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Research Article /«v https://doi.org/10.21603/2308-4057-2021-l-117-125
Open Access ' Available online at http:jfrm.ru/en
Optimization of canthaxanthin extraction from fermented biomass of Paracoccus carotinifacuens VTP20181 bacteria
strain isolated in Vietnam
Le Xuan Duy1'2, Tran Quoc loan1'2* , Dang Viet Anh1'2, Nguyen Phi Hung1, Trinh Thi Thu Huong1, Pham Quoc Long1, Nguyen Manh Dat3, Do Thi Thuy Le3, Dung Thuy Nguyen Pham4 , Nguyen Phu Thuong Nhan4'** , Do Van Manh5
1 Institute of Natural Products Chemistry, Hanoi, Vietnam 2 Graduate University of Science and Technology, Hanoi, Vietnam 3 Food Industries Research Institute, Hanoi, Vietnam 4 Nguyen Tat Thanh University"0", Ho Chi Minh, Vietnam 5 Institute of Environmental Technology, Hanoi, Vietnam * e-mail: [email protected] ** e-mail: [email protected] Received October 28, 2020; Accepted in revised form December 02, 2020; Published online March 5, 2021
Abstract:
Introduction. The bacterium strain Paracoccus carotinifaciens VTP20181 isolated in Vietnam produces canthaxanthin, a carotenoid widely used in the food and pharmaceutical industries. The aim of this work was to determine optimal parameters for canthaxanthin extraction from fermented biomass of P. carotinifaciens VTP20181.
Study objects and methods. First, a series of single factor investigations were carried out in regard to maximal carotenoid content in the biomass extract obtained by using ultrasonic waves. Four parameters of the extraction process, such as extraction temperature, solvent/material ratio, extraction time, and ultrasonic output power, were studied. The obtained results were then optimized by using Response Surface Methodology (RSM) and Box-Behnken experimental design.
Results and discussion. The optimal technological parameters of the extraction process included extraction temperature of 35°C, solvent/material ratio of 9.5:1 (v/w), extraction time of 90 min, and ultrasonic output power of 145 W. Under optimal conditions, canthaxanthin and total carotenoid contents were determined as 14.95 ± 0.12 and 18.21 ± 0.11 mg/g respectively, which were compatible with theoretical calculations - 15.074 and 18.263 mg/g, respectively.
Conclusion. Current results confirmed that the strain of halophilic P. carotinifaciens VTP20181 is a potential source for canthaxanthin biosynthesis.
Keywords: Paracoccus carotinifaciens VTP20181, canthaxanthin, total carotenoid, optimization, response surface methodology
Please cite this article in press as: Duy LX, Toan TQ, Anh DV, Hung NP, Huong TTT, Long PQ, et al. Optimization of canthaxanthin extraction from fermented biomass of Paracoccus carotinifacuens 20181 VTP bacteria strain isolated in Vietnam. Foods and Raw Materials. 2021;9(1):117-125. https://doi.org/10.21603/2308-4057-2021-1-117-125.
E-ISSN 2310-9599 ISSN 2308-4057
INTRODUCTION
Natural pigments derived from p-carotene exhibit many outstanding features, such as strong antioxidative properties and enhanced color persistence, and have been studied for feasibility in industrial and food applications [1, 2]. Experimental data and clinical trials proved beta carotene and its derivatives, such as canthaxanthin, astaxanthin, zeaxanthin and lutein, to be able to confer beneficial effects on human health. They
are able to remove free radicals, strengthen cell walls, as well as have anti-tumoral, immunity-enhancing and cell protecting capabilities that greatly contribute to prevention and treatment of cardiovascular diseases and obesity [3-6].
Currently, carotenoids are one of the natural pigment groups widely used in the food, pharmaceutical, cosmetic, and livestock industries [7-9]. The total value of products derived from carotene worldwide in 2015
Copyright © 2021, Duy et al. This is an open access article distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), allowing third parties to copy and redistribute the material in any medium or format and to remix, transform, and build upon the material for any purpose, even commercially, provided the original work is properly cited and states its license.
reached $1.21 billion and is increasing gradually, 3-5% each year. By 2025, the commercial value is estimated to reach USD $2 billion [10, 11].
Canthaxanthin (4,4'-diketo-y#-carotene) is a carote-noid with stable polyene backbone frame structure, which provides a better antioxidant effect [12-14]. This compound was discovered for the first time in an edible fungus called Paracoccus carotinifaciens and is now obtained from some plant species, crayfish, salmon, mushrooms, seaweed, and bacteria [15-18].
Although chemical synthesis of carotenoids has been long established, recent restrictions imposed on the use of synthetic chemicals in the food and pharmaceutical industries have called for more efficient production of pigments from natural sources. Engineered biosynthesis of canthaxanthin from microbial sources is an alternative to chemical sinthesis due to its advantages including health safety and independence from natural conditions [19]. Particularly, D. natronolimnaea HS-1 bacterial strain was identified as a suitable microorganism for industrial production of canthaxanthin, with canthaxanthin yield of 5.31 mg/L under optimal culture conditions in batch fermenter system [20, 21]. In Vietnam, some strains with high canthaxanthin production capacity, such as Staphyloccocus CNTP 4191, Staphyloccocus CNTP 4192, Haloferax alexandrinus NBRC 16590, and P. carotinifaciens VTP20181, were also isolated.
Extraction of carotenoids and beta carotene derivatives from bacterial biomass can be carried out by using various techniques. They are microwave ussisted-extraction, ultrasound-assisted extraction, pulsed electric field assisted e xtraction, and supercritical fluid extraction [22-25]. However, efficiency of such pro cesses vary greatly depending on technological parameters, surf20tants, and used solvents [26-30]. Therefore, further optimization of technological param^ers witn respect to output is necessary in process intensific ation at larger scale [31, 30 ].
This study was aimed to optimize canthaxanthin axtractian process 00om the biomass of thE bacterium P. carx-inifeciens VTP20181 isolated in Vietnam.
STUDY OBJECTS AND METHODS
The object of the study was dry biomass of Paracoccus carotMfacien3 VTP20i01 bacteria obtai^d after fermentation and spray dIeiag• The beomass was aocked in vaauum bags and refrigerated ait-4i0C te be prepared for theextrattien proteia.
Extraction. ExaTtiy WO g od ony biomass was weighed by usmg a PA214 analytical scale (OhausUS, China) anC transferred to a 2000 mL three-neck flask. Different volumes of solvents (7:1, 9:1, and 11:1, v/w) were added into the flask and shook to allow Convena peneteation into the biomass. The solvent was 96% food-grade ethanol supplemented with 0.5% glyceryl monostearate for more effective extration. The temperature was maintained at pre-determined levels by using the reflux condenser apparatus and a water bath.
A UP200Ht ultrasonic homogenizer with sonotrode S26d14 ultrasound head (Germany, 26 kHz, 0-200 W) was usedfor extraction. The ultrasonic power and time were also adjusted for investigation at certain research levels. The extract was separated from the solid phase through a Buchner funnel and concentrated to obtain the total extract that contained canthaxanthin and totsl caratenoids.
Determination of total carotenoid content. To
determine total caratenoids, we used the method of de Carvalho et al. with slight modifications [33]. First, 5 g of the biomass extraxt was extracted with 25 mL of acetone and filtered under vacuum. The permeate was re-extracted three times until the color of the obtained extract was transparent. Purified water was added to the obtained extract to prevent emulsion formation, then transferred to a 500 mL separatory funnel containing 40 mL of petroleum ether. Carotenoids will move to the petroleum ether phase (light phase), and the soluble acetone phase (dense phase) was removed. The separation was performed four times till no solvent was observed. Afterwards, water was removed from the petroleum ether phase by using anhydrous sodium sulfate in a 50 mL flask. To determine tottal caratenoid content (mg/g), the absorbance of the sample was read at 450 nm.
Carotenoids content = A x 10 (1)
A1 cm x p
where A is tru absorbance; V is tru to0al extract volume, mL; Pis tru sample weight, g; ( x p is tru /(carotene extinction coefficient of petroleum ether (( x p = 2592).
Determination of canthaxanthin content [34]. The reference standard, canthaxanthin (99% HPLC), was purchased fromSigma-Aldrich (Merck). Sigma-Aldrich also supplied methanol and and i-propanol usedintheexp
Analytical Hypersil Gold and detector ] (97:3, v/v) was degassed. The 1.0 mL/min at
80000 cs 60000
<D
H 40000 20000 0
0 100 200 300 400 500 600 700 Concentration canthaxanthin, ^g/mL
Figure 1 Calibration curve of canthaxanthin
all solvents (CHROMASOLV® grade chloroform, ethanol p.a., n-hexane p.a., p.a). Deionized water (c < 0.4 ^S/cm) was leriment.
HPLC was performed with a C-18 column (5^m; 150^4.6 mm)on a Thermo system PDA. The methanol-water mobile phase filtered through a 0.45 ^m membrane and analysis was carried out at a flow rate of room temperature. Chromatograms were
Calibration curve of canthaxanthin
y = 123.89x + 453 R2 = 0.9979
Table 1 Independent variables and their corresponding levels
Independent Variables Codes Variable Levels
range -1 0 1
(A)
Z1: Extraction A 5 30 35 40
temperature, °C
Z2: Solvent/material, v/w B 2 7 9 11
Z3: Extraction time, min C 30 60 90 120
Z4: Ultrasonic power, W D 20 120 140 160
Table 2 Experimental design and response values
Run A B C D Y 1, mg/g Y2 mg/g
1 -1 -1 0 0 11.08 ± 0.17 12.86 ± 0.13
2 +1 -1 0 0 11.39 ± 0.15 14.33 ± 0.17
3 -1 +1 0 0 12.73 ± 0.18 15.79 ± 0.19
4 +1 +1 0 0 12.60 ± 0.21 14.86 ± 0.15
5 0 0 -1 -1 12.35 ± 0.11 15.02 ± 0.11
6 0 0 +1 -1 9.68 ± 0.08 11.61 ± 0.18
7 0 0 -1 +1 12.17 ± 0.15 14.87 ± 0.19
8 0 0 +1 +1 12.45 ± 0.13 15.27 ± 0.16
9 -1 0 0 -1 12.06 ± 0.12 14.40 ± 0.12
10 +1 0 0 -1 12.01 ± 0.11 14.43 ± 0.13
11 -1 0 0 +1 13.21 ± 0.14 15.60 ± 0.18
12 +1 0 0 +1 13.26 ± 0.17 16.20 ± 0.12
13 0 -1 -1 0 11.72 ± 0.16 14.69 ± 0.11
14 0 +1 -1 0 11.58 ± 0.12 15.30 ± 0.17
15 0 -1 +1 0 8.87 ± 0.09 9.67 ± 0.08
16 0 +1 +1 0 11.81 ± 0.11 14.01 ± 0.11
17 -1 0 -1 0 11.22 ± 0.18 13.58 ± 0.18
18 +1 0 -1 0 12.74 ± 0.19 15.41 ± 0.19
19 -1 0 +1 0 12.55 ± 0.14 15.18 ± 0.15
20 +1 0 +1 0 11.31 ± 0.15 13.69 ± 0.16
21 0 -1 0 -1 11.93 ± 0.12 14.44 ± 0.13
22 0 +1 0 -1 10.51 ± 0.13 12.72 ± 0.13
23 0 -1 0 +1 10.17 ± 0.17 12.31 ± 0.15
24 0 +1 0 +1 13.26 ± 0.16 16.05 ± 0.18
25 0 0 0 0 14.39 ± 0.10 17.42 ± 0.14
26 0 0 0 0 15.21 ± 0.19 18.41 ± 0.12
27 0 0 0 0 15.20 ± 0.16 18.40 ± 0.13
recorded at 475 nm and used to determine the content of canthaxanthin in the sample, which was expressed as mg/g extract.
To prepare calibration standards, 2.5 mg of canthaxanthin standard was dissolved in 25 mL of chloroform to form the stock solution, which was stored at 12°C. The stock solution was then diluted with methanol to obtain standard solutions with known concentrations ranging from 100 to 700 ^g/mL. The standard solutions were then measured for peak area to build the calibration curve.
Experiment design and optimization. The canthaxanthin extraction process was optimized using the Response Surface Methodology (RSM), with canthaxanthin and total carotenoid contents as
Table 3 Estimated coefficients of the response models with canthaxanthin content and total carotenoid content as dependent variables
Source Y1, mg/g Y, mg/g
F-value P-value F-value P-value
Model 22.07 < 0.0001* 17.84 < 0.0001*
A 0.096 0.7620ns 0.034 0.8560ns
B 25.74 0.0003* 22.96 0.0004*
C 12.51 0.0041* 12.47 0.0041*
D 17.12 0.0014* 15.37 0.0020*
AB 0.28 0.6050ns 0.63 0.4450ns
AC 10.86 0.0064* 8.6 0.0126*
AD 0.013 0.9113 NS 0.09 0.7694 ns
BC 13.59 0.0031* 8.09 0.0148*
BD 29.21 0.0002* 23.12 0.0004*
CD 12.49 0.0041* 10.15 0.0078*
A2 29.17 0.0002* 22.22 0.0005*
B2 127.2 < 0.0001* 98.30 < 0.0001*
C2 115.01 < 0.0001* 92.81 < 0.0001*
D2 56.73 < 0.0001* 46.41 < 0.0001*
R2 0.9626 0.9542
Adj-R2 0.9190 0.9007
Adeq-Precision 18.589 16.489
*P < 0.05; ns = not significant
dependent variables. Experimental factors of the process included extraction temperature, solvent/material ratio, extraction time, and ultrasonic power. First, the factors were individually investigated to define a set of empirical values and the central range. Further, the obtained values were used in Box-Behnken model using Design-Expert 7.0 software to produce 27 sets of process parameters (Tables 1 and 2). Those sets were then actually attempted to collect data on canthaxanthin content and total carotenoid content, which were fitted in two second-order polynomial equations [35].
The analysis of variance (ANOVA) was carried out to determine the compatibility of the model. The second-order equation representing the general function form of one desired outcome with respect to independent variables looks as follows:
Y = bo + j bjXj + Jj buiXuX j + j j2 (2)
where, Y is the respone variable, X is independent variables, and k is number of tested variables. b0 is the intercept coefficient; b is the linear coefficient; b.. is the square coefficient and buj istheinteraction coefficient.
RESULTS AND DISCUSSION
Single factor investigation. Based on some preliminary investigations of canthaxanthin extraction from microbial biomass, we selected the initial parameters for this process: extraction temperature of 35°C, solvent/material ratio of 9:1 (v/w), extraction time of 90 min, and ultrasonic power aof 160 W. In our investigations, we varied only one of the selected6
—i-130 35 40 45 50 Extraction temperature, °C
(a)
„M M
ten
0 no c
'o
s
1 o
ao H
25
220
15
10
30 60 90 120 Eiittaction time, min
(c)
150
18 15 12
9 6 3 0
20 15 10
55
1
M
fl o
c c
nxatinhitxhann §
O
-22? m
o n te
trcoa5 c
3
o
H
20 -i
o
H
Solvent to material ratio (b)
20 15 10 5
I I I
■■ 1
100 120 140 160 180 Ultrasonic power, 15
(d)
15
10 a J3
5 xa
Total c-toiaeoiP coeiaei
acnathnathxaxnathnitnh icnocnotenntet nt
Figure 2 E0fect of axtraction temperature (a), solvent/material ratio (b), extraction time (c), and ultrasonic power (d) on the total carotenoid content and canthaxanthin content from dried extract
5
0
0
0
0
conditions, nther three conditions were kept at their initial levet s .
Firefly, we investigated the effects of temperature on the extraetion process (Fig. 2a). Temperature ranged from 30 to 50°C with a 5°C interval. At 30°C, the obtained total carotenoid content and canthaxantOin content reached 17.6 and 14.2 mg/g, respectively. As the temperature was increased from 30 to 35°C, the extraction efficiency increased rapidly and reached its maximum at 35°C, with a total carotenoid content of -U.( mgog nod canthaxanthin content of 14.9 mg/g. When the temperat r continued being increased to 40 and to 50°C, the total carotenoid and canthaxanthin contents tended to decrease gradually and reached the lowest values of 15.7 and 12.5 mg/g, respectively, at 50°C. The results were completely consistent with Aflaki as well as Das and Bera who studied effects of temperature on carotenoid extraction [36, 37].
The increasing of the temperature from 30 to 35°C improved efficiency extraction due to the increased carotenoid diffusion capacity and decreased solvent viscosity, which allows for better penetration of the solvent into the material. However, elevating the temperature past 40°C can degrade or oxidize carotenoid compounds. Therefore, to ensure the highest efficiency of canthaxanthin and total carotenoid extraction, we
selected 35°C as the optimum temperature for successive experiments. The low level (-1) and the high level (+1) were 30 and 40 °C, respectively (Table 1).
In the next experiment, a solvent/material ratio was varied from 5:1 to 13:1 (v/w). Figure 2b shows that the increase of the solvent/material ratio from 5:1 to 9:1 increased significantly canthaxanthin and total carotenoid contents from 10.2 to 15.1 mg/g and from 14.7 to 18.2 mg/g, respectively. When the ratio was increased to 11:1 and 13:1, canthaxantOin and total carotenoid contents were almost unchanged. Our results were entirely consistent with those of other researchers [37, 38].
Solute concentrations of the material and solvent significantly differed, according to the equilibrium principle, the outward movement of solutes from intracellular spaces into the solvent occurred at high speed. When equilibrium was attained, the diffusion process would gradually slow down despite the increase in solvent volume. Therefore, the solvent/material ratio of 9:1 was selected as the optimum ratio. The low level (-1) and the high level (+1) were 7:1 and 11:1, respectively (Table 1).
Figure 2c demontrates the effect of time (30 to 150 min) on the extraction process. With increasing extraction time from 30 to 90 min, canthaxanthin
Duy L.X. et al. Foods and Raw Materials, 2021, vol. 9, no. 1, pp. 117-125 Table 4 Empirical second-order polynomial model of canthaxanthin and total carotenoid contents
Response Model Equations R2 P - value
Y1 (total canthaxanthin content) Y1 = 14.94 + 0.61B - 0,43C + 0.5D - 0.69AC + 0.77BC + 0.9626 < 0.0001
+ 1.13BD + 0.74CD - 0.98A2 - 2.04B2 - 1.94C2 - 1.36D2 (1)
Y2 (total carotenoid content) Y2 = 18.07 + 0.79B - 0.58C + 0.64D - 0.83AC + 0.81BC + 0.9542 < 0.0001
+ 1.36BD + 0.9CD - 1.16A2 - 2.44B2 - 2.37C2 - 1.67D2 (2)
(b)
Figure 3 Response surface of canthaxanthin content (a) and total carotenoid content (b)
content increased from 6.4 to 15.0 mg/g, and total carotenoid content increased from 9.3 to 18.2 mg/g. When the extraction time was increased from 90 to 150 min, canthaxanthin and total carotenoid contents did not change significantly. Similar results were found by Roohinejad et al. and Strati and Oreopoulou [39, 40].
Initially, an increase in extraction time allowed more solutes to diffuse into the solvent. However, at a certain threshold, equilibrium will be established, and even a significant increase in extraction time does not produce any noticeable change in extraction yield. Therefore, to ensure the extraction efficiency and the energy and time
Duy LX. et al. Foods and Raw Materials, 2021, vol. 9, no. 1, pp. 117-125 Table 5 The values of the independent and real variables
Independent variables Real variables
ABC D Extraction temperature, °C Solvent/material ratio Extraction time, min Ultrasonic power, W
"001 023 -0.02 027 35 95 90 145
Table 6 Predicted response values and experimental response values obtained under optimum conditions
Dependent variables Optimum value
Experimental Predicted
Y1, mg/g 14.95 ± 0.12 15.074
Y2, mg/g 18.21 ± 0.11 18.263
optimization of the process, we selected an extraction time of 90 min as the baseline for the next experiment. The low level (-1) and the high level (+1) were 60 and 120 min, respectively (Table 1).
Lastly, we investigated the effect of ultrasonic output power, which was in a range of 100 to 180 W, on canthaxanthin and total carotenoid contents (Fig. 2d). The results show that increasing the ultrasonic power from 100 to 140 W increased sharply canthaxantOin and total carotenoids from 12.3 to 15.2 mg/g and 14.5 to 18.3 mg/g, respectively. Further increasing the ultrasonic power to 160 W caused a slight reduction in the canthaxanthin and total carotenoid contents to 15.1 and 18.1 mg/g, respectively. When output power reached 180 W, both canthaxantOin and total carotenoids decreased rapidly to 14.8 and 17.7 mg/g.
This is because ultrasonic waves act as agents breaking down the cell membrane of materials, which makes the diffusion process easier. However, when the ultrasonic power exceeds the threshold, the excessive number of air bubbles slows down the extraction process. The contact surface between the raw material and the solvent diminishes, resulting in reduced performance. Similar results were revealed by Yan et al. [41]. Therefore, ultrasonic power of 140 W was selected for the futher experiments. The low level (-1) and the high level (+1) were 120 and 160 W, respectively (Table 1).
Estimation of RSM model and statistical analysis.
Two models corresponding to the two target functions, namely canthaxanthin content (Y) and total carotenoid content (Y2), were estimated using data from the experiments guided by the Box-Beheken design. Four independent variables were extraction temperature, extraction time, solvent/material ratio, and ultrasonic output power. After the estimated function had been obtained and optimal conditions had been calculated, real experiments were performed to verify those optimal conditions and to determine model validity.
Based on separate single factor investigations, 27 experiments were conducted according to the experimental design matrix. To justify Y1 and Y2 response functions, F-, P-, and R2-values were used to
evaluate the linear regression analysis results (Table 3). Based on the regression results, canthaxanthin content (Y1) and total carotenoid content (Y2) could be described as independent variables of second-degree functions, as shown in Table 4.
The significance of the regression was also confirmed by F-values for Y1 and Y2, which achieved the value of 22.07 and 17.84, respectively and the very low P-value (P < 0.0001) (Table 3). The coefficients of determination (R2) of the two equations were 0.9626 and 0.9542, suggesting that 96.26 and 95.42% of variability in canthaxanthin and total carotenoid content were explainable by experimental results, respectively. Besides, the value of Adj-R2 (0.9190 and 0.9007, respectively), also showed the high accuracy of the experimental data in the limited range.
Regression equations (1) and (2) showed that all four technological factors (A, B, C, and D) affected the target function's value. Of which, extraction temperature (A) exerted the minimal direct impact on the value of the target function and influenced the responses mostly through its indirect interaction with extraction time (AC) and square interaction (A2). The remaining three variables had a significant influence on the target functions through linear effects (B, C, D). Among them, single variables B and D had a positive effect on the target functions, while variable C had an inverse effect on the target functions corresponding to their coefficients in the regression equation (1) and (2). The influence of the technological variables on the target function could be ranked descendingly by the impact magnitude as follows: B > D > C > A.
Response surface analysis. Three-dimensional response surface spaces were plotted by using Design Expert software. The X and Y axes of the response surfaces in three dimensions represented the two varying factors, while other factors where held at their central values. The Z-axes represented one of the two target functions: canthaxanthin content, and total carotenoid content.
The red areas on the response surfaces represented pairwise combinations that gave desirable outcomes of Y1 or Y2 and depended on the magnitude and the sign of the component variable that formed the response. For example, C exhibited negative signs in both (1) and (2). Therefore, the area that corresponded to optimal outcomes of Y1 and Y2 in the surfaces constituted by C was smaller than those of remaining pairs without C (AD, AB and BD).
Optimization and model verification. The optimal values of independent variables were determined by
16.2127 10.6715
18.4079
Figure 4 Optimum conditions by solution of ramps
Y2 = 18.2535
Y. = 16.0738
solving the quadratic regression equation with respect to maximal canthaxanthin and total carotenoid content. The importance of canthaxanthin content (Yj) and total carotenoid content (Y2) was selected as at level 4 and level 3, respectively. Predicted values showed that canthaxanthin content and total carotenoid content attained their maxima with the following conditions: extraction temperature of 35°C, extraction time of 90 min, ultrasonic output power of 145 W, and solvent/ material ratio of 9.5:1 (v/w). (Table 5, Fig. 4). Under optimized conditions, predicted and actual values of canthaxanthin content and total carotenoid content (Table 6) were approximately equal to each other, we could once again assert that our established model had a high compatibility.
CONCLUSION
In this study, the surface response methodology combined with the experimental design of Box-Behnken model was applied to optimize the extraction process of canthaxanthin from fermented biomass of Paracoccus carotinifaciens VTP20181 bacteria isolated in Vietnam. We used four independent variables: extraction time, extraction temperature, ultrasonic output power, and solvent/material ratio (v/w). Dependent variables were canthaxanthin content and total carotenoid content.
The obtained optimized conditions for the extraction process were: extraction time of 90 min, extraction temperature of 35°C, ultrasonic output power of 145 W, and solvent/material ratio of 9.5:1. Under these conditions, canthaxanthin and total carotenoid contents were 14.95 ± 0.12 and 18.21 ± 0.11 mg/g, respectively. Theoretical calculation models were completely compatible with the experiment.
CONTRIBUTION
Investigation - L.X. Duy, T.Q. Toan, D.V. Anh, N.P. Hung, T.T.T. Huong, N.M. Dat, D.T.T. Le, D.T.N. Pham, N.P.T. Nhan, and D.V. Manh. Supervision - P.Q. Long. Original draft writing - L.X. Duy and P.N.T. Dung. Review writing and editing - D.T.N. Pham.
CONFLICT OF INTEREST
The authors declare no conflict of interest.
ACKNOWLEDGMENTS
This research was funded by project code No. 10.17/CNSHCB under the project of Biotechnology Development and Application in the Manufacturing Industry to 2020 of the Ministry of Industry and Trade.
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ORCID IDs
Tran Quoc Toan https://orcid.org/0000-0003-0760-5750 Dung Thuy Nguyen Pham http://orcid.org/0000-0003-2396-9474 Nguyen Phu Thuong Nhan https://orcid.org/0000-0002-3494-7230
