**2.1. Raw materials**

polyphenols, carotenoids and vitamin C. Chayote is also an important source of folic acid. There is an increasing interest in highly nutritious and instant foods, which is why the concentrated juice powder of these fruits could be an excellent and profitable option for consumption. In this way, chayote is mainly produced in Mexico and unknown in most countries. Due to the physical characteristics of the different types of fruit and the environmental conditions in the growing regions, large amounts of the harvested fruits fall short of the minimum quality

In recent years, new processes have been under development in order to achieve commercialization for fruit that fails to meet quality standards—the idea is to create products higher in quality and with greater added value. In this sense, the production of fruit juice powders is a better alternative for the use of raw material that fails to meet quality standards for exportation. In the processing of fruit juice, many variables exist that can lead to changes in the final product quality [1]. Rheological properties play an important role in the handling and processing, quality control and sensory evaluation of various foods [2]. The determination of rheological properties such as viscosity is of great importance in the prediction of heat and mass coefficients as well as for the design or development of heat transfer equipment and mass in the fruit juice industry [3]. Operational effects, such as concentration by evaporation, reverse osmosis, pumping and homogenization, are due to variations in viscosity [3]. In addition, factors such as the variety or maturity of the fruit and the treatment applied to fruit juice affect the viscosity of a reconstituted juice, so that the preference and acceptability of the consumer will be influenced by these factors [1, 4, 5]. Spray-drying is an alternative process for products which are sensitive to heat and has been used successfully in fruit juices [6]; the result is a product that has acceptable sensory characteristics and

In order to increase the glass transition temperature (Tg), the addition of thermoprotective additives such as maltodextrin is necessary to guarantee an adequate control of the spray drying process in fruit juices and the quality of the products obtained. The average aggregate amount has been reported between 30% and 75% (w/v); however, an excess of these generates increases in viscosity [7, 8], which stands in function of the total solids content of the particular juice to be processed. Carrier agent usually used in spray drying of fruit juices are carbohydrate based, such as maltodextrins and gums, mainly due to their high solubility, low viscosity, which are important conditions for the spray-drying process [9]. The production of fruit powders presents a challenge in the reduction of the viscosity of the juice of feeding, for the improvement of the drying, handling and storage. The presence of fructose, glucose and sucrose which are low molecular weight sugars as well as some organic acids in the fruit have

Recent studies have attributed agave fructans with thermal protective and encapsulating properties, as well as technological functions as stabilizers [10]. Fructans are rich in fructose polymers with a terminal glucose and are composed of fructose units and terminal glucose unit linked by β-(2 → 1) and β-(2 → 6) links [11]. The most common inulin type fructans are from chicory roots (*Cichorium intybus*). On the other hand, levan-type fructans are present in grasses and cereals as well as those produced by bacteria [12]; however, this levan fructans are

changes in the viscosity of the fruit powder and the reconstituted.

standards for direct use and result in significant losses.

stability for storage.

120 Polymer Rheology

Chayote, carrot, mango and pineapple fruit in consumption degree of ripeness were obtained in Tepic, Nayarit and subsequently washed and disinfected in a sodium hypochlorite solution (NaClO) at 200 ppm (0.02%). Then, they were peeled, and the juice of these fruits was obtained using a conventional extractor. Maltodextrin DE10 or native agave fructans were added by homogenization using an electric laboratory homogenizer (PRO Scientific. Inc. 300 PC) at 350 rpm during 15 min and filtered in a No. 50 filter sieve. One liter of homogenized juice was used for each test.

## **2.2. Spray drying**

A pilot dryer (model LPG-5, CIMA Industries Inc.) equipped with a rotatory nozzle was used for the spray-drying process with a feed rate of 15 mL.min−1, 2.5 bar, a juice feed temperature of 25°C, air inlet rate of 9.4 m/s and temperature of 120°C. Maltodextrin was added to reach a final concentration of 10% (m/v). Fructans were added to a concentration of 0.2% or 4%. The inlet temperature and maltodextrin concentrations were determined in preliminary studies. Total solids were determined in fresh chayote, carrot, mango and pineapple juices; these parameters were taken as a reference for rehydration. A mass balance was performed to determinate the quantity of water necessary to reconstitute the powder with total solids content similar (TSS) to fresh juice.

#### **2.3. Rheological properties of juices**

The rheometric measurements were carried out with a controlled stress rheometer (Model AR-G2 TA Instruments with Software Trios v4.0.1) using concentric cylinder geometry [exterior cylinder diameter 21.96 mm, interior cylinder diameter 20.38 mm, height 59.50 mm], gap 500 μm, a constant temperature of 25°C, maintained in a circulating water bath and a AG2 heater. The flow behavior was analyzed in a simple shear flow, low cutting speed in a range of 5–200 s−1. Juices were reconstituted based on the total soluble solids of the fresh juice. The experimental data of fresh or reconstituted juices were fitted to different flow models such as Newtonian (Eq. 1), Bingham (Eq. 2) and Ostwald-de-Waele Power Law model (Eq. 3).

$$
\tau = \eta \dot{\gamma} \tag{1}
$$

$$
\pi - \pi\_o = \eta' \circ \tag{2}
$$

$$
\pi = K \dot{\gamma}^{\eta} \tag{3}
$$

in the curves flow a Newtonian behavior (viscosity independent of the shear rate) for all the concentrations of fructans studied. In this sense, shear thinning behavior is characterized for a viscosity decrease with the shear rate due to structure destruction or a new structure formation. In this study, the concentrations of fructans were below 5%, so it is important to mention that for Cfructan ≤ 30% [w/v] [which were measured in a double wall Couette geometry], and at shear rates smaller than 70 s−1 shear thinning was detected followed by shear thickening at

**Figure 1.** Flow behavior index curves of reconstituted chayote (a), pineapple (b), carrot (c), and mango (d) powders [ ]

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Arvidson et al. [12] found shear thinning for aqueous levan polysaccharide solutions of 30% [w/v] and were measured at 20°C. The double wall Couette-type geometry presents secondary flow formation or Taylor vortices at higher shear rates, behaving turbulently as a flow type. The observed shear thickening behavior at high shear rates is attributed to the formation

This phenomenon has been studied predicting the stress near to the wall with the theoretical analysis of Stuart [22, 23]. Others authors have reported hydrodynamic instabilities such as Taylor-Couette Vortices in Newtonian fluids [23] and viscoelastics fluids [24, 25]. Macias et al. [26] observed flow instabilities at shear rates higher than 250 s−1 for water in Double

shear rates higher than 270 s−1 in accordance with Ponce et al. [20].

of instabilities of hydrodynamic flow [21, 22].

0% FT, [ ] 2% FT, [ ] 4% FT. FT: Fructanos.

where τ is the shear stress [Pa], *γ*̇ is the shear rate [s−1], η is the viscosity (Pa.s), η' is the plastic viscosity (Pa.s), τ0 is the yield stress (Pa), K is the consistency index (Pa1/2 sn) and n is the flow behavior index.

The best rheological model for describing the flow behavior of juices was selected by comparing the value of correlation coefficient, R2 .

#### **2.4. Rheological analysis**

**Figure 1** represents the flow curve of reconstituted juices containing three different concentrations of native agave fructans 0.2 and 4%. As can be observed from the figure, the flow curves at the three concentrations demonstrate an initial yield stress, indicating the presence of entangled rehydrated powders which prevents the free flow of the juices at zero shear rates. Similar flow curves were observed in the three concentrations of fructans. **Figure 1** shows

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**2.2. Spray drying**

122 Polymer Rheology

model (Eq. 3).

viscosity (Pa.s), τ0

**2.4. Rheological analysis**

behavior index.

content similar (TSS) to fresh juice.

**2.3. Rheological properties of juices**

*τ* = *K γ*̇

ing the value of correlation coefficient, R2

A pilot dryer (model LPG-5, CIMA Industries Inc.) equipped with a rotatory nozzle was used for the spray-drying process with a feed rate of 15 mL.min−1, 2.5 bar, a juice feed temperature of 25°C, air inlet rate of 9.4 m/s and temperature of 120°C. Maltodextrin was added to reach a final concentration of 10% (m/v). Fructans were added to a concentration of 0.2% or 4%. The inlet temperature and maltodextrin concentrations were determined in preliminary studies. Total solids were determined in fresh chayote, carrot, mango and pineapple juices; these parameters were taken as a reference for rehydration. A mass balance was performed to determinate the quantity of water necessary to reconstitute the powder with total solids

The rheometric measurements were carried out with a controlled stress rheometer (Model AR-G2 TA Instruments with Software Trios v4.0.1) using concentric cylinder geometry [exterior cylinder diameter 21.96 mm, interior cylinder diameter 20.38 mm, height 59.50 mm], gap 500 μm, a constant temperature of 25°C, maintained in a circulating water bath and a AG2 heater. The flow behavior was analyzed in a simple shear flow, low cutting speed in a range of 5–200 s−1. Juices were reconstituted based on the total soluble solids of the fresh juice. The experimental data of fresh or reconstituted juices were fitted to different flow models such as Newtonian (Eq. 1), Bingham (Eq. 2) and Ostwald-de-Waele Power Law

*τ* = *η γ*̇ (1)

*τ* − *τ*<sup>0</sup> = *η*´ *γ*̇ (2)

where τ is the shear stress [Pa], *γ*̇ is the shear rate [s−1], η is the viscosity (Pa.s), η' is the plastic

The best rheological model for describing the flow behavior of juices was selected by compar-

**Figure 1** represents the flow curve of reconstituted juices containing three different concentrations of native agave fructans 0.2 and 4%. As can be observed from the figure, the flow curves at the three concentrations demonstrate an initial yield stress, indicating the presence of entangled rehydrated powders which prevents the free flow of the juices at zero shear rates. Similar flow curves were observed in the three concentrations of fructans. **Figure 1** shows

.

is the yield stress (Pa), K is the consistency index (Pa1/2 sn) and n is the flow

*<sup>η</sup>* (3)

**Figure 1.** Flow behavior index curves of reconstituted chayote (a), pineapple (b), carrot (c), and mango (d) powders [ ] 0% FT, [ ] 2% FT, [ ] 4% FT. FT: Fructanos.

in the curves flow a Newtonian behavior (viscosity independent of the shear rate) for all the concentrations of fructans studied. In this sense, shear thinning behavior is characterized for a viscosity decrease with the shear rate due to structure destruction or a new structure formation. In this study, the concentrations of fructans were below 5%, so it is important to mention that for Cfructan ≤ 30% [w/v] [which were measured in a double wall Couette geometry], and at shear rates smaller than 70 s−1 shear thinning was detected followed by shear thickening at shear rates higher than 270 s−1 in accordance with Ponce et al. [20].

Arvidson et al. [12] found shear thinning for aqueous levan polysaccharide solutions of 30% [w/v] and were measured at 20°C. The double wall Couette-type geometry presents secondary flow formation or Taylor vortices at higher shear rates, behaving turbulently as a flow type. The observed shear thickening behavior at high shear rates is attributed to the formation of instabilities of hydrodynamic flow [21, 22].

This phenomenon has been studied predicting the stress near to the wall with the theoretical analysis of Stuart [22, 23]. Others authors have reported hydrodynamic instabilities such as Taylor-Couette Vortices in Newtonian fluids [23] and viscoelastics fluids [24, 25]. Macias et al. [26] observed flow instabilities at shear rates higher than 250 s−1 for water in Double wall Couette-type geometry. The shear thinning observed at low fructans concentration (Cfructans ≤ 30% [w/v]) could be due to these flow instabilities, since the viscosity of agave solutions is near to the water viscosity.

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The increase in viscosity is explained based on the transition of non-entangled fructan chains, however, an increase in the fructans concentration produce a greater amount of entanglements. The two slope changes they present themselves at medium concentration regimen at Cfructans = 35% [w/v] which are related to the overlap chains concentration. At higher concentrations at Cfructans = 70% [w/v], the solution behaves like a weak gel where high entanglements between fructan chains are detected. In solutions of linear polymers diluted with good solvents the dependence of η0 with concentration should be η ≈ Cfructans 4.7 [27]. Nevertheless, an increase in the concentration of polysaccharides causes the addition in the values of the exponent in the law of viscosity scale. Therefore, the value of the power law generates a screen in the understanding of the structure of the solution.

At 30°C, the agave fructan solutions exhibit a Newtonian behavior, this for samples with concentrations ≤80% [w/v]. In higher concentrations, the formation of a highly viscous solution is observed, so that the system at temperatures between 25 and 30°C shows a shearing dilution behavior; however, at high temperatures, there is a shear thickening [20]. The effect of fructan concentration on viscosity was similar to that of fructose or sucrose solutions. This confirms that the dependence of rheology on fructan concentration is closer to that of low molecular weight monosaccharides than to that of high molecular weight polysaccharides, as was proposed by Martínez-Padilla [28].

**Table 1** shows the fitted parameters of the Newtonian, Bingham and Power Law rheological models for chayote, carrot, mango and pineapple fresh or reconstituted juices with different content of fructans. For all the reconstituted juices, the best adjustment of flow data was obtained with the Bingham model, values of R2 ranged between 0.9992 and .9999. These results are in agreement with those of Shamsudin et al. [29] who found that the flow curves of Yankee pineapple juices were described by the Bingham model.

FT: fructans, N/A: no additives. All samples contain 10% maltodextrin. Note: similar letters no significant differences. Different letters significant differences (p > 0.05).

Bingham model describes plastic fluid that behaves as a rigid body at low stresses but flows as a viscous fluid at high stress. Then this type of fluid is characterized by a yield stress and a plastic viscosity. These parameters were statistically compared in **Table 2** for each formulation of juices. Whether for pineapple, carrot, mango or chayote juices, the addition of maltodextrin (10% [w/v]) and fructans (0–4% [w/v]) and the step of spray-drying had no significant influence on the plastic viscosity of juices as compared to fresh juices. Moreover, all the considered juices (**Table 1**) presented a low plastic viscosity that ranged from 0.0026 to 0.0030 Pa.s at 25°C. In contrast, yield stresses were impacted by the addition of maltodextrin, fructans or by the step of spray drying. Yield stress values were correlated to the presence and the degree of entanglement of colloids in fluids. For chayote and carrot juices, the addition of maltodextrin decreases significantly the value of the yield stress 124 Polymer Rheology Effect of Maltodextrin Reduction and Native Agave Fructans Addition on the Rheological… http://dx.doi.org/10.5772/intechopen.75758 125


wall Couette-type geometry. The shear thinning observed at low fructans concentration (Cfructans ≤ 30% [w/v]) could be due to these flow instabilities, since the viscosity of agave solu-

The increase in viscosity is explained based on the transition of non-entangled fructan chains, however, an increase in the fructans concentration produce a greater amount of entanglements. The two slope changes they present themselves at medium concentration regimen at Cfructans = 35% [w/v] which are related to the overlap chains concentration. At higher concentrations at Cfructans = 70% [w/v], the solution behaves like a weak gel where high entanglements between fructan chains are detected. In solutions of linear polymers diluted with good solvents the dependence of η0 with concentration should be η ≈ Cfructans 4.7 [27]. Nevertheless, an increase in the concentration of polysaccharides causes the addition in the values of the exponent in the law of viscosity scale. Therefore, the value of the power law generates a screen

At 30°C, the agave fructan solutions exhibit a Newtonian behavior, this for samples with concentrations ≤80% [w/v]. In higher concentrations, the formation of a highly viscous solution is observed, so that the system at temperatures between 25 and 30°C shows a shearing dilution behavior; however, at high temperatures, there is a shear thickening [20]. The effect of fructan concentration on viscosity was similar to that of fructose or sucrose solutions. This confirms that the dependence of rheology on fructan concentration is closer to that of low molecular weight monosaccharides than to that of high molecular weight polysaccharides, as was pro-

**Table 1** shows the fitted parameters of the Newtonian, Bingham and Power Law rheological models for chayote, carrot, mango and pineapple fresh or reconstituted juices with different content of fructans. For all the reconstituted juices, the best adjustment of flow data

results are in agreement with those of Shamsudin et al. [29] who found that the flow curves of

FT: fructans, N/A: no additives. All samples contain 10% maltodextrin. Note: similar letters no

Bingham model describes plastic fluid that behaves as a rigid body at low stresses but flows as a viscous fluid at high stress. Then this type of fluid is characterized by a yield stress and a plastic viscosity. These parameters were statistically compared in **Table 2** for each formulation of juices. Whether for pineapple, carrot, mango or chayote juices, the addition of maltodextrin (10% [w/v]) and fructans (0–4% [w/v]) and the step of spray-drying had no significant influence on the plastic viscosity of juices as compared to fresh juices. Moreover, all the considered juices (**Table 1**) presented a low plastic viscosity that ranged from 0.0026 to 0.0030 Pa.s at 25°C. In contrast, yield stresses were impacted by the addition of maltodextrin, fructans or by the step of spray drying. Yield stress values were correlated to the presence and the degree of entanglement of colloids in fluids. For chayote and carrot juices, the addition of maltodextrin decreases significantly the value of the yield stress

ranged between 0.9992 and .9999. These

tions is near to the water viscosity.

posed by Martínez-Padilla [28].

in the understanding of the structure of the solution.

was obtained with the Bingham model, values of R2

Yankee pineapple juices were described by the Bingham model.

significant differences. Different letters significant differences (p > 0.05).


**Table 1.** Experimental data fitted to parameters of rheological models (Newtonian, Bingham and Power Law).

from 0.0145 Pa (fresh juice) to 0.0029 Pa. The addition of maltodextrin to chayote and carrot juice induces a significant decrease of the yield stress of juice. This effect may be attributed to the interactions between the maltodextrin and the other polysaccharides, which do not allow these polysaccharides to fully extend in solution [30]. According to Grabowski et al. 2008 who studied the rheological properties of spray-dried sweet potato-maltodextrin powders, maltodextrin polysaccharide interactions could induce a decrease of the viscosity, since longer molecules have a larger hydrodynamic volume, which increases solution viscosity.

The additional supplementation of fructans up to 4% induced a slight but significant increase of the yield stress of fresh chayote juice up to 0.0078 Pa. Furthermore, spray drying did not seem to deeply impact the rheological behavior of chayote juices (**Table 1**). Pineapple juices presented higher yield stresses than chayote, while they had the same plastic viscosity. These findings could be because fruit juices contain colloidal systems. These colloids are part of the fruit itself or may be formed by microorganisms during fruit ripening. Most of the colloids come from the plant itself. The amount of colloids present in fruit juice is in the range of 100–1000 mg/L. An examination of colloids in the juice after pressing shows that they are basically polysaccharides such as pectins and starch [31, 32]. In this sense, the pineapple contains

more pectins than chayote, carrot and mango, and pectins are responsible for the turbidity and high viscosity of fruit juices. The addition of maltodextrin and fructans up to 4% [w/v] also induced a slight but significant increase of the yield stress of pineapple juices. However,

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, pa) and plastic viscosity (η', pa.S) of juices.

**Table 2.** Influence of fructans addition and spray-drying on yield stress (τ0

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from 0.0145 Pa (fresh juice) to 0.0029 Pa. The addition of maltodextrin to chayote and carrot juice induces a significant decrease of the yield stress of juice. This effect may be attributed to the interactions between the maltodextrin and the other polysaccharides, which do not allow these polysaccharides to fully extend in solution [30]. According to Grabowski et al. 2008 who studied the rheological properties of spray-dried sweet potato-maltodextrin powders, maltodextrin polysaccharide interactions could induce a decrease of the viscosity, since longer molecules have a larger hydrodynamic volume, which increases solution

**Table 1.** Experimental data fitted to parameters of rheological models (Newtonian, Bingham and Power Law).

The additional supplementation of fructans up to 4% induced a slight but significant increase of the yield stress of fresh chayote juice up to 0.0078 Pa. Furthermore, spray drying did not seem to deeply impact the rheological behavior of chayote juices (**Table 1**). Pineapple juices presented higher yield stresses than chayote, while they had the same plastic viscosity. These findings could be because fruit juices contain colloidal systems. These colloids are part of the fruit itself or may be formed by microorganisms during fruit ripening. Most of the colloids come from the plant itself. The amount of colloids present in fruit juice is in the range of 100–1000 mg/L. An examination of colloids in the juice after pressing shows that they are basically polysaccharides such as pectins and starch [31, 32]. In this sense, the pineapple contains

viscosity.

126 Polymer Rheology

**Table 2.** Influence of fructans addition and spray-drying on yield stress (τ0 , pa) and plastic viscosity (η', pa.S) of juices.

more pectins than chayote, carrot and mango, and pectins are responsible for the turbidity and high viscosity of fruit juices. The addition of maltodextrin and fructans up to 4% [w/v] also induced a slight but significant increase of the yield stress of pineapple juices. However, a decrease of this rheological parameter was observed for reconstituted juices after spray drying especially for samples with 4% of fructans, which could be due to the solubility of fructans above 95% [10].

**Acknowledgements**

**Author details**

**References**

Darvin Ervey Jimenez-Sánchez1

Pedro Ulises Bautista Rosales<sup>3</sup>

Juan Arturo Ragazzo-Sánchez1

The authors thank CONACyT [México] for their support in conducting the work throughout

, Montserrat Calderón-Santoyo1

and

Effect of Maltodextrin Reduction and Native Agave Fructans Addition on the Rheological…

, Julio Cesar Barros-Castillo1

1 Laboratorio Integral de Investigación en Alimentos, Tecnológico Nacional de México—

2 Université de Montpellier, UMR 1208, Ingénierie des Agropolymères et Technologies

3 Centro de Tecnología de Alimentos, Universidad Autónoma de Nayarit, Ciudad de la

[1] Juszczak L, Witczak M, Fortuna T, Solarz B. Effect of temperature and soluble solids content on the viscosity of beetroot [Beta vulgaris] juice concentrate. International Journal of

[2] Rao A.Rheology of Fluid, Semisolid, and Solid Foods: Principles and applications. Rheology

[3] Magerramov MA, Abdulagatov AI, Azizov ND, Abdulagatov IM. Effect of temperature, concentration, and pressure on the viscosity of pomegranate and pear juice concentrates.

[4] Tiziani S, Vodovotz Y. Rheological effects of soy protein addition to tomato juice. Food

[5] Aguiló-Aguayo I, Oms-Oliu G, Soliva-Fortuny R, Martín-Belloso O. Changes in quality attributes throughout storage of strawberry juice processed by high-intensity pulsed electric fields or heat treatments. LWT- Food Science and Technology. 2009;**42**(4):813-818

[6] Bhandari BR, Senoussi A, Dumoulin ED, Lebert A. Spray drying of concentrated fruit juices spray drying of concentrated fruit juices. An International Journal Drying Technology.

, Laetitia Picart-Palmade2

http://dx.doi.org/10.5772/intechopen.75758

,

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project number 210874 and for the scholarship granted to Jimenez-Sanchez D. E.

\*

\*Address all correspondence to: jragazzo@ittepic.edu.mx

Instituto Tecnológico de Tepic, Tepic, Nayarit, México

Emergentes, Place Eugène Bataillon, Montpellier, France

Cultura "Amado Nervo", Tepic, Nayarit, México

Food Properties. 2010;**13**(6):1364-1372

Fluid, Semisolid, Solid Foods. 2013;**19**:461

Hydrocolloids. 2005;**19**(1):45-52

1993;**11**(55):10811092

Journal of Food Engineering. 2007;**80**(2):476-489

The viscosity of agave fructans solutions (*Agave tequilana* Weber blue var.) at different concentrations and temperatures has been studied by Ponce et al. [20]. They observed that solutions with concentrations inferior to 30% [w/v] at temperatures ranging between 30 and 60°C presented a low viscosity, similar to water. Meanwhile, the viscosity of solutions with concentrations superior or equal to 30% [w/v], increased when increasing the concentration up to 70%, forming a highly viscous fluid. The results obtained in this work are in agreement with previous findings; lower plastic viscosity was observed in fructans powders with lower concentrations, this according to the flow parameters such as plastic viscosity (η') and yield stress (τ0 ) obtained with Eq. 2. This shear thinning behavior at low shear rate (20 s−1) followed by thickening behavior at high shear rate [300 s−1] in low fructans concentrations (Cfructans ≤ 30% in weight) could be due to flow instabilities such as vortices, since the viscosity of the samples is close to that of water [33].

The effect of adding maltodextrin on tomato pulp during spray-drying has been studied by Goula and Adamopoulos [30]. They observed that reconstituted tomato pulp from the resulting powder showed a non-Newtonian behavior with low stress, and a decrease in viscosity when the maltodextrin concentration and dextrose equivalent increase. This same effect is observed in the reconstituted chayote and pineapple powders and is attributed to the fact that the 10% maltodextrin concentration is higher in comparison to that of fructans.

Chayote, carrot, mango and pineapple juices [fresh and reconstituted] did not present the same rheological behavior [specially for the yield stress]. In this sense, studies have found that a decrease in sweet-potato solids, as well as interaction between maltodextrin and sweetpotato polysaccharides contributed to a decrease in viscosity of the reconstituted purée [34]. In general, the flow behavior of fresh and reconstituted sweet-potato solutions was different suggesting that the solids concentration being modified by the molecular changes during spray-drying. This could also explain the distinct rheological behavior for each reconstituted fruit powder in the present study.
