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Ciência Rural

versão impressa ISSN 0103-8478versão On-line ISSN 1678-4596

Cienc. Rural vol.49 no.10 Santa Maria  2019  Epub 03-Out-2019

https://doi.org/10.1590/0103-8478cr20170430 

FOOD TECHNOLOGY

Optimization of the osmotic dehydration of ginger

Otimização da desidratação osmótica do gengibre

Leonardo Pereira de Siqueira1 

Leonie Asfora Sarubbo2 

Neide Kazue Sakugawa Shinohara1 

Marcela Sarmento Valencia3 

Neila Mello Santos Cortez3 
http://orcid.org/0000-0002-2778-3944

Samara Alvachian Cardoso Andrade3 

1Universidade Federal Rural de Pernambuco (UFRPE), Recife, PE, Brasil.

2Universidade Católica de Pernambuco (UNICAP), Recife, PE, Brasil.

3Universidade Federal de Pernambuco (UFPE), Recife, PE, Brasil.


ABSTRACT:

The present research aimed to optimize the process of osmotic dehydration (OD) of ginger with hypertonic sucrose solution employing response surface methodology. A 23 experimental planning was carried out and 17 experimental assays were performed based on three independent variables (temperature, concentration of the osmotic solution and immersion time) and three dependent variables (moisture loss (ML), solids gain (SG) and dehydration efficiency index (DEI)). The selected assay conditions exhibited the preferred DEI value (the highest ML and lower SG), which were considered in the optimization. Assay 16 demonstrated to be the most favorable conditions for the osmotic dehydration of ginger (DEI =1.61) at 40 40 °C, 50 °Brix and 90 minutes of immersion time. Assay 1 performed at 34 °C, 44 °Brix and 120 minutes of immersion time also displayed desirable response (DEI =1.45). Thus, these two assays were evaluated for the presence of thermal-tolerant coliforms: Bacillus cereus and Salmonella sp.. The analyses presented values below the acceptable limits, which assured high quality hygienic and sanitary conditions of the product.

Key words: Zingiber officinale Roscoe; water loss; microbiological analysis

RESUMO:

A presente pesquisa teve como objetivo otimizar o processo de desidratação osmótica (DO) do gengibre, com solução hipertônica de sacarose, pelo método de superfície de resposta. Foi utilizado um planejamento fatorial 23 completo, totalizando 17 ensaios, tendo como variáveis independentes: temperatura, concentração da solução osmótica e tempo de imersão e variáveis dependentes, como,: perda de umidade (PU), ganho de sólidos (GS) e índice de eficiência de desidratação osmótica (IED). Para otimizar foi considerado o melhor ensaio, o que obteve maior IED, ou seja, maior PU e menor GS. As melhores condições para a desidratação osmótica de gengibre foram obtidos a 40 °C, 50 °Brix e 90 minutos de imersão (Ensaio 16) com IED de 1.61 vindo em seguida o Ensaio 1 (34 ºC, 44 ºBrix e 120 minutos de imersão) com IED de 1.45. Estes ensaios foram avaliados quanto à coliformes tolerantes térmicas, Bacillus cereus e Salmonella spp., apresentando valores abaixo dos limites aceitáveis, indicando boas condições higiênicas sanitárias do produto.

Palavras-chave: Zingiber officinale; perda de água; análise microbiológica

INTRODUCTION:

Ginger (Zingiber officinalle) is native to Tropical Asia and the Malay Archipelago, but has been cultivated as a monoculture worldwide. In Brazil, the main crops are from Paraná and Santa Catarina, which together export approximately 70% of the national production to the Netherlands, Canada, Germany, and the United States (KIZHAKKAYIL & SASIKUMAR, 2011).

Quality of ginger rhizomes is commonly affected after harvesting as a result of weight loss, wilting, surface wrinkling, physiological deterioration, attack of pathogens and physicochemical alterations in compounds such as a decrease in protein and crude fiber levels. These events can lead to lower product value and shelf-life (GARCÍA-TOLEDO et al., 2016).

The OD is a mass-transfer operation where water is partially removed through the immersion of products in hypertonic aqueous solutions such as syrups or brines and it may be a feasible alternative to increase shelf-life of products of plant origin (SIMPSON et al., 2015). Immersion of a product in a hypertonic solution creates a chemical gradient between the external and internal environment as the result of different osmotic potentials. During a dynamic period in the mass transfer process, water is transported from the food to the solution and, simultaneously, the solute is deposited on the product’s surface (SOURAKI et al., 2014).

This operation has been widely studied in food processing and it has been used as an alternative for the pre-treatment of jenipapo (ANDRADE et al., 2007), radish (HERMAN-LARA et al., 2013) and cherry tomatoes (DEROSSI et al., 2015) because it can contribute to improving the quality of the final product (PEREIRA et al., 2006) regardless the reduction of some nutrients such as vitamins and minerals (CHAVARRO - CASTRILLÓ et al., 2006). In addition, OD is considered an energy-efficient method because water is removed from the product at mild temperatures (HERMAN-LARA et al., 2013).

Hence, this research aimed to optimize the process conditions of osmotic dehydration of ginger using response surface methodology with a hypertonic sucrose solution.

MATERIALS AND METHODS:

Samples of fresh ginger rhizomes (Zingiber officinale) were randomly purchased in local markets (Recife, PE, Brazil) after being visually selected by color, size, and absence of physical damage. Granulated white sugar (União Coopersucar, Limeira, SP, Brazil) was used as the osmotic agent. After being properly sanitized, ginger roots were peeled, sliced 0.2 cm thick, and weighed. These samples were subsequently immersed in the osmotic sucrose solution and placed in a shaker (Marconi, MA-410) at 160 rpm with controlled temperature and time. The assays were carried out in 600 mL sealed cylindrical glass containers. Approximately 20 g of ginger were dehydrated in 400 g of hypertonic solution (1:20 sample/solution ratio) to ensure the constant concentration in the osmotic solution.

An experimental study evaluated a 2³ factorial planning with eight factorial points (± one level), three central points (level 0), and six axial points (± α), totaling 17 assays. The independent variables were: temperature (T), osmotic solution concentration (C), and immersion time (t). The dependent variables were: moisture loss (ML), solid gain (SG), and the ML/SG ratio = DEI. The obtained data were fitted to a polynomial function described by Equation 1 where β n are the regression coefficients, y is the response of interest (ML, SG, and ML/SG), and T, C, and t are the independent variables.

Y = φ(T,t,C) = β0 + β1T + β2C + β3t + β11T2 + β22C2 + β33t2 + β12TC + β13Tt + β23Ct (1)

The evaluated conditions are presented in Levels (-α, -1, 0, 1 and +α). The decoded levels of the independent variables are: Level -α (30 °C, 40 °Brix, and 90 minutes of immersion time); level -1 (34 °C, 44 °Brix, and 120 min of immersion time); level 0 (40 °C, 50 °Brix, and 165 min of immersion time); level 1 (46 °C, 56 °Brix, and 210 min of immersion time), and level +α (50 °C, 60 °Brix, and 240 min of immersion time).

The responses of interest were calculated as it is shown in Equations 2-4.

ML%=100xUiMi-UfMfMi (2)

SG%=100xBfMf-BiMiMi (3)

DEI=MLSG (4)

Where: (3)Mi= initial mass (g); Mf = final mass (g); ML = moisture loss (%); Ui= initial moisture content (%); Uf= final moisture content (%); SG = solid gain (%); Bi = initial soluble solids content in the material (ºBrix); Bf = final content of soluble solids in the material (ºBrix); and DEI = dehydration efficiency index

The analytical determinations were performed in triplicate, before and after each osmotic treatment. Total soluble solids were determined by direct reading on a bench-top refractometer (AUS JENA). Moisture content (M) was determined at 105 °C (AOAC, 2002; Method 985.14), and weight (W) was measured on an analytical balance. Statistical data analyses were performed in “Statistic for Windows 6.0” software (STATSOFT, 2002) at 5% significance.

The presence of thermal-tolerant coliforms (NMP/mL) (AOAC, 2002; Method 991.14), Bacillus cereus CFU/g (AOAC, 2002), and Salmonella sp. (AOAC, 2002; Method 996.08) was evaluated in the microbiological analysis according to the provisions of Resolution - RDC n° 12 from January 2, 2001 (BRAZIL, 2001). The amounts of thermal-tolerant coliforms were determined in raw sample and the three samples which presented the highest DEI values in factorial planning assays in order to guarantee the microbiological safety of these products.

RESULTS AND DISCUSSION:

The experimental results from 17 assays for ML, SG, and DEI are shown in table 1. During ginger OD, the ML values were higher than the SG values in most of the assays. These results corroborate with the findings of SILVA et al. (2014) and BARBOSA JÚNIOR et al., (2013) reporting the osmotic dehydration of pineapple and melon in sucrose solution, respectively. Lower SG values in osmotic dehydration are desirable since when SG values are higher than ML values, larger is the probability of modifications in the characteristics of the final product.

Table 1 Results obtained for ML, SG, and DEI in the 23 factorial planning of ginger osmotic dehydration. 

Assay ------------------------------------Independent variables---------------------------------- --------------Dependent variables--------------
Temperature (ºC) ºBrix Immersion time (min.) ML (%) SG (%) DEI
1 34 44 120 42.13 28.96 1.45
2 46 44 120 37.30 35.32 1.06
3 34 56 120 50.18 38.56 1.30
4 46 56 120 50.08 41.8 1.20
5 34 44 210 38.33 33.25 1.15
6 46 44 210 31.51 39.8 0.79
7 34 56 210 50.86 38.4 1.32
8 46 56 210 46.99 45.3 1.04
9 40 50 165 45.67 37.56 1.21
10 40 50 165 45.99 36.8 1.25
11 40 50 165 44.62 37.9 1.18
12 30 50 165 41.36 40.26 1.03
13 50 50 165 42.47 47.89 0.89
14 40 40 165 31.52 31.57 0.99
15 40 60 165 55.99 39.9 1.40
16 40 50 90 48.94 30.35 1.61
17 40 50 240 44.09 36.9 1.19

*°Brix: concentration of soluble solids; min: minutes; ML: Moisture loss; SG: Solid gain; DEI: Dehydration efficiency index.

According to table 1, the highest ML (55.99%) response was obtained in assay 15 (40 °C, 60 °Brix, and 165 min of immersion time), although the lowest SG value (28.96%) was achieved in assay 1 (34 °C, 44 °Brix, and 120 min of immersion time). The elevated moisture loss observed in the results of assay 15 may be related to the high concentration of the osmotic solution applied. An increase in the concentration of the osmotic solution implies an enhancement of osmotic pressure gradient and, consequently, higher mass transfer rates (SILVA et al., 2014). The SG value observed in assay 1 may be related to the conditions of low temperature, concentration, and immersion time. SG has a tendency to increase as the dehydration time and temperature increases. Therefore, shorter times and inferior temperatures lead to less structural changes in the product (MOURA, 2004).

The ideal level of solute absorption strongly depends on the purpose of the process and the desired characteristics in the final product. Thus, elevated DEI is indicative of a treatment that aims a large level of dehydration and low solid absorption (MATUSKA et al., 2006). Since this work aimed to maximize ML and minimize SG, the selected responses for ginger OD with sucrose were those obtained in assay 16 (DEI = 1.61) with 48.94% ML and 30.35% SG, followed by assay 1 (DEI = 1.45) with ML 42.13% and 28.96% SG and assay 15 (DEI = 1.40) with 55.99% ML and 39.90% SG. Therefore, assay 1 demonstrated the best osmotic conditions (34 °C, 44 °Brix, and 120 min of immersion time) with the lowest SG values, which leads to a product that is the closest to that in natura.

Regression analysis was applied to model the values of dependent variables as quadratic functions of the osmotic solution concentration, temperature, and immersion time (Table 3). The effects of the independent variables on ML, SG, and DEI are presented in table 2. According to the data, the osmotic solution concentration displayed the greatest influence on ML, i.e., the increase in the osmotic agent concentration favored ML, which can be observed in figure 1 (a). This behavior may be attributed to the fact that the increase in the solution viscosity results in greater osmotic pressure, boosting the output of water from the food. However, based on the immersion time, this variable had little influence on ML (Figure 1). These results corroborate those found by ABRAÃO et al. (2013) when studying the influence of osmotic dehydration parameters on the quality of pumpkins.

Table 2 Effects of independent variables on ML, SG, and DEI. 

ML p SG p DEI p
β0 45.47 0.000 37.43 0.000 1.21 0.000
β1 -2.03 0.035 5.27 0.003 -0.20 0.009
β11 -2.77 0.023 4.71 0.005 -0.19 0.012
β2 13.22 0.001 5.99 0.002 0.16 0.014
β22 NS 0.078 NS 0.063 NS 0.460
β3 -2.96 0.017 3.40 0.008 -0.21 0.008
β33 NS 0.339 -2.81 0.014 0.12 0.027
β12 NS 0.063 NS 0.224 NS 0.065
β13 NS 0.105 NS 0.137 NS 0.270
β23 NS 0.071 NS 0.076 0.11 0.049
R2 0.965 0.984 0.908

*NS: not-significant (p>0.05); ML: Moisture loss (%); SG: Solid gain (%), and DEI: Dehydration efficiency index. The regression coefficients represent: β0 = average; β1 = the linear term of temperature; β11 = the quadratic term of temperature; β2 = the linear term of osmotic solution concentration; β22 = the quadratic term of osmotic solution concentration; β3 = the linear term of immersion time; β33 = the quadratic term of osmotic solution concentration; β12 = term of the interaction between temperature and concentration of the osmotic solution; β13 = term of the interaction between temperature and concentration of the osmotic solution; β23 = term of the interaction between osmotic solution concentration and immersion time; R2 = determination coefficient.

Figure 1 Response surface for: (a) moisture loss(%) as a function of osmotic solution concentration (°Brix) and immersion time (minutes); (b) solid gain(%) as a function of osmotic solution concentration (°Brix) and temperature (°C); and (c) Dehydration efficiency index(DEI) as a function of temperature (ºC) and immersion time(minutes). 

It can be observed that the osmotic solution concentration (°Brix) and temperature were the variables with the greatest influence on SG (Table 2), i.e., the increase in osmotic agent concentration and temperature induced an increase in SG values, which are graphically represented in figure 1. These findings are in accordance with those found by KHUMAR et al. (2012) on the osmotic dehydration of lychee, where the temperature was found to be the main variable to influence SG. According to the authors, increased processing temperature leads to decreased viscosity in the sugar solution, improving the mass transfer rates between the material and the hypertonic solution. Similar results were also reported by GENINA-SHAI et al. (2011) in a study on the effect of temperature and different concentrations of sucrose solutions during the osmotic dehydration of sweet potato cubes.

Elevated SG values in the process of osmotic dehydration are undesirable because they can lead to alterations in the product’s sensory properties. Furthermore, when the impregnated solute concentration in plant tissues is high, the efficiency of dehydration is reduced due to the formation of an external barrier for the mass transfer mechanism (BORIN et al., 2008). However, there are processes when the incorporation of solutes on the surface of the product is desirable, such as the impregnation processes, in which the presence of solute provides desirable properties (BARBOSA JÚNIOR et al., 2013).

From the data in table 2, it can also be highlighted that temperature and immersion time had a significant influence on DEI (p < 0.05). Figure 1 (c) shows that the greatest DEI value was observed with the shortest immersion time and temperature of 40 °C. The graph in Figure 1 (c) features downward concavity, which results from the negative quadratic term for temperature influence. According to ANDRADE et al. (2003) and TONON et al. (2006), when temperature increases above the threshold of plant tissue growth, it may cause damage that prevents water diffusivity and compromises the efficiency of the osmotic process.

The results from the analysis of variance (Table 3) show that the models adjusted to ML, SG, and DEI were predictive and presented significant regression and non-significant lack of fit. The coefficients of determination (R2) were higher than 0.90 in all models, which means that the percentages of variation explained by the models were greater than 90%.

Table 3 Variance analysis for the model adjusted to ML, SG, and DEI. 

--------------------------------------------------------------------------------------ML------------------------------------------------------------------------------------
Source of variation DF QS QA Fcalculated Ftabled
Regression 4 657.478 164.369 40.267 3.26
Residue 12 48.981 4.082
Lack of fit 10 47.954 4.795 9.347 19.4
Pure error 2 1.027 0.513
Total 16 R2 = 0.965
--------------------------------------------------------------------------------------SG-------------------------------------------------------------------------------------
Source of variation DF QS QA Fcalculated Ftabled
Regression 5 338.096 67.619 42.61 3.20
Residue 11 17.463 1.587
Lack of adjustment 9 16.829 1.870 5.90 19.4
Pure error 2 0.634 0.317
Total 16 R2= 0.984
---------------------------------------------------------------------------------------DEI-----------------------------------------------------------------------------------
Source of variation DF QS QA Fcalculated Ftabled
Regression 6 0.539 0.090 10.84 3.22
Residue 10 0.083 0.0083
Lack of adjustment 8 0.081 0.010 10 19.4
Pure error 2 0.002 0.001
Total 16 R2= 0.907

*ML: Moisture loss; SG: Solid gain; DEI: Dehydration efficiency index; DF: Degrees of freedom; QS: Quadratic sum; QA: Quadratic average; R2= Determination coefficient.

Ginger in natura and the two osmotically dehydrated ginger samples resulting from the assays 1 and 16 are in accordance with the standards established by Resolution RDC N° 12 (BRAZIL, 2001) for the presence of thermal-tolerant microorganisms (total coliforms NMP/mL, Bacillus cereus/g, and Salmonella sp./25 g) indicating the appropriate sanitary and hygienic conditions of these products.

The advantages of osmotic dehydration are demonstrated in the acquisition of products with intermediate moisture, improved texture, and reduced losses of sensorial characteristics. Moreover, the reduction in energy costs in the subsequent stages of OD and the low-cost process are also valuable features in the OD process. Conversely, nutrient losses and solids gains are observed, which alter the in natura nutritional profile of the food.

The removal of moisture in the dehydration process favors the reduction of microbial activity and it provides a longer shelf-life product since microbiological and enzymatic activities are at acceptable levels. Furthermore, it is worth mentioning that the hygienic-sanitary procedures and best practices throughout product treatment are of great importance in the prevention of diseases and quality of the final product through the reduction of natural microbial loads present on plant surfaces.

CONCLUSION:

The evaluation of parameters involved in the osmotic dehydration of ginger demonstrated that the concentration of the osmotic solution has a great influence on moisture loss and solids gains. Moreover, the dehydration efficiency index is greatly influenced by temperature and immersion time. The best conditions for the osmotic dehydration of ginger were obtained at 40 °C, 50 °Brix, and 90 minutes of immersion time with DEI of 1.61 and 34 °C, 44 °Brix, and 120 minutes with DEI of 1.45. These assays were evaluated for the presence of thermal-tolerant coliforms, Bacillus cereus and Salmonella sp., and attested good hygienic and sanitary conditions in the dehydration of the product. Hence, the osmotic dehydration of ginger is a viable, applicable, cost-effective, and relatively simple technique that may be used by small industries or rural producers providing options with the potential of expanding this commercialization of the crop.

ACKNOWLEDGEMENTS

And was financed in part by the Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES), Brasil - Finance code 001.

REFERENCES

ABRAÃO, A.S. et al.Influence of osmotic dehydration process parameters on the quality of candied pumpkins. Food and Bioproducts Processing, v.91, n.4, p.481-494, 2013. Available from: <Available from: https://doi.org/10.1016/j.fbp.2013.04.006 >. Accessed: Jan. 15, 2016. doi: 10.1016/j.fbp.2013.04.006. [ Links ]

ANDRADE, S. A. C. et al. Osmotic dehydration of Jenipapo (Genipa americana L.). Ciência e Tecnologia de Alimentos, v.23, n.2, p.276-281, 2003. Available from: <Available from: http://dx.doi.org/10.1590/S0101-20612003000200029 >. Accessed: Jan. 15, 2016. doi: 10.1590/S0101-20612003000200029. [ Links ]

ANDRADE, S.A.C.et al.Influência de revestimentos comestíveis na redução de ganho de sólidos em jenipapos desidratados osmoticamente. Ciência e Tecnologia de Alimentos, v.27, n.1, p.39-43, 2007. Available from: <Available from: http://dx.doi.org/10.1590/S0101-20612007000100007 >. Accessed: Mar. 25, 2016. ISSN 0101-2061. [ Links ]

AOAC. Association of Official Analytical Chemistry: Official Methods of Analysis (13. ed.). Washington:AOAC, 2002. [ Links ]

BARBOSA JÚNIOR et al. Mass transfer kinetics and mathematical modelling of the osmotic dehydration of orange-fleshed honeydew melon in corn syrup and sucrose solutions. International Journal of Food Science & Technology, v.48, n.12, p.2463-2473, 2013. Available from: <Available from: http://onlinelibrary.wiley.com/doi/10.1111/ijfs.12237/full >. Accessed: Mar. 03, 2016. doi: 10.1111/ijfs.12237. [ Links ]

BRASIL, Agência Nacional de Vigilância. Resolução - RDC nº 12, de 02 de janeiro de 2001. Regulamento técnico sobre padrões microbiológicos para alimentos. Diário Oficial da República Federativa do Brasil. 2001. [ Links ]

BORIN, I.et al. Efeito do pré-tratamento osmótico com sacarose e cloreto de sódio sobre a secagem convectiva de abóbora. Ciência Tecnologia de Alimentos, v.28, n.1, 39-50, 2008. Available from: <Available from: http://dx.doi.org/10.1590/S0101-20612008000100008 >. Accessed: Mar. 10, 2016. doi: 10.1590/S0101-20612008000100008. [ Links ]

CHAVARRO - CASTRILLÓN et al. Efecto de la madurez, geometria y presión sobre la cinética de transferência de massaem La deshidratación osmóica de papaya (Carica papaya L., var. Maradol). Ciência e Tecnologia de Alimentos, Campinas, v.26, n.3, p596-603, 2006. Available from: <Available from: http://dx.doi.org/10.1590/S0101-20612006000300018 >. Accessed: Mar. 10, 2016. ISSN 1678-457X. [ Links ]

DEROSSI, A. et al. Study and optimization of osmotic dehydration of cherry tomatoes in complex solution by response surface methodology and desirability approach. Food Science and Technology, v.60, n.2, p.641-648, 2015. Available from: <Available from: http://www.sciencedirect.com/science/article/pii/S0023643814006914 >. Accessed: Mar. 12, 2016. doi: 10.1016/j.lwt.2014.10.056. [ Links ]

GARCÍA-TOLEDO, J.A. et al. Effect of osmotic dehydration on the physical and chemical properties of Mexican ginger (Zingiber officinale var. Gran Cayman). Journal of Food, v.14, n.1, p.27-34, 2016. Available from: <Available from: http://dx.doi.org/10.1080/19476337.2015.1039068 >. Accessed: Jun. 10, 2016. doi: 10.1080/19476337.2015.1039068. [ Links ]

HERMAN-LARA, E. et al.Mass transfer modeling of equilibrium and dynamic periods during osmotic dehydration of radish in NaCl solutions. Food and Bioproducts Processing, v.91, n.3, p.216-224. 2013. Available from: <Available from: http://dx.doi.org/10.1016/j.fbp.2012.10.001 >. Accessed: Jan. 05, 2016. doi: 10.1016/j.fbp.2012.10.001. [ Links ]

KIZHAKKAYIL, J.;SASIKUMAR, B. Diversity, characterization and utilization of ginger: a review. Plant Genetic Resources, v.9, n.3, p.464-477, 2011. Available from: <Available from: http://dx.doi.org/10.1017/S1479262111000670 >. Accessed: Jan. 10, 2016. doi: 10.1017/S1479262111000670. [ Links ]

MATUSKA, M. et al.On the use of edible coatings to monitor osmotic dehydration kinetics for minimal solids uptake.Journal of Food Engineering, v.72, n.1, p.85-91. 2006. Available from: <Available from: http://dx.doi.org/10.1016/j.jfoodeng.2004.11.023 >. Accessed: Mar. 05, 2016. doi: 10.1016/j.jfoodeng.2004.11.023. [ Links ]

PEREIRA, L.M. et al.Kinetic aspects, texture, and color evaluation of some tropical fruits during osmotic dehydration. Drying Technology, v.24, n.4, p.475-484, 2006. Available from: <Available from: http://dx.doi.org/10.1080/07373930600611968 >. Accessed: May, 27, 2016. doi: 10.1080/07373930600611968. [ Links ]

SILVA, K.S. et al. Osmotic dehydration of pineapple with impregnation of sucrose, calcium, and ascorbic acid. Food and Bioprocess Technology, 7(2), 385-397, 2014. Available from: <Available from: http://link.springer.com/article/10.1007/s11947-013-1049-0 >. Accessed: May, 27, 2016. doi: 10.1007/s11947-013-1049-0. [ Links ]

SIMPSON, R. et al. Diffusion mechanisms during the osmotic dehydration of Granny Smith apples subjected to a moderate electric field. Journal of Food Engineering, v.166, p.204-211, 2015. Available from: <Available from: http://dx.doi.org/10.1016/j.jfoodeng.2015.05.027 >. Accessed: May, 05, 2016. doi: 10.1016/j.jfoodeng.2015.05.027. [ Links ]

SOURAKI, B.A. et al. Correction of moisture and sucrose effective diffusivities for shrinkage during osmotic dehydration of apple in sucrose solution. Food and Bioproducts Processing, v.2, n.1, p.1-8, 2014. Available from: <Available from: http://dx.doi.org/10.1016/j.fbp.2013.07.002 >. Accessed: May, 27, 2016. doi: 10.1016/j.fbp.2013.07.002. [ Links ]

Statsoft, Inc. STATISTICA for Windows 6.0 [Computer program manual], Tulsa- UK: StatSoft, 2002. [ Links ]

TONON, R.V. et al. Estudo da Desidratação osmótica de Tomate em Soluções Ternárias pela Metodologia de Superfície de Resposta. Ciência Tecnologia de Alimentos, v.3, n.26, p.715-723, 2006. Available from: <Available from: http://www.scielo.br/pdf/cta/v26n3/31780 >. Accessed: Jun. 10, 2016. doi: 10.1590/S0101-20612006000300036. [ Links ]

CR-2017-0430.R5

Received: July 27, 2017; Accepted: May 29, 2019; Revised: September 14, 2019

E-mail: neilacortez@yahoo.com.br. *Corresponding author

DECLARATION OF CONFLICT OF INTERESTS

The authors declare that they have no conflict of interest. The founding sponsors had no role in the design of the study, nor in the data collection, analyses, or interpretation of data, the writing of the manuscript, nor the decision to publish the results.

AUTHORS’ CONTRIBUTIONS

The authors contributed equally to the manuscript.

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