In this study, hydrocolloids from butternut squash pulp (BSPH) have been employed as stabilizers for the development of acidified milk drinks to evaluate their physicochemical, rheological, and microstructural properties. BSPH was obtained in the alkaline medium (yield of 630 mg of hydrocolloids/100 g of pulp), presenting 79.97 ± 0.240% carbohydrate and non-Newtonian-type shear thinning. Four acidified milk drinks (AMDs) were obtained with 0.25, 0.50, and 1.00% BSPHs and a control sample without BSPHs. The addition of BSPHs did not alter the proximal composition of AMDs with similar proximal values; also, the samples present typical behavior of non-Newtonian-fluid-type shear thinning adjusted to the Carreau-Yasuda model. Storage (G') and loss (G″) moduli values were slightly dependent on the frequency in most of the studied systems. Then, the addition of BSPHs retained their uniform internal structure and contributed to the stabilization of the products.
In this study, hydrocolloids from butternut squash pulp (BSPH) have been employed as stabilizers for the development of acidified milk drinks to evaluate their physicochemical, rheological, and microstructural properties. BSPH was obtained in the alkaline medium (yield of 630 mg of hydrocolloids/100 g of pulp), presenting 79.97 ± 0.240% carbohydrate and non-Newtonian-type shear thinning. Four acidified milk drinks (AMDs) were obtained with 0.25, 0.50, and 1.00% BSPHs and a control sample without BSPHs. The addition of BSPHs did not alter the proximal composition of AMDs with similar proximal values; also, the samples present typical behavior of non-Newtonian-fluid-type shear thinning adjusted to the Carreau-Yasuda model. Storage (G') and loss (G″) moduli values were slightly dependent on the frequency in most of the studied systems. Then, the addition of BSPHs retained their uniform internal structure and contributed to the stabilization of the products.
Acidified milk drinks
(AMDs) are a generic term for a group of
popular beverages produced from fermented milk or by mixing fruit
or fruit juice concentrates with milk.[1−5] AMDs are usually manufactured by direct fermentation or acidification
of milk with lactic acid bacteria, followed by homogenization process
and acidification with acids or juice of fruits;[6] the final pH of these products generally ranges from 3.6
to 4.6.[4]One of the most common technological
challenges faced in AMD preparation
is “wheying” by forming a clear layer on top of the
drink. This separation occurs due to a decrease in electrostatic repulsion
between casein micelles, resulting in the aggregation of casein micelles,
occurring when the milk is acidified at a pH lower than 4.6.[6,7] To prevent phase separation and aggregation, different products
are used to stabilize AMDs; stabilizers are important for controlling
the physical properties of the drink, such as texture and mouthfeel.[3] The addition of stabilizers is one of the key
strategies to maintain the physical stability of food products. Protein–protein
interactions and subsequent aggregation can be minimized by the addition
of certain polysaccharides[8] for AMD products.
The food additive must present high solubility and stabilization behavior
of protein particles under acidic conditions without increasing the
viscosity; some additives present limitations to prevent protein aggregation
or precipitation under pH 4.0.[9] Currently,
the commonly used stabilizers of acid dairy products are soybean-soluble
polysaccharides[10] high-methoxy pectin,[2,3] carboxymethylcellulose,[11] carrageenan,[12,13] and gellan gum.[14,15]The stability of AMDs has
also been found to depend on the size
of the protein particle; usually, homogenization is used in the dairy
industry to reduce the creaming and sedimentation of milk. The exploration
of natural stabilizers has attracted much attention from researchers.
Formulation manufacturers especially value them for answering the
increasing demand of consumers for “clean labels” and
“natural ingredients” due to their perceived healthiness
and sustainability.[16] In the case of butternut
squash (Cucurbita moschata), the pulp
is a source of carbohydrate[17] including
xylose, arabinose, glucose, galactose, and gluconic acid. These are
macromolecular compounds that are characterized by solubility in water
and organic solvents and significant biological applications.[17,18] Different authors have studied the isolation of hydrocolloids from
butternut squash. Yuan et al.[19] extracted
starches from Cucurbita maxima Duch
and C. moschata Duch. Ex Poir. Milosevic
and Antov[20] and Fissore et al.[21] extracted pectin from the pulp and cell wall
of C. moschata, respectively. Wang
et al.[22] extracted polysaccharides from C. moschata seeds. Their application as a stabilizer
in food products was studied by Rojas et al.,[23] who stablized natural yogurt with hydrocolloids from butternut squash
seeds, and Orgulloso et al.[24] and Quintana
et al.,[25] who employed hydrocolloids from
butternut squash peel to stabilize mayonnaise-type sauce and jam,
respectively.However, there are few reports on squash pulp
characterization
and techno-functional properties and their use in developing food
products. For example, Umavathi et al.[26] extracted polysaccharides from C. moschata Duch with biological activities (anti-inflammatory, antioxidant,
and antimicrobial activities). Du et al.[27] studied the prebiotic potential of oligosaccharides from C. moschata with high solubility. Torkova et al.[28] obtained pectin from C. maxima D. var. Cabello de Ángel with antioxidant and antiproliferative
properties. Baississe and Fahloul[29] extracted
pectin from C. maxima with plastic
properties. Nevertheless, the extraction from hydrocolloids from squash
pulp has not been done. Therefore, this study aimed to stabilize acidified
milk beverages with butternut squash pulp hydrocolloids (BSPHs) and
evaluate their physicochemical, rheological, and microstructural properties.
Results and Discussion
Butternut Squash Pulp Hydrocolloids
(BSPHs)
Butternut squash pulp hydrocolloids (BSPHs) were
obtained in an
alkaline medium with 630 mg of hydrocolloids/100 g of pulp extraction
yield. BSPHs present values of 4.80 ± 0.63% moisture, 3.01 ±
0.53% ash, 1.10 ± 0.35% fat, 12.21 ± 0.11% protein, and
79.97 ± 0.240% carbohydrate, associated with saccharide content
including xylose, arabinose, glucose, galactose, and gluconic acids,
the main components of Cucurbita sp. polysaccharides.[30] The results demonstrate that the pulp of butternut
squash (C. moschata) is an excellent
source of carbohydrates for the commercial production of hydrocolloids.BSPHs show a decrease in apparent viscosity with increasing shear
rate (Figure ), indicating
a non-Newtonian property-type shear-thinning behavior; this behavior
is due to the alignment of biopolymer chains in the direction of probe
rotation with the decrease in the macromolecule chain interactions
and apparent viscosity[31] as well as breaking
strong bonds at high shear rates.[32] The
rheological properties of hydrocolloids influence their application
in food products; they are an alternative to increase the viscosity
or thickness of food products and improve the water-binding ability
and texture of foods. The choice of hydrocolloid depends on the attributes
desired in the final product and the conditions of processing.[23]
Figure 1
Viscous curve of hydrocolloids from butternut squash pulp
(C. moschata).
Viscous curve of hydrocolloids from butternut squash pulp
(C. moschata).Then, shear-thinning behavior is reported for most hydrocolloids,
such as hydrocolloids from C. moschata seed,[33] mulberry (Morus
alba L.) leaves,[34]Pereskia bleo,[35] and Prosopis flexuosa seeds.[36]The experimental data were fitted to the Carreau–Yasuda
model, according to eq where η is the viscosity (Pa·s),
γ ˙is the shear rate (s–1), η0 is the viscosity at a low shear rate (Pa·s), η∞ is the viscosity at a high shear rate (Pa·s),
λ is the relaxation time constant (s) (the inverse of λ
has an interpretation of the critical shear rate at the point where
the viscosity begins to decrease), α is the power that determines
the transition between low shear rate and high shear rate region (dimensionless),
and n is the flow index (dimensionless).The
data adjust very well to the Carreau–Yasuda model, presenting
a correlation coefficient (R2) of 0.99.
The BSPHs present η0 of 22084.19 Pa·s, η∞ of 0.15 Pa·s, λ(c) 425 s, a of 1.950, and n 0.01, corroborating the
shear-thinning properties. Then, BSPHs are a potential ingredient
in developing food products because their characteristics include
desirable attributes in providing satisfaction to consumers.[20]The viscoelastic properties of hydrocolloids
were evaluated. The
amplitude test performed over the studied stress range determines
the linear viscoelastic region of BSPHs, indicating a linear viscoelastic
region where G′ and G″
were almost constant (between 0.1 and 10 Pa) and a nonlinear region
where G′ and G″ began
to decrease; then, 1 Pa was chosen to perform a frequency sweep to
obtain the mechanical spectra for BSPH at room temperature (Figure ). The structure
of polymers also influences the viscoelastic behavior of BSPHs.
Figure 2
■ Storage
(G′) and □ loss
(G″) modulus of hydrocolloid from butternut
(C. moschata) squash pulp.
■ Storage
(G′) and □ loss
(G″) modulus of hydrocolloid from butternut
(C. moschata) squash pulp.Storage modulus (G′) was higher than
the
loss modulus (G″) in the entire angular frequency
(ω), presenting more elastic properties than viscous ones, which
corresponds closely to that of a gel increase with the increased frequency.
Therefore, the gel structure and viscoelastic behavior of hydrocolloids
were stable in the range of temperatures studied. Similar results
have been reported for hydrocolloids with a high carbohydrate content,
i.e., seed gum–xanthan blend[37] and
amorphous Gelditsia depending on their concentration,[38] also according to the frequency sweep. BSPH
presents a loss tangent value (tan δ = G’’/G’) of 0.305, which suggests
a concentrated amorphous polymer rather than a gel.[39]The dynamic analysis can give information about the
time or frequency
dependence and the structural behavior of components. The results
obtained are essential for predicting material behavior through the
manipulation of processing.[40] The interactions
of hydrocolloids with other components coexisting in food matrices
allow increased flexibility for food research development. The stabilizers
are indispensable in the design of food structure and functionality
demanded by consumers in modern society.[41]
Acidified Milk Drinks
Four acidified
milk drinks were obtained with 0.25% (AMDs + BSPH0.25),
0.50% (AMDs + BSPH0.50), and 1.00% BPSH (AMDs + BSPH1.00); also, a control sample without BPSH (AMDs) was prepared.
The physicochemical properties of AMDs are shown in Table . The control sample presents
different pH, SS, and acidity value compared to the samples with BSPH;
then, the employee of BPSH presents a slight increase in pH, soluble
solids, and acidity.
Table 1
Acidified Milk Drink’s
Formation
and Physicochemical Properties Stabilized with Butternut Squash Pulp
Hydrocolloids (BSPHs)
code sample
BSPH (%)
pHa
SSa °brix
acidity (%) acid lactic
AMDs
0
3.81
10.70b
0.11 ± 0.05b
AMDs + BSPH0.25
0.25
4.28
12.44b
0.19 ± 0.01
AMDs + BSPH0.50
0.50
4.38
12.56b
0.17 ± 0.78
AMDs + BSPH1.00
1.00
4.40
11.38b
0.17 ± 0.01
Data with CV <0.5%.
Data are expressed as mean ±
standard deviation. Different letters in the same columns express
statistically significant differences (p < 0.05).
Data with CV <0.5%.Data are expressed as mean ±
standard deviation. Different letters in the same columns express
statistically significant differences (p < 0.05).The addition of BSPHs did not
alter the proximal composition of
AMDs (p > 0.05) with similar values of moisture
(79.24–81.07%),
ash (1.51–1.84%), carbohydrate (14.78–16.50%), and protein
(0.38–0.47%) and an increase in fat (0.57–1.32%) (Table ).
Table 2
Proximal Composition of Acidified
Milk Drink Stabilized with Butternut Squash Pulp Hydrocolloids (BSPHs)
code sample
moisture (%)
ash (%)
fat (%)
carbohydrate (%)
protein (%)
AMDs
81.07 ± 0.41a
1.51 ± 0.43a
0.57 ± 0.25a
16.50 ± 1.13a
0.47 ± 0.008a
AMDs + BSPH0.25
79.99 ± 0.08a
1.69 ± 0.57a
0.86 ± 0.15a,b
14.78 ± 0.30a
0.38 ± 0.005a
AMDs + BSPH0.50
79.61 ± 0.25a
1.84 ± 0.66a
1.32 ± 0.10b
15.80 ± 0.60a
0.38 ± 0.004a
AMDs + BSPH1.00
79.24 ±0.24a
1.71 ± 0.51a
1.10 ± 0.31b
16.22 ±1.55a
0.41 ± 0.009a
Data are expressed as mean ±
standard deviation.
Different
letters in the same columns
express statistically significant differences (p <
0.05).
Data are expressed as mean ±
standard deviation.Different
letters in the same columns
express statistically significant differences (p <
0.05).
Rheological
Properties
The AMDs
viscous flow curves are shown in Figure a. The apparent viscosity of the samples
decreases with the increasing shear rate, typical behavior of non-Newtonian
fluid-type shear thinning; the same behavior is observed in acidified
milk products. Aljewicz et al.[42] obtained
shear-thinning behavior for yogurt-like products, Yuliarti et al.[43] for acidified milk drinks stabilized with carboxymethylcellulose
and pectin, Janhøj et al.[44] for acidified
milk drinks, and Martin et al.[45] for skim
milk gels acidified with glucono-δ-lactone.
Figure 3
(a) Viscous flow behavior
and (b) flow curve of acidified milk
drink stabilized with BSPH.
(a) Viscous flow behavior
and (b) flow curve of acidified milk
drink stabilized with BSPH.The samples present a critical shear rate at which the viscosity
begins to decline,[46] which was due to the
change in the structure of molecules upon the application of BSPHs.
Then, to evaluate the shear stress behavior with the shear rate, a
flow curve was plotted (Figure b) by adjusting the experimental data to the Herschel–Bulkley
model (eq )where τ
is the shear stress (Pa), τ0 is the apparent yield
stress (Pa), m is
the consistency coefficient (Pa·s), γ ˙ is the shear rate (s–1), and n is the flow behavior index (dimensionless).
This model can describe Newtonian and time-independent non-Newtonian
fluids; then, there are six main classes to this model: shear thinning
(n < 1.0), shear thickening (n < 1.0), and neither (1.0), with yield stress (τ0 < 0) or without yield stress (τ0 > 0);[47] when the yield stress is the minimum, the shear
stress required to initiate product flow is related to the material’s
internal structure, which must be broken.[48,49]Table shows
the
rheological parameters obtained for acidified milk drink stabilized
with BSPHs, which present higher correlation coefficients (R2 > 0.90). A difference between the parameters
with the formulation employee was observed. All samples have a flux
index value (n) of less than 1 (p < 0.05), confirming the shear thinning behavior; also, the consistent
coefficient (m) decreases with the increasing BSPHs
(p < 0.05), preserving its pseudoplastic properties.
The samples present an increase in yield stress (τ0 > 1) with the increase in BSPHs (p < 0.05),
attributed to higher interaction as well as the presence of a thick
three-dimensional structure. This behavior can be explained by the
fact that the shear thinning in steady shear test, under large deformation,
can occur when rodlike particles are aligned in the flow direction
and have lost their junctions in polymer solutions, which, in turn,
finally results in the breakdown of polymer agglomerate.[50]
Table 3
Parameters of Adjustment
of Hershel–Bulkley
Model of Acidified Milk Drink Stabilized with Butternut Squash Pulp
Hydrocolloids (BSPHs)
sample code
τ0 (Pa)
m (Pa·sn)
n
R2
AMDs
6.42 ± 0.98a
15.99 ± 1.05a
0.17 ± 0.001b
0.98
AMDs + BSPH0.25
7.69 ± 2.43a
18.40 ± 2.61b
0.15 ± 0.01b
0.94
AMDs + BSPH0.50
11.34 ± 3.80b
19.67 ± 4.04b
0.13 ± 0.02a
0.93
AMDs + BSPH1.00
12.47 ± 0.56b
21.50 ± 1.31c
0.11 ± 0.09a
0.90
Data are expressed as mean ±
standard deviation.
Different
letters in the same columns
express statistically significant differences (p <
0.05).
Data are expressed as mean ±
standard deviation.Different
letters in the same columns
express statistically significant differences (p <
0.05).The viscoelastic
characteristics of AMDs depend on the concentration
of BSPH (Figures and 5). Storage (G′) and loss
(G″) moduli values were strongly dependent
on the frequency in the majority of the system studied. For all samples, G′ and G″ present a strong
frequency dependence with the elastic component exceeding the elastic
one for the whole frequency range examined, indicating an elastic-like
behavior. All samples exhibited viscoelastic properties normally observed
for weak-gel systems, which is typical in this type of product: the
elastic response predominated over the viscous response, both dynamic
moduli showed only slight variation with oscillation frequency, and
the frequency dependencies of dynamic moduli become parallel.[51,52]
Figure 4
Storage
(G′) and loss (G″)
moduli as the function of angular frequency (ω) of
acidified milk drink stabilized with butternut squash pulp hydrocolloids
(BSPHs).
Figure 5
Loss tangent (tan δ) of acidified
milk drink stabilized
with butternut squash pulp hydrocolloids (BSPHs).
Storage
(G′) and loss (G″)
moduli as the function of angular frequency (ω) of
acidified milk drink stabilized with butternut squash pulp hydrocolloids
(BSPHs).Loss tangent (tan δ) of acidified
milk drink stabilized
with butternut squash pulp hydrocolloids (BSPHs).Then, the elastic contribution gradually prevailed over the viscous
one; in AMD systems, the dynamic moduli (G′
and G″) decrease with the increasing BSPH
(Table ). Then, the
elastic contribution gradually prevailed over the viscous one; in
AMD systems; the control samples (AMDs) present the lowest dynamic
moduli (G′ and G″);
nevertheless, analyzing the addition of hydrocolloids, G′ and G″ decrease with the increase
in BSPH (Table ) owing
to the entanglement of gum. The intermolecular association of the
chain of xanthan gum (1,4)-β-d-glucose with trisaccharide
side chain[53] interacts with functional
groups to form different structures.[54−58] Then, similar results were obtained for acidified
and fermented dairy products, e.g., acidified skim milk, yogurts,
and fresh cheese, which can be considered as a viscoelastic soft matter.[59−63]
Table 4
Viscoelastic Parameters of Acidified
Milk Drink Stabilized with BSPHs at the Frequency of 10.00 rad s–1
sample code
G′ (Pa)
G″ (Pa)
tan δ
AMDs
212.5
56.56
0.266
AMDs + BSPH0.25
1142.0
263.3
0.237
AMDs + BSPH0.50
712.3
175.1
0.245
AMDs + BSPH1.00
381.8
102.6
0.269
In this study, the loss tangent (tan δ)
of samples
(Figure ) averaged
between 0.237 and 0.269 (Table ), demonstrating that the storage modulus is a primary characteristic
to be considered in all AMDs stabilized with BSPHs and represents
a small loss tangent as an elastic material.
Microstructural
Properties
The
microstructural properties of acidified milk drink stabilized with
hydrocolloids from butternut squash (C. moschata) pulp are shown in Figure .
Figure 6
Microscopy (100×) of acidified milk drink stabilized with
butternut squash pulp hydrocolloids (BSPHs). (a) AMDs, (b) AMDs +
BSPH0.25, (c) AMDs + BSPH0.50, and (d) AMDs
+ BSPH1.00.
Microscopy (100×) of acidified milk drink stabilized with
butternut squash pulp hydrocolloids (BSPHs). (a) AMDs, (b) AMDs +
BSPH0.25, (c) AMDs + BSPH0.50, and (d) AMDs
+ BSPH1.00.The stability of such
a milk system might mainly be due to the
increase in viscosity by added polysaccharides and the steric effect
of electrostatic adsorption between negatively charged polysaccharides
and positively charged casein particles.[64] The microstructure of protein–polysaccharide systems such
as casein–BSPH mixtures is determined by the competition between
the “phase separation” and the “electrostatic
interaction” between the protein and polysaccharide.[65]Many authors indicate a close relationship
between structure and
rheology.[66,67] Protein–polysaccharide aggregates,
open cavities, and casein micelles were present in all of the AMD
samples, suggesting that AMDs and AMDs + BSPH1.00 have
similar microstructures; the inclusion of BSPHs increased the openness
of the sample, inhibiting the aggregation of casein particles, in
agreement with previous studies.[68,69] From the previous
research, it is reasonable to conclude that the polysaccharide–protein
interaction can stabilize the emulsion system and yogurt gels.[70] Then, the BSPHs retained their uniform internal
structure after the addition and contributed to the stabilization
of the products. This behavior could be related to the increase in
rheological parameters: yield stress (τ0) and consistency
index; where the dark areas, which could be related to a higher water
retention capacity and a higher stability during storage.[71]
Materials
and Methods
Materials
Butternut squash with similar
weight and commercial maturity was purchased from the local food market
(Cartagena, Colombia). Hexane and ethanol (99.5% purity) were obtained
from Panreac (Barcelona, Spain). Acetic acid, sodium hydroxide (NaOH, pellet for analysis), petroleum
ether (grade for analysis), buffer solutions (boric acid/potassium
chloride/sodium hydroxide), sodium azide, and phenolphthalein were
purchased from Sigma-Aldrich (St. Louis, MO). Citric acid, sodium
bicarbonate, and sucrose were purchased from Tecnas S.A. (Itagui,
Colombia). Commercial pasteurized and homogenized milk and skim milk
powder was purchased from a local Colombian market. All other reagents
were of analytical grade.
Hydrocolloid Extraction
The extraction
of hydrocolloids from squash pulp (BSPH) was done following the procedures
described by Quintana et al.[25] and López-Barraza
et al.[35] with some modifications. A ratio
of 1:8 of pulp–water at pH 10 was continuously agitated at
80 °C for 4 h. The resulted mixture was separated by centrifugation
for 15 min at 4000 rpm, and the supernatant was recollected. For isolating
the polymeric hydrocolloids, the extract supernatant was added in
a 1:1 ratio of 99.5% ethanol (analytical grade) to precipitate its
biopolymer fraction, followed by centrifugation and freeze-drying
at −50 °C and 0.02 Pa for 48 h by employing a freeze-dry
equipment (Labconco Freezone 1.5 Liter Benchtop).
Formulation of Acidified Milk Drinks (AMDs)
Skim milk
powder was reconstituted with a nonfat milk drink of
16% (w/v) using deionized water with 0.02% (w/v) sodium azide to prevent
microbial growth. The nonfat milk drink was stirred at 60 °C
for 1 h to dissolve the milk powder completely. Subsequently, the
sample was pasteurized at 121 °C for 5 min, cooled, and fermented
with yogurt culture (3% w/v) at 43 °C until pH 4.1 was obtained.
After that, the sample was cooled to 25 °C. Different amounts
of BSPHs (0.25, 0.50, and 1.00%) were used as stabilizing products.
Then, the mixture was homogenized using an ultraturrax (IKA T25 basic,
Deutschland, Germany) with an S25 N–10ST dispersing tool at
16 800 rpm for 10 min at room temperature. Finally, the prepared
AMDs were stored at 5 °C for future use. A control sample without
BSPHs was performed. All experiments were carried out in duplicate.
Physicochemical and Proximal Composition
The physicochemical and proximal composition of the samples was
performed following the procedures described by the Association of
Official Analytical Chemistry 41. pH (AOAC 943.02), titratable acidity
(AOAC 935.57), ash (AOAC 942.05), moisture (AOAC 934.01 and 930.15),
fat (AOAC 926.08 and 945.16), protein (AOAC 984.13), and carbohydrate
(AOAC 920.44/906.03) were analyzed.[72]
Rheological Properties
The rheological
characterization of BSPHs and AMDs was carried out on a controlled-stress
rheometer (Modular Advanced Rheometer System Haake Mars 60, Thermo-Scientific,
Germany) based on the methods by Quintana et al. and Rojas et al.[23] using a parallel plate (diameter 35 mm and GAP
1 mm) for hydrocolloids and coaxial cylinder (inner radius 12.54 mm,
outer radius 11.60 mm, cylinder length 37.6 mm). Each sample was equilibrated
600 s before the rheological test to ensure the same thermal and mechanical
history for each sample.
Viscous Flow Properties
Viscous
flow tests were carried out at a steady state by analyzing the variation
in the apparent viscosity in a range of shear rates between 0.001
and 1000 s–1 at 25 °C.
Viscoelastic Properties
A small-amplitude
oscillatory shear analysis was performed. Initially, stress sweeps
were carried out by applying an ascending series of stress values
from 0.001 to 1000 Pa at a frequency of 1 Hz at 25 °C to determine
the linear viscoelasticity interval; after that, the frequency sweeps
were performed in a frequency range between 10–2 and 102 rad s–1 to obtain the mechanical
spectrum using a stress value within the linear viscoelastic range.The data recorded include the storage modulus (G′), which provides the elastic component, the loss modulus
(G″), which is related to the viscous component
of the material, and the loss tangent (Tan δ), which
is the ratio G″/G′
and provides the ratio of elastic to the viscous response of the material
under consideration.
Microstructural Analysis
A primo
Star optical microscope (Carl Zeiss Primo Star Microscopy GmbH, Jena,
Germany) with a 100× magnification lens was used to observe the
internal distribution and droplet size of the samples (ca. 50 μL).
A DCMC310 digital camera with Scope Photo software (version 3.1.615)
from Hangzhou Huaxin Digital Technology Co., Ltd., Zhejiang, China,
attached to the optical microscope captured the image.
Statistical Analysis
Statistical
analysis of the results was performed using the Statgraphics Centurion
XVI (Statgraphics, Rockville, MD). An ANOVA (unidirectional) test
was applied to determine statistically significant differences (p < 0.05) between the samples submitted to the characterizations.
All tests were performed in triplicate.
Conclusions
Butternut squash pulp hydrocolloids (BSPHs) were obtained in an
alkaline medium with a high percentage of carbohydrates (79.97 ±
0.240%), presenting a non-Newtonian-fluid-type shear thinning behavior
adjusted to the Carreau–Yasuda model (R2 > 0.98). The viscoelastic properties show that the storage
modulus (G′) was higher than the loss modulus
(G″) in the entire angular frequency (ω),
presenting more elastic properties than viscous ones and presents
tan δ of 0.305, which suggests a concentrated amorphous
polymer rather than a gel. The development of acidified milk drinks
was carried out using hydrocolloids from butternut squash pulp as
stabilizers, with percentages of 0, 0.25, 0.50, and 1.00%. The control
samples (0% of hydrocolloids) have different pH, SS, and acidity values
compared to the samples with BSPHs; then, the BPSHs added presented
a slight increase in pH, soluble solids, and acidity; nevertheless,
the addition of BSPHs did not alter the proximal composition of the
drinks. Drinks present a typical behavior of non-Newtonian-fluid-type
shear thinning and viscoelastic properties related to the percentage
of hydrocolloids used: the storage (G′) modulus
is higher than the loss (G″) modulus presenting
properties for weak-gel systems, typical of acidified or fermented
milk products. The microstructure shows the interaction of milk protein
with carbohydrate of hydrocolloids determined by the competition between
the electrostatic interaction between protein and polysaccharide.
Then, the addition of BSPHs retained its uniform internal structure
and contributed to the stabilization of the products.
Authors: Anna A Torkova; Ksenia V Lisitskaya; Ivan S Filimonov; Olga A Glazunova; Galina S Kachalova; Vladimir N Golubev; Tatyana V Fedorova Journal: PLoS One Date: 2018-09-20 Impact factor: 3.240