Research noteApplication of the Guggenheim, Anderson and De Boer model to correlate water activity and moisture content during osmotic dehydration of apples
Introduction
In the context of minimal processing, the measurement and prediction of water activity provide the best available tool for evaluating the stability of foods. The sorption isotherm, consisting of a graphic representation of water activity (aw) against moisture content at constant temperature, is a common way of presenting the relationship between these two parameters (McLaughlin & Magee, 1998; Rahman & Labuza, 1999). Desorption isotherms are of particular importance in the design of a food dehydration process, especially in the determination of a drying end point. The end point of drying is the residual moisture content of the final product which ensures economic viability and microbiological safety, i.e. a water activity value lower than 0.60. Desorption isotherms focus therefore on low moisture or intermediate moisture zones, because this is the range of moisture content of the food product after drying methods such as air-drying and freeze-drying. The effect of temperature on moisture sorption isotherms has also been reported in many studies (Velásquez de la Cruz, Torres, & Martı́n-Polo, 2001; Wang & Brennan, 1991).
Numerous mathematical models have been proposed for the study of both adsorption and desorption of foods, such as the GAB, Iglesias and Chirife, BET, Oswin, and Ferro Fontán models (Barbosa-Canovas & Vega-Mercado, 1996; Crapiste & Rotstein, 1982; Gekas, 1992; Wang & Brennan, 1991). There is a lack of knowledge on how the overall water activity of cellular material is evaluated near the full turgor state (Crapiste & Rotstein, 1982). The Guggenheim–Anderson–de Boer (GAB) model is reported to be the best for fitting sorption isotherm data for the majority of food products up to aw levels of approximately 0.9 (Barbosa-Canovas & Vega-Mercado, 1996; Timmermann, Chirife, & Iglesias, 2001; Tsami, Krokida, & Drouzas, 1999). At aw>0.9, which is the region where cellular material is still in a quasi-turgor state, the water activity was seldom accurately measured or studied.
Osmotic dehydration is characterized by a more complex mass transfer process than air-drying. The transport of water out of the tissue is completed by a counter-current diffusion of the osmotic agent from the solution toward the tissue. These two simultaneous transports have a depressing effect on the aw of the samples. Osmotic processes are often evaluated in terms of water loss (WL) and solid gain (SG) (Bolin, Huxsoll, Jackson, & Ng, 1983; Erba, Forni, Colonello, & Giangiacomo, 1994; Garrote, Silva, & Bertone, 1992; Hawkes & Flink, 1978). Mathematic models have been reported in the literature to describe the water transport during osmotic drying (Azuara, Beristain, & Garcia, 1992; Fito & Chiralt, 1997; Panagiotou, Karathanos, & Maroulis, 1998; Toupin, Marcotte, & Le Maguer, 1989). However, only few studies aim at representing kinetics of water activity changes (Hough, Chirife, & Marini, 1993; Monsalve-Gonzalez, Barbosa-Cánovas, & Cavalieri, 1993). Marcotte and Le Maguer (1991) developed a model based on the equality of aw between the osmotic solution and potato material.
A mathematical model, based on the principles of desorption isotherms, can be a suitable way to predict the aw of a product during osmotic dehydration using the moisture content data. A reduction of the experimental work can therefore be reached. In addition, this model can be included in the mathematical models for description of water transport during dehydration allowing the direct prediction of the water activity in the product.
The aim of this study was to evaluate if the GAB model can be used (1) to describe the relationship between aw and moisture content in the particular case of osmotic dehydration and (2) to study the effect of temperature on the parameters of this model.
Section snippets
Sample preparation
A Swedish apple variety (Mutsu) produced in the Kivik region was purchased from a local market and stored at 4 °C at a relative humidity of around 95%. In the experiments two batches of apples were used. It was always ensured that apples of satisfying and equivalent quality in terms of firmness, colour and size were chosen. In order to evaluate the quality of the apples, the degree Brix was always measured and only apples with Brix 12.8 ± 1.0 were used. A cork borer was used to extract the
Results and discussion
Desorption isotherm graphs of apples during osmotic dehydration with sucrose solution at four different temperatures are presented in Fig. 1. As it can be observed the fit of the GAB model is good and it is quantified with the regression coefficient R2 (Table 2). At 65 °C, however, the model is satisfying below 0.970 but not above.
The GAB parameters at each temperature are also gathered in Table 2. The so-called monolayer value X0 looses here its original meaning since it was derived from
Conclusions
The GAB model showed a good fit with experimental data at nearly all the studied temperatures, and at 65 °C it was suitable for water activities below 0.970. A strong correlation was found between the C constant in the GAB model and temperature. It should, however, be borne in mind that the model is only an empirical model, which was not derived from any set of physical laws or diffusion theories. Accordingly, despite its demonstrated success, therefore, its general applicability cannot be
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