehydration technique for the preservation of fruits and vegetables. Innovative Food Science & Emerging Technologies, 34, 29-43. http://dx.doi.org/10.1016/j.ifset.2016.01.003
http://dx.doi.org/10.1016/j.ifset.2016.0...
; Lenart, 1996Lenart, A. (1996). Osmo-convective drying of fruits and vegetables: technology and application. Drying Technology, 14(2), 391-413. http://dx.doi.org/10.1080/07373939608917104
http://dx.doi.org/10.1080/07373939608917...
). Alternative solutes, such as sorbitol, have also been used (Brochier et al., 2014Brochier, B., Marczak, L. D. F., & Noreña, C. P. Z. (2014). Osmotic dehydration of bacon using glycerol and sorbitol as solutes: water effective diffusivity evaluation. Food and Bioprocess Technology, 8(3), 623-636. http://dx.doi.org/10.1007/s11947-014-1432-5
http://dx.doi.org/10.1007/s11947-014-143...
; Chauhan et al., 2011Chauhan, O. P., Singh, A., Singh, A., Raju, P. S., & Bawa, A. S. (2011). Effects of osmotic agents on color, textural, structural, thermal, and sensory properties of apple slices. International Journal of Food Properties, 14(5), 1037-1048. http://dx.doi.org/10.1080/10942910903580884
http://dx.doi.org/10.1080/10942910903580...
; Rodríguez et al., 2013). Sorbitol is one of the polyols naturally found in several fruits and it was one of the first to become commercially available (Assis et al., 2017aAssis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
). Aprea et al. (2017)Aprea, E., Charles, M., Endrizzi, I., Laura Corollaro, M., Betta, E., Biasioli, F., & Gasperi, F. (2017). Sweet taste in apple: The role of sorbitol, individual sugars, organic acids and volatile compounds. Scientific Reports, 7(1), 44950. PMid:28322320. http://dx.doi.org/10.1038/srep44950
http://dx.doi.org/10.1038/srep44950...
reported sorbitol contents in some of the apple varieties (except Royal Gala) of a maximum of 12.9 g/kg. Sorbitol is described as non-cariogenic. In the food industry, sorbitol is used as a sweetener (E420). It has 60% of the sweetness of sucrose and it has a lower caloric value: it gives the consumers 2.6 kcal per gram (EU) instead of 4 kcal per gram given by sucrose. Another health property is related to sorbitol producing no significant post-prandial hyperglycemia, which is a positive aspect for a diabetic diet (Ellis & Krantz, 1943Ellis, F. W., & Krantz, J. C. (1943). Sugar alcohols XXIV. The metabolism of sorbitol in diabetes. Annals of Internal Medicine, 18(5), 792-796. http://dx.doi.org/10.7326/0003-4819-18-5-792
http://dx.doi.org/10.7326/0003-4819-18-5...
). Sorbitol has molecular mass lower than sucrose, and osmotic agents with low molecular mass find less resistance to penetrate into the fruit cell tissues. Assis et al. (2017a)Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
showed that a 60 °Brix sorbitol solution had lower viscosity than a sucrose solution with the same concentration. Sorbitol was found to be a better osmotic agent than fructose to obtain pulsed vacuum osmotically dehydrated bacon slices with a higher fructan retention (Oliveira et al., 2016Oliveira, L. F., Corrêa, J. L. G., Pereira, M. C. A., Ramos, A. L. S., & Vilela, M. B. (2016). Osmotic dehydration of bacon (Smallanthus sonchifolius): optimization for fructan retention. Lebensmittel-Wissenschaft + Technologie, 71, 77-87. http://dx.doi.org/10.1016/j.lwt.2016.03.028
http://dx.doi.org/10.1016/j.lwt.2016.03....
).

The present work aimed to evaluate quality parameters, such as water activity, color, total phenolic content (TPC) and antioxidant activity (AA) of ‘Royal Gala’ apple cubes during the OD at different conditions of osmotic agent, pressure, and temperature using sucrose and sorbitol.

2 Material and methods

2.1 Samples

Apples (Malus spp., variety Royal Gala) were graciously supplied by Campotec, Portugal, and stored at 4 °C. The apple cubes (12 mm) were prepared according to Assis et al. (2017a)Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
. The soluble solids content of the apple was 16.2 ± 1.2 °Bx (hand refractometer, Atago, China).

2.2 Osmotic dehydration process

The OD process was carried out with sucrose or sorbitol solutions at 60 °Brix and a mass ratio of sample to solution of 1:4 and at a constant agitation of 50 rpm (Assis et al., 2017aAssis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
). The experiments with the sucrose solution were performed first at 25, 40 and 60 °C, at atmospheric pressure and in vacuum (hermetic containers at 150 mbar). After analysis of the results, the experiments with the sorbitol solution were set up at 25 and 60 °C.

The apples samples were removed from the solution at different times and selected quality parameters were evaluated in the apple cubes.

The experiments were performed in duplicate.

2.3 Moisture content (Md)

The samples moisture content in dry basis was determined in an oven (FP115, Binder, Tuttlingen, Germany) and calculated through the Equation 1:

M d = w s w d w d (1)

ws(g) is the initial weight of the apple cubes; wd(g) is the weight of the apple cubes after 24 hours at 105 °C in the oven.

The moisture content was evaluated in triplicate.

Afterwards, Md was normalized by dividing it by Md,0, because the initial value of the apple sample was different for each experiment.

2.4 Quality evaluation

2.4.1 Water activity (aw)

The aw of the samples was determined during the process, using a hygrometer (Aqualab Series 3, Decagon Devices Inc., Pullmam, Washington, USA) at 22 °C. Each determination was performed in duplicate.

2.4.2 Color

Samples color was determined in the CIE L*a*b* color space (Commission Internationale de L’eclairage, 1978Commission Internationale de L’Eclairage – CIE. (1978). Recommendations on uniform color spaces: Color-difference equations, psychometric color terms (Publ., No. 15, Suppl. 2). Paris: CIE.), using a Minolta CR-300 colorimeter (Minolta Camera Co., Ltd., Osaka, Japan). Three replicates were used for each sample. The total color difference (ΔE) was calculated through the Equation 2:

ΔE = L 0 * L * 2 + a 0 * a * 2 + b 0 * b * 2 (2)

the index “0” indicating the sample before OD.

2.4.3 Total Phenolic Content (TPC)

The apples samples were ground in liquid nitrogen with a mortar. Subsequently, we weighed 2 g of each sample, and added 10 mL of methanol (Sigma Aldrich, Steinheim, Switzerland); the mixture was then homogenized using an ultra-turrax (T25, IKA, Breisgau, Germany) for 2 min. The supernatant was used after centrifugation at 5000 rpm and 4 °C for 15 min (Chong et al., 2013Chong, C. H., Law, C. L., Figiel, A., Wojdylo, A., & Oziemblowski, M. (2013). Color, phenolic content and antioxidant capacity of some fruits dehydrated by a combination of different methods. Food Chemistry, 141(4), 3889-3896. PMid:23993562. http://dx.doi.org/10.1016/j.foodchem.2013.06.042
http://dx.doi.org/10.1016/j.foodchem.201...
).

The total phenolic content was determined by the Folin-Ciocalteu method (Singleton & Rossi, 1965Singleton, V., & Rossi, J. A. (1965). Colorimetry of total phenolics with phosphormolybdic-phosphotungstic acid reagents. American Journal of Enology and Viticulture, 16, 144-158.). The reaction was performed by adding 0.5 mL of apple extract, 0.5 mL of Folin-Ciocalteu reagent, 1 mL of sodium carbonate 75 (g L−1) (Sigma-Aldrich) and 1.4 mL of deionized water. After 1 h in the dark at room temperature, the TPC was determined at 750 nm in a spectrophotometer (Shimadzu UV-vis 1240, Japan). Quantification was performed with respect to the standard curve of the gallic acid. The determinations were carried out in triplicate.

2.4.4 Antioxidant Activity (AA)

The ABTS method was used to determine the AA (Gião et al., 2007Gião, M. S., González-Sanjosé, M. L., Rivero-Pérez, M. D., Pereira, C. I., Pintado, M. E., & Malcata, F. X. (2007). Infusions of Portuguese medicinal plants: Dependence of final antioxidant capacity and phenol content on extraction features. Journal of the Science of Food and Agriculture, 87(14), 2638-2647. PMid:20836172. http://dx.doi.org/10.1002/jsfa.3023
http://dx.doi.org/10.1002/jsfa.3023...
). After addition of 1 mL of the ABTS+ solution (absorbance = 0.700 ± 0.02) to 0.2 mL of extract, the analysis was performed after 6 min at 734 nm and expressed as mg ascorbic acid/g dry matter. The determinations were performed in triplicate.

2.5 Mathematical models

The following models were used to fit the TPC and AA data.

Peleg’s model

TPC TPC 0 or AA AA 0 = 1 t k 1 + k 2 t (3)

Page’s model

TPC TPC 0 or AA AA 0 = exp A t B (4)

A and B, and k1 and k2 being Page’s and Peleg’s model parameters, respectively; the index “0” indicating the sample before OD.

2.6 Statistical analysis

The statistical analysis was performed using Microsoft Excel 2000 (Microsoft Corporation, Washington, USA) (mean and standard deviation calculations) and IBM SPSS® Statistics 20.0 for Windows® (2012, SPSS Inc., Chicago, USA). The model parameters of the experimental data fit were estimated by non-linear regression procedures, and the estimates margin of error was calculated at 95% (the margin of error is the half width of the confidence interval at 95%). The regressions were also assessed by ANOVA approaches, assuming a significance level of 5%.

The adequacy of the models fit was evaluated by the determination coefficient (R2) and by the residual analysis. The residual analysis was performed in order to check the assumptions of independence, randomness and normality. The normality of the residuals was evaluated by Kolmogorov-Smirnov test.

3 Results and discussion

The aw decreased during OD (results not shown). This is important for safety issues. This decrease in aw was confirmed by Assis et al. (2017a)Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
during OD of apple cubes. OD with sorbitol solutions produced apple cubes with significantly lower aw than with sucrose solutions, which is in agreement with Assis et al. (2017a)Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
. The aw of the apple cubes osmotically dehydrated with sorbitol was 0.892-0.914, while the samples osmotically dehydrated with sucrose presented a aw of 0.933-0.944. No effect of the pressure on aw was found in the present work. Vieira et al. (2012)Vieira, G. S., Pereira, L. M., & Hubinger, M. D. (2012). Optimisation of osmotic dehydration process of guavas by response surface methodology and desirability function. International Journal of Food Science & Technology, 47(1), 132-140. http://dx.doi.org/10.1111/j.1365-2621.2011.02818.x
http://dx.doi.org/10.1111/j.1365-2621.20...
found that aw was mainly affected by temperature. They also found that a higher vacuum pulse time (at least 20 min) also favored a aw decrease.

When the OD is carried out at atmospheric pressure, ΔE was lower than when the apple cubes were osmotically dehydrated in vacuum (Figure 1). Color differences between samples osmotically dehydrated in vacuum and at atmospheric pressure were visually perceived. The highest ΔE corresponds to the highest changes in L* (results not shown), both at atmospheric pressure and in vacuum. Neri et al. (2016)Neri, L., Di Biase, L., Sacchetti, G., Di Mattia, C., Santarelli, V., Mastrocola, D., & Pittia, P. (2016). Use of vacuum impregnation for the production of high quality fresh-like apple products. Journal of Food Engineering, 179, 98-108. http://dx.doi.org/10.1016/j.jfoodeng.2016.02.002
http://dx.doi.org/10.1016/j.jfoodeng.201...
and Moreno et al. (2017)Moreno, J., Zúñiga, P., Dorvil, F., Petzold, G., Mella, K., & Bugueño, G. (2017). Osmodehydration assisted by ohmic heating/pulse vacuum in apples (cv. Fuji): Retention of polyphenols during refrigerated storage. International Journal of Food Science & Technology, 52(5), 1203-1210. http://dx.doi.org/10.1111/ijfs.13385
http://dx.doi.org/10.1111/ijfs.13385...
explained that the L* parameter decreased more in OD in vacuum than at atmospheric pressure, because of the total or partial air-to-solution replacement in the sample pores that occurred with vacuum impregnation, at pressures below 857 mbar.

Figure 1
Total color difference (ΔE) of apple cubes during the osmotic dehydration in 60 °Brix sucrose and sorbitol solutions at atmospheric and vacuum (150 mbar) pressures, and at 25 and 60 °C (Md,0 was 6.58±0.99 kg water/kg DM).

There was an increase in ΔE at 60 °C, probably due to Maillard reactions, which are more intense at higher temperatures and lower aw (until approximately 0.8) (Fennema, 1996Fennema, O. R. (1996). Water and ice. In O. R. Fennema (Ed.), Food chemistry (3rd ed., pp. 17-94). New York: Marcel Dekker.). Enzymatic browning by polyphenol oxidase could have occurred at room temperature within 15 minutes after cutting (Tuccillo, 2018Tuccillo, F. (2018). Color variations of ‘Royal Gala’ and ‘Golden Delicious’ apple surface due to enzymatic browning and its inhibition: Experimental findings. Bra, Italy: Università degli Studi di Scienze Gastronomiche.). However, a proper pre-treatment was performed to avoid this browning process: immediately after cutting, the cubes were immersed in a solution with 0.9% sodium chloride for 3 min (Assis et al., 2017aAssis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
).

The highest color change (ΔE) was, therefore, observed in cubes osmotically dehydrated at 60 °C in vacuum and the smallest one at 25 °C and atmospheric pressure. The use of sorbitol showed a tendency to induce a higher ΔE than sucrose, especially at high temperatures.

After 8 h of osmotic treatment in the sucrose solution at 60 °C and atmospheric pressure, the losses of TPC and AA of apple cubes were around 75% (Figures 2 and 3), in agreement with Assis et al. (2017b)Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017b). Microwave drying of apple cubes: effect of the osmotic pre-treatment and comparison with hot air drying. Advances in Food Science and Engineering, 1, 112-122.. These losses were around 60% at 40 °C and 40% at 25 °C.

Figure 2
Experimental data and the fit of Peleg’s model for normalized total phenolic content of apple cubes during the osmotic dehydration in a 60 °Brix sucrose solution at atmospheric and vacuum (150 mbar) pressures and at 25, 40 and 60 °C (TPC0 = 4.77 ± 1.04 mg gallic acid/ g DM).
Figure 3
Experimental data and the fit of Peleg’s model for normalized AA of apple cubes during the osmotic dehydration in a 60 °Brix sucrose solution at atmospheric and vacuum (150 mbar) pressures and at 25, 40 and 60 °C (AA0 = 7.42 ± 1.21 mg ascorbic acid/g DM).

In general, both Peleg’s and Page’s models fitted well the experimental data of the antioxidant activity (AA) and total phenolic content (TPC) of apple cubes during OD, as high determination coefficients (R2) were obtained (Table 1) and the residual analysis showed that the residuals are normally distributed at a 5% significance level. The visual analysis of the scatterplot of residuals versus predicted values allowed noting that the residuals were distributed randomly around zero with no systematic pattern, satisfying the assumption of homoscedasticity and zero mean errors. Therefore, we selected the best fit based on the precision of parameter estimation, calculated though the Standard Half Width (SHW = margin of error/ parameter value) at 95% confidence. The average SHW was 20% and 27% for AA and 21% and 30% for TPC, for Peleg’s and Page’s models, respectively. Thus, Peleg's model described better the evolution of AA and TPC of apples cubes during OD, with the highest precision of parameter estimates (lowest SHW) for all conditions tested (Figures 2 -5, Table 1). None of these models fitted well the TPC of apple cubes during the OD with sucrose solution at 40 °C and vacuum (Figure 2). Therefore, we did not take this condition into account in the comparison of the process variables. In addition, none of the models fitted ΔE data well, because they did not follow one or more of the assumptions described above.

Table 1
Parameters of the fit of Peleg’s and Page’s models of the antioxidant activity (AA) and total phenolic content (TPC) of apple cubes during OD.
Figure 4
Experimental data and the fit of Peleg’s model for normalized total phenolic content of apple cubes during the osmotic dehydration in a 60 °Brix sorbitol solution at atmospheric and vacuum (150 mbar) pressures and at 25 and 60 °C (TPC0 = 4.77 ± 1.04 mg gallic acid/g DM).
Figure 5
Experimental data and the fit of Peleg’s model for normalized antioxidant activity of apple cubes during the osmotic dehydration in a 60 °Brix sorbitol solution at atmospheric and vacuum (150 mbar) pressures and at 25 and 60 °C (AA0 = 7.42 ± 1.21 mg ascorbic acid/ g DM).

The value of -1/k1 (Peleg’s model) gives the initial rate of the kinetics of the TPC and AA. Based on this, it could be observed that the process variables (type of solute, pressure and temperature) did not affect the kinetics of TPC. The value of 1-1/k2 is the equilibrium value given by Peleg’s model (Equation 3). The TPC at equilibrium did not follow a clear pattern and, in most conditions, the process variables did not affect the final TPC. The same trend was observed with respect to the parameters of Page’s model (Equation 4). Concerning the AA, k1 and A parameters tend to present the same behavior. Based on Figures 2 -5, OD condition of 25 °C and atmospheric pressure seems to preserve TPC and AA of apple cubes better during the process. These results on the quality of osmotically dehydrated apple cubes go along with the findings on the OD process rate, which increases when temperature increases (Assis et al., 2017aAssis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017a). Mathematical modelling of osmotic dehydration kinetics of apple cubes. Journal of Food Processing and Preservation, 41, e12895. http://dx.doi.org/10.1111/jfpp.12895
http://dx.doi.org/10.1111/jfpp.12895...
). As in the present work, Assis et al. (2017bAssis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017b). Microwave drying of apple cubes: effect of the osmotic pre-treatment and comparison with hot air drying. Advances in Food Science and Engineering, 1, 112-122., 2018Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2018). Osmotic dehydration combined with freeze-drying of apple cubes and comparison with microwave drying and hot air drying. Advances in Food Science and Engineering, 21(1), 38-47. http://dx.doi.org/10.22606/afse.2018.21005
http://dx.doi.org/10.22606/afse.2018.210...
) did not find a significant difference neither in TPC nor in AA between OD in sucrose and sorbitol solutions after 8 h at the same conditions.

4 Conclusions

The water activity of apple cubes was lower after osmotic dehydration (OD) with sorbitol solutions. The highest color changes were found in the vacuum experiments.

Peleg’s model was the most adequate to fit the total phenolic content (TPC) and antioxidant activity (AA) during the OD process.

In order to prevent color changes and preserve TPC and AA of apple cubes, we recommend OD at atmospheric pressure and 25 °C. Sorbitol did not seem to affect these parameters in relation to sucrose.

Acknowledgements

This work was supported by National Funds from FCT - Fundação para a Ciência e Tecnologia through project UID/Multi/50016/2013. The first author acknowledges the financial support by the ERASMUS program. The second author acknowledges the financial support by CAPES (1528/13-0). The authors also acknowledge Campotec for graciously supplying the apples for this study.

  • Cite as: Pieters, B., Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2020). Quality of ‘Royal Gala’ cut apple during osmotic dehydration. Brazilian Journal of Food Technology, 23, e2019059. https://doi.org/10.1590/1981-6723.05919
  • Funding: Coordenação de Aperfeiçoamento de Pessoal de Nível Superior -1528/13-0 and Ministério da Educação e Ciência /Fundação para a Ciência e a Tecnologia - UID/Multi/50016/2013.

References

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    » http://dx.doi.org/10.1016/j.ifset.2016.01.003
  • Aprea, E., Charles, M., Endrizzi, I., Laura Corollaro, M., Betta, E., Biasioli, F., & Gasperi, F. (2017). Sweet taste in apple: The role of sorbitol, individual sugars, organic acids and volatile compounds. Scientific Reports, 7(1), 44950. PMid:28322320. http://dx.doi.org/10.1038/srep44950
    » http://dx.doi.org/10.1038/srep44950
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    » http://dx.doi.org/10.1111/jfpp.12895
  • Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2017b). Microwave drying of apple cubes: effect of the osmotic pre-treatment and comparison with hot air drying. Advances in Food Science and Engineering, 1, 112-122.
  • Assis, F. R., Morais, R. M. S. C., & Morais, A. M. M. B. (2018). Osmotic dehydration combined with freeze-drying of apple cubes and comparison with microwave drying and hot air drying. Advances in Food Science and Engineering, 21(1), 38-47. http://dx.doi.org/10.22606/afse.2018.21005
    » http://dx.doi.org/10.22606/afse.2018.21005
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    » http://dx.doi.org/10.1007/s11947-014-1432-5
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Publication Dates

  • Publication in this collection
    13 Mar 2020
  • Date of issue
    2020

History

  • Received
    25 Mar 2019
  • Accepted
    08 Nov 2019
Instituto de Tecnologia de Alimentos - ITAL Av. Brasil, 2880, 13070-178 Campinas - SP / Brasil, Tel 55 19 3743-1762 - Campinas - SP - Brazil
E-mail: bjftsec@ital.sp.gov.br