Release Profile of Betanin from Chitosan
Microparticle Containing Beetroot
(Beta vulgaris Linn) Extract
Anita Sukmawati(B) , Isna V. Risdiyanti, and Clara C. Marthadilla
Faculty of Pharmacy, Universitas Muhammadiyah Surakarta, Jl. A Yani, Tromol pos 1,
Pabelan, Kartasura, Sukoharjo 57162, Indonesia
anita.sukmawati@ums.ac.id
Abstract. Beetroot (Beta vulgaris L.) was formulated into Microparticles (MP)
to maintain its antioxidant stability and control the release of active substances
for longer use. Chitosan was used as a matrix to encapsulate beetroot extract.
This study aims to determine the effect of chitosan concentration on drug loading, encapsulation efficiency, and release profile of betanin from MP containing
beetroot extract. Three formulas of microparticles were prepared using the ionic
gelation method with concentrations of chitosan 0.5% w/v, 1% w/v, and 2% w/v.
Encapsulation efficiency was analyzed using the direct method, and the release
profile of the active substance was evaluated using the dissolution method utilizing distilled water as a medium. The results showed that increasing the chitosan
concentration from 1 to 2% could reduce the encapsulation efficiency. The release
profile of beetroot extract microparticles from chitosan microparticles followed
the Higuchi model. The release rate constants of beetroot extract microparticles
revealed that using a 2% w/v concentration of chitosan could reduce betanin
release rate from beetroot extract microparticles compared to chitosan matrix
concentrations of 0.5% w/v and 1% w/v.
Keywords: beetroot · chitosan · drug release microparticle
1 Introduction
Beetroot (Beta vulgaris L.) has a potent antiradical and antioxidant activity from betalain,
consisting of betacyanin (red-purple) and betaxanthin (yellow) [1]. These compounds
have water-soluble properties and are easily degraded under the influence of pH, temperature, and light [2]. However, the antioxidant activity in beetroot has a limitation
on stability. Therefore, it is necessary to design a delivery system for the active substance that can effectively protect the stability of beetroot in the long term, such as
microencapsulation.
Encapsulation technique using Microparticle (MP) can be used to protect the core
substance from damage during the manufacturing and storage process by coating its core
material [3]. Microparticle (MP) is also a delivery system for active substances that can
© The Author(s) 2023
A. Sri Wahyuni et al. (Eds.): ICB-Pharma 2022, AHCPS 3, pp. 5–13, 2023.
https://doi.org/10.2991/978-94-6463-050-3_2
6
A. Sukmawati et al.
control their release, improving the stability of active substances. This microencapsulation technique can also be used to control the release of active compounds, provide
better stability active compounds, protect materials that are sensitive to the environment,
and protect against unwanted effects due to the influence of light, humidity, and oxygen
[4].
Moreover, microparticles (MP) are known to protect the active ingredients from factors that cause damage, such as changes in temperature, humidity, oxygen and microorganisms[5, 6]. In the manufacture of microparticles, it is necessary to have a matrix
for the active ingredient encapsulation process. Here, chitosan is a polymer that can be
used for the encapsulation process. Chitosan has amino and reactive hydroxy groups that
have the potential to be further modified [7]. In addition, chitosan has good adhesion
properties, minimal toxicity, mechanical strength, hydrophilicity, and stability [8].
As a microparticle polymer, chitosan has a positively charged primary amine group
that can be cross-linked to form a gel through ionic interactions with polyanionic compounds, including tripolyphosphate (TPP). Malangngi et al. [9] synthesized and modified a thin layer of chitosan-tripolyphosphate as a drug coating material to control drug
release. The cross-linked chitosan and tripolyphosphate formed were more stable to
swelling. Nussinovitch [10] also stated that chitosan-tripolyphosphate microparticles
have better mechanical strength, and the force required to break microparticles is about
10 times that of chitosan-sulfate or chitosan-citrate microparticles [10].
In the microparticle preparation process, the matrix’s concentration can affect the
microparticles’ characteristics, including the encapsulation efficiency (EE) of the active
ingredient on the matrix. To obtain good physical characteristics and absorption efficiency of active ingredients, it is possible to evaluate the appropriate matrix concentration in the manufacture of microparticles. The chitosan concentration as a microparticle
matrix can affect the release profile of the active ingredient from the microparticle
preparation. Research conducted by Sukmawati et al. [11] showed that the release of
doxorubicin and PGV-1 was influenced by the concentration of the chitosan matrix used
in the manufacture. The other research revealed that using sodium alginate as a matrix in
mefenamic acid microparticles reduced the release rate of active substances [12]. In this
research, the release profile of active antioxidant ingredients of beetroot from microparticle preparation was investigated. The various concentration of chitosan as a matrix in
MP were used to maintain the release of betanin for a long period and maintained for a
prolonged period.
2 Materials and Method
2.1 Material
The materials used in this study were beetroot (Beta vulgaris, Linn) obtained from
Cepogo, Boyolali, Central Java, Indonesia, tween 80, chitosan (MW 100–200 kDa, CV
Chi Multiguna, Indonesia), acetic acid glacial, sodium tripolyphosphate (Na TPP), citric
acid (Merck), distilled water, betanin (Aldrich). Unless otherwise stated, all materials
were in pharmaceutical grade and provided by Bratachem, Indonesia.
Release Profile of Betanin from Chitosan Microparticle
7
2.2 Preparation of Beetroot Dry Extract
A peeled beetroot (200 g) was cut into small pieces and mashed with 200 mL of 1%
citric acid until smooth using a blender. The mashed beetroot was then filtered using a
clean cloth to obtain the juice. The beetroot juice was then dried using freeze-dry until
the dry mass was obtained. The yield of dry beetroot powder using this process was
3.23%.
2.3 Preparation of Microparticle
The microparticle (MP) containing beetroot extract was made using three various concentrations of chitosan. A 1.25 g of chitosan was dissolved in 250 mL, 125 mL, and
62.5 mL of 1% acetic acid to give chitosan concentration 0.5%, 1%, and 2% w/v, respectively. The solution was stirred using a magnetic stirrer for two hours at a speed of
700 rpm to produce a clear chitosan solution. A 0.625 g of beetroot powder as an active
substance for each formula was dissolved in 5 mL of distilled water and added to the
chitosan solution. The mixture was stirred for ten minutes at a speed of 350 rpm. Tween
80 was then added to the mixture to give a concentration of 0.2% v/v to stabilize particles in the solution and prevent clumping between particles [13]. A 10 mL sodium
tripolyphosphate (Na TPP) 1% w/v as a cross-linking agent was added dropwise into
each formula using a sprayer. The solution was continuously stirred at 350 rpm for 24
h to perfect the cross-linking process. The solution was then centrifuged at 3000 rpm
for 15 min to precipitate the particle. The particle obtained was then washed three times
using 3 mL of distilled water. The wet particle was then dried utilizing a freeze dryer for
three days and stored at 4 °C in a container covered with aluminum foil.
2.4 Evaluation of Drug Loading (DL) and Encapsulation Efficiency (EE)
Beetroot extract’s Drug Loading (DL) and Encapsulation Efficiency (EE) were evaluated
using the direct method and calculated using betanin as a standard. A 50 mg of microparticle was dissolved in 1 mL of 1% glacial acetic acid to dissolve chitosan matrix and then
mixed with 4 mL of distilled water in the ratio of 1:4. Then, the solution was centrifuged
at 3000 rpm for five minutes to precipitate the chitosan debris. The absorbance of clear
solution was measured with a UV-Vis spectrophotometer (Genesys 10S) at 532 nm.
The amount of betanin in encapsulated beetroot extract was determined using betanin
calibration curve Y = 0.0002 x – 0.0325. DL and EE of betanin in MP were calculated
using Eq. (1) and Eq. (2).
DL (% w/w) =
EE (% ) =
amount of betanin in MP
× 100%
amount of microparticles
amount of betanin in MP
× 100%
amount of beetroot added
(1)
(2)
8
A. Sukmawati et al.
2.5 Evaluation of Betanin Release Profile from Microparticles
The release of betanin as the active substance from chitosan microparticles was carried
out using the dissolution method. A 250 mg of MP were dispersed in a 20 ml tube
containing 5 mL of distilled water as a dissolution medium. The tube was placed in a
shaking thermostatic water bath (Julabo SW 22) at 37°C ± 0.5 and shaking speed of
150 rpm. The betanin released from the MP was evaluated at certain time intervals from
2 to 180 min by taking out 5 mL of the dissolution medium. Before sampling, the tube
was centrifuged for two minutes at a speed of 3000 rpm. Therefore, the MP could settle
in the bottom of the tube. The dissolution medium was replaced with the same volume
in each sampling time. The clear sample solution was then measured using a UV-V
spectrophotometer (Genesys 10s) at 532 nm to evaluate the amount of betanin released
from the MP using betanin calibration curve Y = 0,0002 x – 0,0325. The amount of
betanin released from MP was then plotted into zero-order (Eq. (3)), first-order (Eq. (4)),
second-order (Eq. (5)), and Higuchi model (Eq. (6)) to determine the release kinetics of
active substance from MP.
C = K0. T
Log C = Log C0. −
(3)
K.t
2.303
(4)
1
1
=
+ K.t
C
C0
(5)
Qt = KH . t1/2
(6)
Whereas C is the concentration of betanin releases, C0 is the initial concentration of
betanin, K is the release constant, Qt is the amount of betanin released, KH is Higuchi
released constant, and t is time (minutes).
3 Results and Discussion
The drying process of beetroot extract was carried out using freeze-drying as the active
substance is susceptible to high temperatures. Betanin compounds in beetroot are affected
by temperature, pH, light, and oxygen; therefore, citric acid was used to maintain the
stability of betanin as an antioxidant. According to Kendall and Sofos [14], citric acid
was used to maintain pH stability and the natural color of a product due to the ability
of citric acid to decrease the pH of substances so that it can reduce the occurrence of
enzymatic browning and maintain the stability of color in the dry product.
Microparticle was made using the ionic gelation method. This method involves a
cross-linking process between the polyelectrolytes in the presence of their multivalent
ion pairs. The reaction mechanism involved the process of dissolving chitosan in 1%
glacial acetic acid solution through a protonation reaction. The amine group accepts
H+ released by acetic acid to become positively charged (−NH3 + ). The formation of
these ions causes the chitosan to be dissolved. The cross-linking process occurs when
Release Profile of Betanin from Chitosan Microparticle
9
Table 1. Drug Loading and Encapsulation Efficiency of Chitosan Microparticle Containing
Beetroot Extract in Various Chitosan Concentration
Chitosan Concentration (%)
Drug Loading (%w/w)*
Encapsulation Efficiency (%)a
0.5%
43.03 ± 2.091
86.05 ± 4.181
1%
46.07 ± 1.392
92.15 ± 2.785
2%
26.41 ± 1.259
52.40 ± 2.498
a calculated as betanin. Values represent mean ± SD (n = 3).
the positively charged amine group (cation) cross-linked with the negative group of the
tripolyphosphate polyanion to form a complex reaction [13].
Evaluation of DL and EE was carried out to evaluate the method’s effectiveness in
encapsulating an active substance. DL showed how much beetroot extract (calculated as
betanin) was entrapped inside the chitosan microparticles, while EE was used to describe
the beetroot’s effectiveness entrapment process of beetroot into microparticles. The DL
and EE of beetroot in chitosan MP with 0.5, 1, and 2% w/v chitosan concentration can
be seen in Table 1.
The highest drug loading results were obtained at 1% chitosan concentration, while
the lowest was 2%. According to Joshi et al. [15], increasing polymer concentration
will enhance the polymer’s cross-linking ability to bind the active substance, resulting
in higher drug loading and encapsulation efficiency. However, the DL obtained in this
study is not in accordance with Joshi’s statement because the microparticles with the
largest chitosan matrix concentration of 2% obtained the lowest DL value. According
to Ko et al. (2002), the high concentration of chitosan used in the formulation would
produce the high viscosity of the chitosan solution. As a result, it formed strong and
thick microparticle walls when interacting with Na TPP so that the swelling ability of
chitosan decreased. In addition, the high viscosity of chitosan increased the density of
the matrix; thereby, it reduced the ability of the chitosan to swell and absorb the active
ingredient [16]. Consequently, only a small amount of beetroot extract adsorbed within
the microparticle.
The t-test on the encapsulation efficiency data revealed that the chitosan matrix
concentration from 1% to 2% had a significant decrease in the EE of chitosan MP (p <
0.05), while the increasing chitosan matrix concentration from 0.5% to 1% showed no
significant difference in EE of chitosan MP (p > 0.05).
The release of the active substance from the chitosan microparticles is influenced
by the concentration of the matrix and the type of polymer used in the formulation.
Moreover, the release of the active substance from the matrix is also influenced by the
solubility of the active substance in the dissolution medium [17] and polymer viscosity,
polymer mixture, and particle size [18]. The result revealed that the cumulative percentages of betanin released in 180 min from MP chitosan in concentrations 0.5%, 1%, and
2% were 77.6% ± 4.68, 78.6% ± 4.78, and 66.2% ± 3.14, respectively (Fig. 1). The
highest cumulative percentage of betanin released was obtained at 1% chitosan concentration, and the lowest was obtained at 2% chitosan concentration. As the polymer
10
A. Sukmawati et al.
Fig. 1. Cummulative percentage of betanin relesed from chitosan microparticle with concentration 0.5% ( ), 1% ( ), and 2% ( ). Bar represents SD (n = 3).
concentration increased, it would reduce the diffusion rate, so the active substance had
a slower release profile [19].
Additionally, the MP at a concentration of 2% chitosan had the lowest encapsulation
efficiency. As a result, only a small amount of betanin was adsorbed in the matrix,
influencing the percentage of betanin released from the microparticle.
The kinetics of betanin release from beetroot extract microparticles was determined
by plotting the amount of betanin released to the zero-order, first-order, second-order, and
Higuchi model equations. The release kinetics of the active substance can be determined
from the R2 value of linear regression, which is close to 1. The R2 value of each released
model can be seen in Table 2. The R2 value close to 1 was found in the Higuchi model;
thus, the release kinetics of betanin from chitosan MP followed the Higuchi model.
The Higuchi model indicates that the active substance’s release mechanism is controlled
by diffusion [20]. All the MP in various chitosan concentrations had a Higuchi release
model, indicating that the polymer concentration did not affect the release model of
betanin from chitosan MP (p > 0.05). In general, the release of the active substance
from a matrix with low solubility in water will follow the Higuchi model [21]. The
release of the active substance from the polymer matrix can occur by diffusion, polymer
degradation, or both. Diffusion release occurs when the active substance flows through
the pores in the matrix or the spaces between polymer chains [12].
The release constant of betanin from chitosan MP was then determined using the
Higuchi release model. The greater the Higuchi constant, the greater the release rate and
vice versa. The Higuchi constant for release of betanin from MP showed that the slowest
release rate appeared at chitosan matrix 2% w/v (Table 3).
According to Saharan et al. (2015), the release of glipizide from microparticles with
poly-lactic acid (PLA) matrix decreased by increasing polymer concentration used in
the manufacture of glipizide microparticles [22]. In this research, the higher concentration of chitosan during the preparation of microparticles would increase the viscosity
of the environment; therefore, it induced the particle compaction process to be faster.
Consequently, the process of releasing the active substance would be delayed.
Release Profile of Betanin from Chitosan Microparticle
11
Table 2. The R2 Value of Betanin Release Profile by Plotting Using Zero-, First-, Second-Order,
and Higuchi model
Chitosan
R2 valuea
Concentration (%) Zero-order
First-order
Second-order
Higuchi
0.5
0.9094 ± 0.0094 0.6640 ± 0.0229 0.3637 ± 0.0332 0.9903 ± 0.0028
1
0.9072 ± 0.0071 0.6390 ± 0.0144 0.3206 ± 0.0154 0.9899 ± 0.0022
2
0.9324 ± 0.0070 0.7461 ± 0.0257 0.4751 ± 0.0318 0.9933 ± 0.0035
a Values represent mean ± SD (n = 3).
Table 3. Higuchi Release Rate Constant of Betanin from Chitosan Microparticle (n = 3)
Chitosan Concentration
(%)
Ka
(mg/min1/2 )
0.5
6.37 ± 0.190
1
7.02 ± 0.293
2
3.62 ± 0.1904
a Calculated as betanin. Values represent mean ± SD (n = 3).
The t-test statistical analysis on the betanin release profile from the microparticles of
beetroot extract revealed that increasing concentration of chitosan as an MP matrix from
0.5 to 1% w/v did not have a significant effect on the release rate of betanin from MP
(p > 0.05), whereas increasing chitosan to 2% w/v had significantly reduced in betanin
release rates from chitosan microparticle compared to chitosan 0.5 and 1% (p < 0.05).
4 Conclusion
The chitosan matrix used for beetroot MP preparation (0.5%, 1%, and 2% w/v) affected
the encapsulation efficiency and the release of betanin from MP. The chitosan 0.5%
and 1% showed the increasing value of encapsulation efficiency and release rate,
although it was statistically not significant. Meanwhile, at the chitosan concentration
of 2%, the release of betanin reduced. In conclusion, using a higher amount of chitosan
could diminish the encapsulation efficiency and the rate of betanin release from chitosan microparticles as a high concentration of chitosan induced high viscosity during
preparation.
Acknowledgment. We want to thank Universitas Muhammadiyah Surakarta for providing the
funding and facilities for this research through Hibah Integrasi Tri Dharma [Tri Dharma Integration
Grant] (HIT) Research Scheme.
12
A. Sukmawati et al.
Authors’ Contributions. Anita Sukmawati has contributed to organizing the general research
and publication; Isna V Risdiyanti and Clara C Marthadilla have contributed to data collection
and report.
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