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Osmo-dehydration of fruits

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<strong>Osmo</strong>-Dehydration <strong>of</strong> Fruits: a thermodynamic approach via Knudsen<br />

Thermogravimetry<br />

Dimitrios Fessas, Marco Signorelli, Alberto Schiraldi<br />

DISTAM, Università di MilanoVia Celoria 2, 20133 Milano, Italy (dimitrios.fessas@unimi.it)<br />

ABSTRACT<br />

The osmo-<strong>dehydration</strong> <strong>of</strong> a fruit pulp can be described with a thermodynamic model that takes into account<br />

the heterogeneity <strong>of</strong> the system. The experimental data are those relevant to the isothermal desorption trends<br />

across the swept RH range for the original (peeled) and partially osmo-dehydrated fruit pulp, and the<br />

hypertonic sugar syrup used. These trend allow evaluation <strong>of</strong> the mass <strong>of</strong> intra- and extra-cellular phases <strong>of</strong><br />

the system at any given RH. The mass change <strong>of</strong> the intra- cellular aqueous phase allows a rough evaluation<br />

<strong>of</strong> the shrinkage that the fruit cells undergo and the correlation between shrinkage and RH, which may be<br />

applied to any kind <strong>of</strong> <strong>dehydration</strong> treatment, provided it does not affect the cell walls.<br />

Keywords: osmo-dehydratio, Knudse thermo-gravimetry; thermodynamics<br />

INTRODUCTION<br />

Water in <strong>fruits</strong> and vegetables has a thermodynamic activity, a W , close to unity, which makes easy their<br />

degradation. This is why a previous <strong>dehydration</strong> is demanded to avoid non enzymatic browning and<br />

preservation <strong>of</strong> bioactive components (mainly vitamins and aromatic compounds).<br />

In osmo-<strong>dehydration</strong> the fruit is poured into a hypertonic solution <strong>of</strong> simple sugars and the intracellular<br />

moisture is drained out because <strong>of</strong> the sugar concentration gradient. The final product is still rather s<strong>of</strong>t and<br />

microbiologically unstable, as part <strong>of</strong> its moisture is retained. A final mild heat treatment (e.g., low<br />

temperature convection drying, freeze drying etc.) enhances the stability.<br />

It must be noticed that fruit cell walls are not actually semipermeable. Some fruit solutes (sugars, organic<br />

acids, minerals, salts, etc.) are therefore leached into the hypertonic solution while some sugar <strong>of</strong> this can<br />

migrate into the intra-cellular spaces (usually, even simple sugars are not able to trespass the cell walls) and<br />

the whole system shrinks as the fruit cells change size and shape. Dehydration extent and composition <strong>of</strong> the<br />

hypertonic syrup can affect the quality <strong>of</strong> the final product [1, 2].<br />

In order to assess the best operating practice models for the water migration and location during the process<br />

have been so far searched. A number <strong>of</strong> models [3,4] were proposed, where, in order to exclude any change<br />

<strong>of</strong> the hypertonic syrup during the process, its mass was supposed to be much larger than the fruit poured in.<br />

All these models assume a fickian behaviour for the diffusion, although they can substantially differ from one<br />

another for the number <strong>of</strong> the fitting equations and adjustable parameters. Unfortunately, they do not<br />

satisfactorily represent the actual system and the real operating conditions for a number <strong>of</strong> reasons: (i) a<br />

substantial change <strong>of</strong> the hypertonic syrup the mass <strong>of</strong> which actually does not exceed the 4:1 ratio versus<br />

that <strong>of</strong> the fruit; (ii) the sample is referred to as a continuum with a given macroscopic geometry that<br />

undergoes shrinkage as a whole; (iii) no general fundament is assumed that may be directly applied to any<br />

kind <strong>of</strong> fruit or vegetable (kind <strong>of</strong> cultivar, age after harvest, storing conditions, etc., are presented as the<br />

reason for the model limit).<br />

A basic statement is indeed lacking in all these models, namely, that the moisture content <strong>of</strong> biological<br />

materials is partitioned in different fractions and states, depending on the kind <strong>of</strong> tissue compartment and the<br />

solutes therein hosted. Because <strong>of</strong> the presence <strong>of</strong> extracellular biopolymers, cell membranes and other<br />

physical barriers, water molecules <strong>of</strong> the various moisture fractions have different mobility, as evidenced by<br />

means <strong>of</strong> NMR relaxometry [5], and are perpetually involved in exchanges between different states.<br />

The present work proposes a thermodynamic approach that defines boundary conditions that must be anyway<br />

obeyed, no matter the kind <strong>of</strong> fruit to be dehydrated and the hypertonic medium used in the process. It makes<br />

use <strong>of</strong> the aW changes both in fruit pulp and hypertonic syrup during a real osmo-<strong>dehydration</strong> process.<br />

To this aim, the isothermal desorption trends <strong>of</strong>: (i) non-treated fruit, (ii) syrup used for the osmo<strong>dehydration</strong>,<br />

(iii) a partially osmo-dehydrate fruit, have to be determined. The experimental method proposed<br />

is the Knudsen Thermogravimetry, which was so far exploited to determine the desorption isotherms <strong>of</strong>


aqueous solutions <strong>of</strong> salts and sugars, and food systems, like dough <strong>of</strong> various cereal flours [6,7]. The kind <strong>of</strong><br />

equipment used, namely, a TG-DSC combined instrument, allows extention <strong>of</strong> the investigation to various<br />

temperatures.<br />

MATERIALS & METHODS<br />

The Knudsen TG, designed by Schiraldi and Fessas [6], allows the direct determination <strong>of</strong> water activity. The<br />

thermo-balance cells are replaced with Knudsen cells, namely closed cells the cover <strong>of</strong> which has a 20 m<br />

orifice through which water molecules are pumped out under high dynamic vacuum (pext ≈ 0). In isothermal<br />

conditions the flux <strong>of</strong> water through the orifice, J, is proportional to the water partial pressure, p W , within the<br />

cell,<br />

dmW<br />

J = ∝ ( pW<br />

− pext<br />

) ≈ K ⋅ pW<br />

(1)<br />

dt<br />

where the constant K depends on the temperature and the size <strong>of</strong> the orifice and the flux J corresponds to the<br />

record <strong>of</strong> the time derivative <strong>of</strong> the thermo-gravimetric (DTG) trace.<br />

A separate experiment (at the same temperature and vacuum conditions) with a pure water sample produces a<br />

flux J* = K p W *, where p W * is the vapour pressure <strong>of</strong> pure water. The p W /p W * ratio is a good approximation<br />

for the value <strong>of</strong> water activity, a W , (or relative humidity, RH) <strong>of</strong> the sample considered. Because <strong>of</strong> the<br />

sample <strong>dehydration</strong> that takes place during the KTG run, the p W /p W * ratio decreases, while the mass drop is<br />

simultaneously recorded: this allows the direct evaluation <strong>of</strong> the residual sample moisture content versus RH,<br />

namely, the desorption isotherm.<br />

A single run therefore allows to draw the whole desorption trend, plotted in the plane (m W /m dm , RH), where<br />

the subscripts “W” and “dm” stand for water and dry matter, respectively, with reference to the trace <strong>of</strong> pure<br />

water recorded immediately before [6].<br />

These desorption trends are to be considered within the RH range actually experienced during an osmo<strong>dehydration</strong><br />

process, i.e. RH ≥ 0.8.<br />

The instrument used was a SETARAM TG-DSC111, Lyon, France, which allowed the simultaneous output<br />

<strong>of</strong> TG trace, namely mass loss-vs-time, its time derivative, DTG, and the relevant thermal effect. Thanks to<br />

such a coupling, the mass loss can be reliably attributed to the release <strong>of</strong> water if the mass-loss-rate/heat flux<br />

ratio has a value <strong>of</strong> about 2.2 J g-1, namely, the vaporization enthalpy <strong>of</strong> water [6], which is expected to hold<br />

also for water rich systems, like salt and sugar solutions, vegetables and <strong>fruits</strong>.<br />

Fuji cultivar apples, peeled and cut into spheres (d about 1.5 cm), were osmo-dehydrated at room temperature<br />

(~25°C) with three different sugar syrups <strong>of</strong> given water activity (a W = 0.89). The hypertonic syrup was<br />

continuously re-circulated through a peristaltic pump and the fruit-syrup mass ratio was kept at 1/8 (w/w);<br />

composition and water activity <strong>of</strong> the syrup underwent some detectable changes. Different treatment times<br />

were exploited (up to 6 h) in order to obtain samples at different <strong>dehydration</strong> levels. After the osmotic<br />

treatment, the samples were carefully and rapidly washed with cold water (details are reported in [8]). 40 mg<br />

mass samples were used for the KTG investigations.<br />

RESULTS & DISCUSSION<br />

In a osmo-<strong>dehydration</strong> process the dry matter <strong>of</strong> the sample increases, the RH <strong>of</strong> the fruit decreases and that<br />

<strong>of</strong> the hypertonic syrup increases, since the removal <strong>of</strong> water from the fruit is more than counterbalanced by<br />

the migration <strong>of</strong> sugars from the syrup toward the apple pulp. The process ends (after about 4 hour, in the<br />

present case) when fruit and syrup attain the same RH value.<br />

Since the intracellular water is sucked out <strong>of</strong> the fruit cells and displaced toward the intercellular regions and<br />

the surrounding medium, the RH <strong>of</strong> this is indeed a little higher at the end <strong>of</strong> the treatment.<br />

The starting samples <strong>of</strong> a Knudsen experiment must be in a steady state, i.e., with no neat water displacement<br />

between fruit compartments. During the isothermal <strong>dehydration</strong> the water fraction with the easiest access to<br />

the head space <strong>of</strong> the Knudsen cell determines the actual vapor pressure and therefore the RH detected. This<br />

means that RH gradients are soon formed between different fruit compartments. The relevant Knudsen trend<br />

therefore reflects quasi equilibrium states only when the effusion through the cell orifice is as slow as the<br />

displacement <strong>of</strong> water from one compartment to another.<br />

The desorption isotherm <strong>of</strong> non-treat fruit deals with a system the dry matter <strong>of</strong> which does not change. The<br />

release <strong>of</strong> water from the fruit is in this case limited by the diffusion <strong>of</strong> water through the cell walls. The fact


that partially heat-dehydrated apple pulp shows a Knudsen desorption trend perfectly overlapped to that<br />

obtained from the original non treated sample (Figure 1) indicates that the Knudsen desorption goes through<br />

the states that are actually met during a heat drying process.<br />

The desorption isotherm <strong>of</strong> a partially osmo-dehydrated fruit instead reflects the removal <strong>of</strong> water from the<br />

intercellular regions where it is more mobile: the desorption trend therefore concerns the partially diluted<br />

(because <strong>of</strong> the water sucked from the apple cells) syrup that remains entrapped in the fruit pulp. If a partially<br />

osmo-dehydrated fruit is further dried with a mild heat treatment, the removal <strong>of</strong> water still deals with the<br />

intercellular moisture. The desorption isotherm <strong>of</strong> such a sample is indeed overlapped to that obtained from a<br />

sample that did not undergo the further heat drying (Figure 1).<br />

Figure 1. Desorption isotherms drawn from KTG traces. Apple pulp samples: non treated, partially heat<br />

dried, partially osmo-dehydrated and heat dried after a partial osmo-<strong>dehydration</strong>.<br />

The desorption trend <strong>of</strong> a partially osmo-dehydrated fruit is shifted toward larger RH with respect to those <strong>of</strong><br />

the non-treated fruit and the hypertonic syrup (Figure 2). It has to be noticed that any fruit pulp is are multiphase<br />

system. In a rough approximation, it may referred to as a two phase system, namely, the intra- and the<br />

extra-cellular aqueous regions. A true thermodynamic equilibrium would imply that each compound that can<br />

be exchanged between these phase may attain the same thermodynamic activity in either phase. The partially<br />

osmo-dehydrated samples considered for the isothermal Knudsen desorption had been removed from the<br />

hypertonic syrup and let at rest for some hours to allow any neat displacement <strong>of</strong> water and sugars between<br />

phases to vanish. The composition <strong>of</strong> either phase therefore reflects the balance <strong>of</strong> the relevant chemical<br />

potentials and the amount <strong>of</strong> each phase can be evaluated with the simple lever rule.<br />

This means that the desorption trends recorded for the non-treated fruit pulp and the sugar syrup reflect the<br />

composition <strong>of</strong> the intra and extra-cellular phase, respectively (Figure 2). Any partial <strong>dehydration</strong> state must<br />

therefore remain between these trends (Figures 2) and, at any given RH, the mass <strong>of</strong> intra- and extra-cellular<br />

phase <strong>of</strong> the partially osmo-dehydrated sample can be easily evaluated [8].<br />

The decrease <strong>of</strong> the intracellular water produces shrinkage <strong>of</strong> the fruit cells, namely, a reduction <strong>of</strong> their<br />

volume. The volume drop is mainly related to the release <strong>of</strong> water: therefore a rough evaluation <strong>of</strong> such cell<br />

shrinkage may be:<br />

VW<br />

,0<br />

−VW<br />

shrinkage ≈ (2)<br />

V<br />

W ,0


Figure 2. Knudsen desorption isotherms collected from non- treated, partially (one hour treatment) osmodehydrated<br />

apple pulp, and the hypertonic sugar syrup used in the process. mW and mdm stand for water and<br />

dry matter mass, respectively.<br />

Since these quantities can be directly correlated to the RH through the relevant desorption isotherm, one may<br />

describe the shrinkage extent versus RH (Figure 3), which therefore applies to every partial <strong>dehydration</strong><br />

level, no matter the way it has been achieved (through osmo-<strong>dehydration</strong>, or heat drying, or combined<br />

treatment).<br />

Figure 3. Shrinkage <strong>of</strong> the cells <strong>of</strong> apple pulp evaluated according to equation 2 (see text). Data from the<br />

Knudsen desorption trend <strong>of</strong> non- treated samples.


CONCLUSION<br />

The osmo-<strong>dehydration</strong> <strong>of</strong> a fruit pulp can be described with a thermodynamic model that takes into account<br />

the heterogeneity <strong>of</strong> the system. The experimental data are those relevant to the isothermal desorption trends<br />

across the swept RH range for the original (peeled) and partially osmo-dehydrated fruit pulp, and the<br />

hypertonic sugar syrup used. These trend allow evaluation <strong>of</strong> the mass <strong>of</strong> intra- and extra-cellular phases <strong>of</strong><br />

the system at any given RH. The mass change <strong>of</strong> the intra- cellular aqueous phase allows a rough evaluation<br />

<strong>of</strong> the shrinkage that the fruit cells undergo and the correlation between shrinkage and RH, which may be<br />

applied to any kind <strong>of</strong> <strong>dehydration</strong> treatment, provided it does not affect the cell walls.<br />

REFERENCES<br />

[1] Torreggiani D. and Bertolo G. J. Food Eng. 2001; 49: 247-.<br />

[2] Lewicki PP., Le H. Vu and Pomaranska-Laznka W. J. Food Eng. 2002 ; 54: 141.<br />

[3] N. M. Panagiotou, V. T. Karathanos, Z.B. Maroulis. Int. J. Food Sci. Technol. 1998, 33, 267.<br />

[4] . L. Seguı´, P.J. Fito, A. Albors, P. Fito, J. Food Eng. 2006, 77, 179.<br />

[5] Hills BP. Magnetic Resonance Imaging in Food Science, John Wiley &Sons, Inc. Publ. New York; 1998<br />

[6] Schiraldi, A. and Fessas, D. , J. Therm. Anal. Cal. 2003, 71, 221.<br />

[7] Fessas, D. and Schiraldi, A. Food Chemistry 2004,90, 61.<br />

[8] Pani P., Schiraldi A., Signorelli M. and Fessas D., Food Biophysics, 2010,5 (3) 177.

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