Extracción acuosa y secado del mucílago de yausabara
(
Pavonia sepium
A. St.-Hil.)
J. Food Sci. Gastron
. (July - December 2023) 1(2): 13-18
https://doi.org/10.5281/zenodo.13994686
ISSN: 3073-1283
ORIGINAL ARTICLE
Aqueous extraction and drying of yausabara mucilage
(
Pavonia sepium
A. St.-Hil.)
Franklin A. Molina
franklin.molina@utc.edu.ec
1 Facultad de Ciencias Agropecuarias y Recursos Naturales,
Universidad Técnica de Cotopaxi, Ecuador.
Received: 07 March 2023 / Accepted: 08 June 2023 / Published online:15 July 2023
© The Author(s) 2023
Evelin M. Chillagana
1
·
Dayanna E. Veloz
1
·
Franklin A. Molina
1
Abstract
The objective of this research work was to eval-
uate the aqueous extraction process for obtaining mucilage
from yausabara (
Pavonia sepium
A. St.-Hil.), a mucilaginous
plant found in various wet areas. The research arose from the
need to ofer alternatives to the agro-industrial sector. The
aqueous extracts of the mucilage were obtained from peeled
stems, both chopped and ground, using solid-liquid ratios of
1:4 and 1:6, over periods of 6, 12, and 24 hours. The viscos-
ity, turbidity, and total solid content of these extracts were
determined. An optimal extraction run was achieved (peeled
and chopped stems with a solid-liquid ratio of 1:4 for 20.42
hours), resulting in a viscosity of 51.72 mPa·s, turbidity of
2600 NTU, and a total solid content of 0.87%. The muci-
lage was precipitated with ethanol from the aqueous extract,
and the precipitate was then dried at 40 ºC in an oven for 3
days. The antioxidant capacity and total phenolic content of
the obtained powder were determined using the Folin-Cio-
calteu and FRAP methods, respectively. The powdered mu-
cilage showed a total phenolic content of 0.0046 mg/g and
an antioxidant capacity expressed as Fe
2+
, of 18.63 µM/g of
powder, values that are low compared to those reported for
plant-derived extracts.
Keywords
yausabara, mucilage, ethanol, distilled water,
extraction.
Resumen
El objetivo del presente trabajo de investigación
fue evaluar el proceso de extracción acuosa para la obtención
del mucílago de yausaba (
Pavonia sepium
A. St.-Hil.), una
planta mucilaginosa que se encuentra en distintos terrenos
húmedos. La investigación surgió de la necesidad de ofre-
cer alternativas al sector agroindustrial. La obtención de los
extractos acuosos del mucílago se realizó a partir de tallos
pelados, tanto troceados como molidos, utilizando relaciones
sólido-líquido de 1:4 y 1:6, durante períodos de 6, 12 y 24
horas. Se determinó la viscosidad, turbidez y contenido de
sólidos totales de dichos extractos. Se obtuvo una corrida
con óptimas condiciones de extracción (tallos pelados y tr-
oceados con una relación sólido-líquido de 1:4 durante 20,42
horas), que arrojó como resultado una viscosidad de 51,72,
una turbidez de 2600 NTU y un contenido de sólidos totales
de 0,87%. El mucílago se precipitó con etanol a partir del
extracto acuoso, y luego se realizó el secado del precipit-
ado a 40 ºC en estufa durante 3 días. Al polvo obtenido se
le determinó su capacidad antioxidante y contenido de po-
lifenoles totales mediante los métodos Folin-Ciocalteu y
FRAP, respectivamente. El mucílago en polvo presentó un
contenido de polifenoles totales de 0,0046 mg/g y una ca-
pacidad antioxidante expresada como Fe
2+
, de 18,63 µM/g
de polvo, valores bajos en comparación con los reportados
para extractos de origen vegetal.
Palabras clave
yausabara, mucílago, etanol, agua destilada,
extracción.
How to cite
Chillagana, E.M., Veloz, D.E., Molina, F.A. (2023). Aqueous extraction and drying of yausabara mucilage (
Pavonia sepium
A. St.-Hil.).
Journal of Food
Science and Gastronomy
,
1
(2), 13-18. https://doi.org/10.5281/zenodo.13994686
J. Food Sci. Gastron
. (July - December 2023) 1(2): 13-18
14
Introduction
Yausabara (
Pavonia sepium
A. St.-Hil.) is a plant native to
tropical regions that has garnered increasing interest in re-
search due to its functional properties and potential applica-
tions in the food and pharmaceutical industries. This species
is characterized by its high mucilage content, a gelatinous
substance found in its aerial parts and roots. The mucilage
from yausabara exhibits emulsifying, gelling, and stabilizing
properties, making it a valuable component for the formula-
tion of food products and medicinal applications (Quezada
et al., 2016).
In the context of its extraction, an aqueous extraction pro-
cess was conducted to maximize the recovery of mucilage.
This method is known for being efcient and sustainable, as
it uses water as a solvent, minimizing environmental impact
and being safe for human consumption. It was considered
that aqueous extraction would yield high-quality mucilage,
preserving the functional properties characteristic of this
plant (Chandran et al., 2023).
The extraction process was carried out at diferent tem
-
peratures and contact times, allowing for the evaluation of
the infuence of these factors on the yield of the extracted
mucilage. Extraction conditions are crucial, as they can af-
fect both the quantity and quality of the mucilage obtained.
This study aimed to determine the optimal conditions for
aqueous extraction, as well as the subsequent oven drying,
which is a fundamental step for the preservation and storage
of mucilage (Bazezew et al., 2022).
Drying the mucilage was considered a critical aspect, as it
infuences the stability and functional properties of the fnal
product. Diferent drying temperatures and times were evalu
-
ated, seeking to maintain the integrity of the mucilage and its
functional characteristics (Santos et al., 2023). Appropriate
drying techniques can contribute to obtaining mucilage with
a longer shelf life and ease of use in food and pharmaceutical
formulations. The objective of this study was to evaluate the
aqueous extraction process for obtaining yausabara mucilage
and its subsequent oven drying.
Materials and methods
The software Design Expert 8.0.6 (Stad-Ease Inc., Min-
neapolis, USA) was used for experimental design and result
analysis, aiming to obtain a raw aqueous extract of yausaba-
ra mucilage that exhibited adequate viscosity and a higher
total solids content. A numerical optimization method was
applied using a fourth-order optimal response surface de-
sign, which generated a mathematical model to describe the
variations of the variables in each experimental run.
The evaluated factors included extraction time (A), the de-
gree of crushing of yausabara stems (B), and the solid-to-liq-
uid ratio (C). The response variables were viscosity and
total solids content. The software defned ten experimental
combinations, of which two were replicates. Table 1 shows
the matrix of the experimental design. The study evaluated
three factors: extraction time (A), a numerical and discrete
variable measured in hours (h) with a range of 6 to 24 hours;
the degree of grinding (B), a categorical nominal variable
with two levels (1 and 2); and the solid/liquid ratio (C), also
categorical and nominal, with the same two levels (1 and 2).
These factors were analyzed to assess their impact on the
outcome of the process.
For the numerical optimization of the design, constraints
were established on the dependent variables, based on the
recommended criteria for the applications of the raw aque-
ous extract of the mucilage. Finally, one of the proposed
solutions was selected, which was considered the optimized
raw extract.
Table 1.
Experimental design matrix for aqueous extraction
Run
Extraction time
(h)
Grinding
degree
a
Solid/liquid
ratio
b
11211
22411
32422
41222
51222
62421
71211
8612
9621
102412
a: 1, chopped (peeled stem of 2 cm and macerated); 2, ground (peeled stem and crushed, cut to 10 cm).
b: 1, solid/water ratio of 1/4; 2, solid/water ratio of 1/6
J. Food Sci. Gastron
. (July - December 2023) 1(2): 13-18
15
To validate the optimization, the determination of total
sugar content, osmolality, and sensory acceptance of the op-
timized beverage was carried out in three repetitions. The
obtained results were compared with the values predicted by
the numerical optimization of the design.
Results and discussion
Table 2 shows the values of viscosity, total solids, and tur-
bidity of the raw aqueous extracts of yausabara. It can be
observed that as the extraction time decreased; the viscosity
of the raw extract was low, which could be attributed to the
degree of grinding and the solid-liquid ratio (Quitério et al.,
2022). The ten runs showed that a shorter extraction time
resulted in a lower amount of total solids, again infuenced
by the degree of grinding and the solid-liquid ratio.
Regarding the turbidity of these runs, similar ranges were
noted in runs 1, 2, and 10, despite having diferent extraction
times. In runs 1 and 2, the degree of grinding was the same,
and in all three runs, the solid-liquid ratio was identical. Runs
3 and 7 exhibited high turbidity values, ranging from 2070
NTU to 2020 NTU, while run 8 showed the lowest turbidity
at 910 NTU, which was due to the degree of grinding, as this
was performed by chopping.
Table 3 presents the signifcance of the analysis of vari
-
ance for the regression and the estimated coefcients for the
response variable, which is the viscosity of the raw yausaba-
ra extract and the total solids content of the crude aqueous
extract of yausabara. It can be seen that the quadratic re-
sponse surface model was signifcant at a 95.0% confdence
level. The R² statistic indicated that the adjusted model ex-
plained 99.49% of the variability in viscosity. It is observed
Table 2.
Indicators of the raw aqueous extracts of yausabara based on the experimental design.
Run
Viscosity
(mPa.s)
Total solids
(%)
Turbidity
(NTU)
180.80.751400
241.580.611350
330.360.892070
413.50.551060
520.10.491080
628.260.741650
776.70.842020
814.280.41910
911.70.461120
1014.940.471470
Table 3.
Analysis of variance of the quadratic response surface model for the viscosity of the raw mucilage extract of
yausabara and 2FI response surface model for the total solids content of the crude mucilage extract of yausabara.
Source
Quadratic response
surface
2FI response
surface model
p
-value
p
-value
Model0.01760.0151
A0.15700.0219
B0.01300.7148
C0.00840.0153
AB0.01860.0059
AC0.04200.0262
BC0.06590.0123
A
2
0.0539
-
R
2
0.9949
0.9767
Lack of ft
-
0.7582
A: extraction time; B: degree of grinding; C: solid/liquid ratio.
J. Food Sci. Gastron
. (July - December 2023) 1(2): 13-18
16
that the two-factor interaction (2FI) response surface model
was signifcant at a 95.0% confdence level. Additionally, the
R² statistic indicates that the ftted model explained 97.67%
of the variability in turbidity.
It can be observed that both the degree of grinding (B) and
the solid-liquid ratio (C) had an efect (
p
≤0.05) on the vis
-
cosity of the raw yausabara mucilage extract. The equation
of the model is:
V = 44.218125 + 4.305 A – 10.974375 B –
13.659375 C + 11.499375 AB + 7.524375 AC +
7.185 BC – 19.738125 A
2
(Eq. 1)
Where the viscosity (V) of the extract was measured in
mPa·s and was determined based on several factors. These
factors included the extraction time (A), expressed in hours,
the degree of grinding (B) of the yausabara stems, and the
solid-liquid ratio (C) used during the extraction process.
It can be observed that both extraction time (A) and solid/
liquid ratio (C) had a signifcant impact (
p
≤0.05) on the total
solids content of the crude mucilage extract of yausabara.
The equation of the obtained model is:
ST = 0.59976744 + 0.07918605 A + 0.0059375 B –
0.0740625 C + 0.1315625 AB + 0.0765625 AC +
0.07976744 BC
(Eq. 2)
According to the equation, ST refers to the total solids ex-
pressed as a percentage, while variables A, B, and C repre-
sent extraction time in hours, degree of grinding, and solid/
liquid ratio, respectively.
The analysis of the equation’s coefcients reveals that the
degree of grinding (B) exerted the most signifcant infuence
on the dependent variable, followed closely by the interac-
tion term between extraction time and degree of grinding
(AB). To verify the normality assumption, we analyzed the
normal probability of the residuals using an analysis of vari-
ance. The results showed that the internally studentized re-
siduals aligned closely with a straight line, indicating that the
errors conform to a normal distribution, thereby supporting
the normality hypothesis (Feng et al., 2020).
It can be observed that the values of the internally studen-
tized residuals aligned in a straight line, indicating a normal
distribution of the errors and thus confrming the normality
hypothesis. For the numerical optimization of the aqueous
extraction process of yausabara mucilage, the evaluated
intervals of the independent variables, which include ex-
traction time, degree of grinding, and solid/liquid ratio, were
used as constraints, to achieve a viscosity a viscosity of 60
mPas and a higher total solid content in the crude extract
(Table 4).
Table 5 presents the six optimized solutions for the aque-
ous extraction process of yausabara mucilage, based on the
Table 4.
Constraints for the optimization of the clarifcation process
ParameterLower limitUpper limitCriteria
Extraction time (h)624In the Interval
Degree of grinding12In the Interval
Solid/liquid ratio12In the Interval
Viscosity (cP)11.780.860
Total solids (%)0.410.89Maximize
a: 1, chopped (peeled stem of 2 cm and macerated); 2, ground (peeled stem and crushed, cut to 10 cm).
b: 1, solid/water ratio of 1/4; 2, solid/water ratio of 1/6.
Table 5.
Results of the numerical optimization of the aqueous extraction process of yausabara mucilage
Solution
Extraction
time (h)
Grinding
degree
a
Solid/liquid
ratio
b
Viscosity
(mPas)
Total solids
(%)
Statistical
convenience
120.421160.00010.6699620.73592617
26.001171.01750.8765990.67615198
323.162231.70.8717930.63116768
419.972138.27860.6740290.55017094
518.041232.21120.4481630.18374751
617.931232.36950.4478620.18372797
a: 1, chopped (peeled stem of 2 cm and macerated); 2, ground (peeled stem and crushed, cut to 10 cm).
b: 1, solid/water ratio of 1/4; 2, solid/water ratio of 1/6.
J. Food Sci. Gastron
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17
previously established constraints. Solution 1 was chosen as
it met the viscosity restriction and demonstrated the greatest
statistical convenience.
The results of the determinations made on the crude ex-
tract under optimal conditions. The indicators obtained in
the study include an average viscosity of 51.72 mPas, a to-
tal solids content of 0.87%, and a turbidity of 2600 NTU.
This extract was obtained using a solid/liquid ratio of 1:4,
with a chopped degree of crushing and an extraction time of
20.42 hours. As a result, a viscosity was obtained that is at
the minimum range compared to the mucilage of the nopal
(Vargas-Rodríguez et al., 2016).
The total solids are in the intermediate range between runs
3 and 7. The turbidity of this run exceeds that of the main
runs due to the shorter resting time. The powdered mucilage
showed a total polyphenol content of 0.0046 mg/g and an
antioxidant capacity expressed as Fe²⁺, determined by the
FRAP method, of 18.63 µM/g of powder, low values com-
pared to those reported for plant-derived extracts. These
values are possibly related to residual polyphenols left over
from the extraction and precipitation of the mucilage from
the crude aqueous extract.
Aloe vera (
Aloe vera
Barbadensis) is a xerophytic and suc-
culent species native to Africa; it has been identifed with
75 active principles; it contains phenolic compounds, mainly
chromones and anthraquinones (Liu et al., 2013), located in
the inner layer of epidermal cells. The gelatinous and col-
orless parenchyma mainly consists of water, mucilages, or-
ganic acids and salts, enzymes, saponins, tannins, traces of
alkaloids, and vitamins.
The phenolic compounds present in aloe vera act as free
radical scavengers or metal chelators, causing an antioxidant
efect. Hęś et al. (2019) suggested that a high content of fa
-
vonoids and anthraquinones is present in aloe vera. The rings
of favonoids have great potential to inhibit the generation of
reactive oxygen species; glycosylated favonoids are often
found in healthy leaves and possess reducing activity.
Of all secondary metabolites, phenolic compounds show
a linear correlation between concentration and antioxidant
capacity expressed in Trolox and ascorbic acid equivalents,
particularly favonoids. Adrianzén (2018) determined the an
-
tioxidant capacity using the ORAC method and total poly-
phenol content through the Folin-Ciocalteu method for the
peel and mucilage of
Cofea arabica
L. The study reported
antioxidant capacity values expressed as Trolox of 0.0412
µM/g and total polyphenols expressed as gallic acid of 17.21
mg/g of mucilage extract using methanol as a solvent. Both
determinations corresponded to low values for both indica-
tors, similar results to those of the present study. Howev-
er, it should be noted that the diference in matrices from
which the mucilaginous extracts were obtained (yausabara
and cofee), in addition to the diferences in analytical meth
-
ods, specifcally in determining antioxidant capacity, limits
comparisons.
Conclusions
The results identifed an optimal run using peeled and
chopped stems, achieving an adequate viscosity and signif-
icant total solids content. The analyses of polyphenols and
antioxidants revealed a low content, suggesting that, despite
these results, the drying process did not afect the properties
of the mucilage, as it was carried out at appropriate tempera-
tures and times. This indicates the potential of yausabara
mucilage as a viable option in agro-industrial applications,
despite the reduced levels of bioactive compounds.
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Conficts of interest
Te authors declare that they have no conficts of interest.
Author contributions
Evelin M. Chillagana, Dayanna E. Veloz and Franklin A.
Molina: Conceptualization, data curation, formal analysis,
investigation, methodology, supervision, validation, visuali-
zation, drafing the original manuscript and writing, review,
and editing.
Data availability statement
Te datasets used and/or analyzed during the current study
are available from the corresponding author on reasonable
request.
Statement on the use of AI
Te authors acknowledge the use of generative AI and AI-as-
sisted technologies to improve the readability and clarity of
the article.
Disclaimer/Editor’s note
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tions are solely those of the individual authors and contri-
butors and not of Journal of Food Science and Gastronomy.
Journal of Food Science and Gastronomy and/or the editors
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