Optimization of Extraction conditions of the Polyphenols, Flavonoids and the Antioxidant activity of the plant Ammosperma cinereum (Brassicaceae) through the Response Surface Methodology (RSM)

 

Bouaziz-Benzid Amina1, Hammoudi Roukia1, Hadj Amahammed Mahfoud1,  Tlili Ahlem1, Bouaziz Sabrina2, Bekka Chahrazed3, Mesrouk Houria1

1Biogeochemistry Laboratory of Desert Environments. Univ. Kasdi Merbah Ouargla, Ouargla 30000, Algeria

2Ecosystems Protective Laboratory of Arid and Semi-arid Zones. Univ. Kasdi Merbah Ouargla, Ouargla 30000, Algeria

3Valuation and Promotion of Saharan Resources Laboratory. Univ. Kasdi Merbah Ouargla, Ouargla 30000, Algeria

*Corresponding Author E-mail: benzidamina2@gmail.com

 

ABSTRACT:

This work focuses on the optimization of the extraction conditions, to extract the maximum polyphenols (TPC), flavonoids (TF) and for optimal antioxidant activity by the response method to (RSM) areas, from the aerial part of Ammosperma cinereum. Independent variables considered are: the methanol percentage (X1: 60-100%), temperature (X2: 20-60°C) and the extraction time (X3: 20 -100 min). Results of ANOVA showed that the proportion of methanol, the temperature and duration of extraction affected TPC and TF, while the antioxidant activity was affected only by the methanol rate. The experimental data were well adjusted by polynomial models of the second order with R2 = 0.986, 0.962 and 0.985 for TPC, TF and I% respectively (p <0.005). In addition, there's a close relationship between the predicted and experimental values. The optimum conditions for the highest performance of TPC (34.16 ± 0.24 mg EAG / g of extract), TF (29.37 ± 1.09 mg ER / g of extract) with 64.82% (± 0.26) of the antioxidant activity were obtained X1 = 93.1%, X2 = 36.9 ° C and for X3 = 66.8 min.

 

KEYWORDS: Ammosperma cinereum, RSM, Box Behnken, TPC, TF, antioxidant activity.

 

 


INTRODUCTION:

Recently, there has been a renewed interest in the plant secondary metabolites for their potential preventive effects on chronic diseases such as cardiovascular disease and cancer. Therefore, the isolation, identification and quantification of phytochemicals in food and assessment of their potential health benefits have been highlighted: However, in vitro and in vivo studies have shown that action of certain chemicals can be obtained by eating certain plants. Thus, extraction of the active ingredient is essential if it is to have a prophylactic or therapeutic value in humans1.

Phenolic compounds are common dietary phytochemicals found in fruits, vegetables and plant seeds2. The main feature of polyphenols is that they are very powerful antioxidants. Indeed, they are able to trap free radicals and activate other antioxidants in3,4 the body.

 

Ammosperma cinereum is a fairly gracile plant of the Brassicaceae family, it is localized only in southern Algeria. It is endemic to North Africa, annual and spontaneous5.

 

To date, no work has been done on the chemical composition or the optimization of extraction conditions, agronomic and zoological studies are cited in the literature.

 

The total phenols, flavonoids and antioxidant activity of aqueous methanol extract of Ammosperma cinereum can be affected by many factors. To surmount this problem, the optimization of extraction conditions was undertaken using multivariate statistical techniques. Among the most relevant techniques used in analytical optimization, figures the response surface methodology (RSM).

 

The objective of this study was to optimize the extraction conditions, including the proportion of methanol, the temperature and the extraction time, to improve the antioxidant activity, the content of total phenols and flavonoids of the Ammosperma cinereum plant aerial part by the response surface methodology using the Box Behnken design.

 

MATERIEL AND METHODS:

Plants:

Ammosperma cinereum was collected in its natural habitat. Harvesting is carried out in the region of Oued Souf (Latitude: 33° 21'21 ''North, Longitude: 6° 51'47 ''East Algeria). The botanical identification of the species was made by the botanist EDDOUD Mr. Amar (Univ kasdi merbah Ouargla). The harvest of the plant material was performed May 17,2017 at the stage of full bloom. The collected portions were dried at ambient temperature and sheltered from light.

 

Preparation of extracts:

Series of extractions were carried out by maceration of a quantity (0.5g) of vegetable matter obtained above in a volume (5mL) of extraction solvent to determine the methanol percentage (X1)% Temperature (X2)°C and the time (X3) min. extraction.

 

Determining the content of phenolic compounds:

The total polyphenol content of the extracts was determined using the Folin-Ciocalteu6, 7. 150µL of each extract (1mg/mL) were added to test tubes, to which 750 uL of Folin-Ciocalteu at (10%) are added. After 10 minutes, 2000µL of sodium carbonate was added (Na2CO3) to 7.5% (w / v). After 30 minutes of incubation in the dark, reading the absorbance of each solution was determined at 765 nm using a UV-VIS spectrophotometer (UNICAM). All measurements are repeated three times. The total phenolic content (TPC) is expressed as mg equivalent gallic acid per mg of extract (EAG/mg of extract).

 

Determination of the flavonoid content

The extracts flavonoids content was determined according to the method of aluminum trichloride7, 8; A 1.5 mL of each extract (1 mg/ml), are added 1.5mL of aluminum trichloride (AlCl3) to 20% (m/v) in distilled water. After incubation in the dark for 30 minutes at room temperature, the assay was performed by UV/Visible spectrophotometry at 430 nm. All operations are repeated three times. The flavonoid concentration (TF) is expressed as mg ER (equivalent of Rutin) per mg of extract.

Antioxidant activity:

The antioxidant capacity of each extract concentration of 1mg/ml, was determined in vitro by the inhibition test (O2.-) according to the method of H. Li et al. (2007)9 with some modifications. The test is based on self-oxidation of pyrogallol (benzene-1,2,3-triol) which is used as anion source (O2.-).

 

4.5mL of the phosphate buffer solution (pH = 8.2) were added in a tube, 0.5mL of each extract. The reaction was initiated by adding 10mL (45mM) of pyrogallol. The absorbance of reaction mixture was measured at 320 nm every 30 seconds3. The rate of inhibition of the autoxidation of pyrogallol is calculated by using the following equation:

 

I% = [ΔA0 - dA / ΔA0] x 100

 

Where: ΔA0 is the speed of the self-oxidation of pyrogallol in the absence of antioxidant, ΔA is the speed of the self-oxidation of pyrogallol in the presence of antioxidant.

 

Method Answer area:

Box-Behnken design:

The method of response surfaces (MSI) consists of a collection of mathematical and statistical approaches to achieve the optimization of a process. Among the most widely used designs, is the Box-Behnken (BBD), which is effective and especially suitable for testing of three variables of three levels10. This method is used to optimize the extraction factors, namely the methanol percentage (%), temperature (°C) and the extraction time (min.). Each of these three coded levels  -1, 0, and 1 (low, medium, and high, respectively) (Table 1).The response values ​​are the polyphenol content (Y1), flavonoids (Y2) and antioxidant activity (Y3). The experimental design has fifteen experimental trials that included twelve point factorial and three central points. The combinations of variables in these tests are described in Table 2.

 

Multiple linear regression and other statistical analyzes were performed using Minitab 17® software. Experimental data have been adjusted by the second-order polynomial model according to the following equation:

 

 

where is the expected response,is the constant of the model; And are independent variables; and  are linear coefficients; , are cross-product coefficients; and ' are the quadratic coefficients [11]. The goodness of fit of the equation 'model polynomial was expressed by the ratio R2[12]

 

The linear coefficients, quadratic, and interaction were determined by least squares regression, followed by analysis of variance (ANOVA). Values ​​of P <0.05 were considered significant.

Table 1: The independent variables and their levels encoded for 'Box-Behnken Design'

 

Varying levels, coded

independent variables

-1

0

1

X1 (%)

60

80

100

X2 (° C)

20

40

60

X3 (min)

20

60

100

 

Model Verification:

The extraction conditions were numerically optimized for maximum content of TPC, TF and with high antioxidant activity based on regression analysis and plots of 3D surface (studs area) of the independent variables. Responses were determined under normal conditions of extraction. Finally, predictable values ​​were compared with experimental ones to assess the validity of the model.

 

RESULTS AND DISCUSSION:

In this study, the relationship between the response functions and process variables, has been identified by design box Behnken and registered by three factors. In addition, the extraction conditions of total polyphenols, flavonoids and antioxidant activities were optimized.

 

The Table 2 illustrates the results of planned and experimentally measured responses for the 15 tests according to the experimental design. The performance of TPC and TF extends EAG 12.66mg/g extract (X1 = 100%; X2 = 60°C; X3 = 60 min) to 38.29 mg EAG / g of extract ( X1 = 80%; X2 = 40 ° C; X3 = 60 min), and 15.71 mg ER / g of extract (X1 = 60%; X2 = 40°C; X3 = 20 min) to 31.64 ER mg / g extract (X1 = 100%; X2 = 20°C; X3 = 60 min) respectively.

 

In terms of antioxidant activity, the ability of trapping of superoxide anion radical I% stretched from 36.94% (X1 = 60%; X2 = 60°C; X3 = 60 min) to 72.79% (X1 = 100%; X2 = 60°C; X3 = 60 min). Based on these data, the extraction process was optimized to obtain the desirable responses to the fullest.

 

Statistical analysis and model fitting:

The matrix of the Box-Behnken design applied with experimental and predicted responses for TPC, TF and I% are shown in Table 2. The results of the analysis of variance (ANOVA) showed a significant result for the model. Overall, the experimental data were well fitted by polynomial models of the second order (R2 = 0.986, 0.962 and 0.985 for TPC, TF and I% respectively). Moreover, a close relationship between the experimental values ​​and the predicted values ​​indicate that the developed model is highly satisfactory.


 

Table 2: Design Box-Behnken with the experimental and predicted values ​​for TPC, TF and I%.

S. No.

 

 

 

TPC (EAG mg / g of extract)

 TF (ER mg / g of extract)

I%

 

X1 (%)

X2 (° C)

X3 (min)

experimental

predictive

experimental

predictive

experimental

predictive

 

80

20

20

18.91

18.80

18.82

19.6575

54.4

55.94

 

80

40

60

40.1

39.24

26.78

26.72

60.87

61.19

 

60

20

60

28.7

27.60

20.93

19.29

64.38

64.96

 

60

40

100

27.04

26.25

21.46

22,30

56.05

56.75

 

80

20

100

26.41

28.28

26.25

27.03

49.26

47.96

 

80

60

20

19.75

17.87

20.64

19.85

44.33

45.62

 

80

40

60

38,29

39.24

26.09

26.72

61.15

61.19

 

100

40

100

18.29

17.09

29.64

28.84

71.07

73.2

 

80

60

100

15.58

15.68

20.6

19.76

56.44

54.89

 

80

40

60

39.33

39.24

27.3

26.72

62.05

61.19

 

100

40

20

14.75

15,53

28.21

27.36

65.76

65.05

 

60

60

60

29.12

29.79

19.43

19.41

36.94

37.77

 

100

20

60

30.16

29.48

31.64

31.65

49.26

48.42

 

100

60

60

12.66

13.75

22.82

24.45

72.79

72.20

 

60

40

20

19.33

20.52

15.71

16.50

65.74

63.61

 


The results of the ANOVA of the regression model, the linear terms, quadratic and interaction are highly significant (0.000 <P <0.008) for TPC and I% but TF for the linear terms are highly significant (P = 0.001) and quadratic terms are significant (P = 0.042) against by the interaction terms are not significant (P = 0.058) (Table 3).

 

Polynomial equations of the second order of answers:

TPC = -163.5 + 3.227 2.323 + X1 X2 + X3 1.210 - 0.01799 X1 * X1 - X2 * X2 0.01721 - 0.007620 * X3 * X1 X2 X3 -0.01120 - 0.00130 X1 * X3 - 0.00365 X2 * X3

 

TF= -39.4 + 0.650 + 0.937 X1 X2 X1 * 0.438 X3- 0.00105 0.00649 X1- X2 * X2 X3 * 0.001592 -0.00458 X3- X1 * X2 - X1 * 0.001350 X3- 0.002334 X2 * X3

 

I% = X1 206,6- 2.939 -1.008 -0.529 X2 X3 + X1 * 0.01004 0.02383 X1- X2 * X2 - X3 0.000449 - 0.03186 * X3 + X1 * X2 + X1 * X3 0.00469 - 0.00539 + X2 * X3

 

All mathematical models obtained have proved suitable for the analysis of the response surface, as no evidence was insufficient detected by the inadequacy of fit test (P> 0.05) [12].


 

Table 3:  Adjusted quadratic model in terms of coded variables for responses Y1, Y2 and Y3.

 

Y1 (TPC)

Y2 (TF)

Y3 (I%)

 

R2

R2Ajusted

R2

R2Ajusted

R2

R2Ajusted

 

98.61%

96.11%

96.08%    

89.04%

98.48%    

95.75%

Source

DL

value F

Value p

DL

value F

p value

DL

value F

p value 

Model

9

39.43

0,000

9

13.63

0.005

9

36.08

0,001

Linear

3

22.59

0,002

3

29.59

0,001

3

13,19   

0,008

 Quadratic

3

83.54

0,000

3

6.63

0,034

3

33.24   

0,001

Interactions 2 factor

3

12,27   

0,010

3

4.67

0,065

3

61.80  

0,000

Fault

5

 

 

5

 

 

5

 

 

The inadequacy of adjustment

3

5.85

0,150

3

9.66

0,095

3

17.78

0,054

pure Error

2

 

 

2

 

 

2

 

 

Total

14

 

 

14

 

 

14

 

 

 

Table 4: The coded coefficients of regression adjusted quadratic model responses for Y1, Y2 and Y3.

 

TPC

TF

I%

coefficients

p value

coefficients

p value

coefficients

p value

Constant

39.24

0,000

26.723

0,000

61.36

0,000

X1

X2

X3

-3.541

-3.384

1,823

0,003 *

0,003 *

0,035 *

4,348

-1.759

1,821

0,000 *

0,021 *

0,019 *

4,471

-0.85

0.324

0,002 *

0.294

0.674

-7.195

-6.885

-12.193

0,001 *

0,001 *

0,000 *

-0.420

-2.598

-2.548

0.616

0,021 *

0,023 *

4.02

-9.53

-0.72

0,013 *

0,000 *

0.531

X1X2

X1X3

X2X3

-4.484

-1.043

-2.917

0,004 *

0.298

0,023 *

-1.83

-1.08

-1.867

0.06 *

0.212

0,056

12.74

3.75

4.31

0,000 *

0,015 *

0,008 *

* Significant difference with p <0.05.

 

  

Fig. 1: The three-dimensional plots showing the effects of the solvent concentration (x1) and temperature (x2) on TPC, TF and I% of the plant Ammosperma cinereum for t = 60 min.

 

 

Fig. 2: The three-dimensional plots showing the effects of the solvent concentration (x1) and time (x3) on TPC, TF and I% of the plant Ammosperma cinereum for T = 40 ° C.

 

Fig. 3: The three-dimensional plots showing the effects of temperature (x2) and time (x3) on TPC, TF and I% of the plant Ammosperma cinereum for C = 80%.

 


Effect of extraction conditions on the total content of polyphénols:

The percentage of methanol (60-100%) has a significant influence on the TPC level in the linear first-order (p <0.003) and second order (p <0.001). The regression coefficients for this factor were negative values, indicating that increasing the ratio of methanol resulted in a decrease of the TPC content; when the methanol concentration was increased by 60% to 100%, a reduction of the phenol content of from 38.29 to 12.66 mg EAG / g extract was observed (Fig. 1). Since extraction and separation of the phenolic compounds are largely dependent on the polarity of solvents and compounds, a combination of alcohol and water is more effective than alcohol alone to remove phenolic compounds13, 14. This tendency to the reduction of extraction capacity with increased alcohol ratio in the solvent has been reported in black tea extracts where the hydro-alcoholic extracts 50% have the highest content of TPC, followed respectively by 80 and 100% aqueous alcohol15. Further, in optimizing the extraction of phenolic compounds from plant Mangifera Pajang and Kosterm peels, the content in the extracts TPC began to decrease after reaching the lower maximum operating conditions of 68% acidified aqueous methanol and 38 min of extraction time16.

 

With regard to the extraction temperature, the TPC increases with increase in temperature to some extent and then decreases (Fig. 1 and Fig. 3). An increase in extraction temperature can break the bonds of the phenolic matrix and influence the membrane structure of plant cells, making them less selective due to the coagulation of lipoproteins17. The dielectric constant of water decreases and the solvent property and ability to change to a higher temperature, resulting in a better extraction of phenolic compounds18. A higher temperature may also increase the phenolic content by increasing phenolic solubility, diffusion rate, the rate of extraction, the decrease in viscosity and surface tension of the solvent19. However, an increase in extraction temperature could degrade phenolic compounds, because of the interference of the stability of the compounds, caused by chemical and enzymatic degradation or reaction with other herbal ingredients reducing the effectiveness extraction20. Pompeu D. R et al (2009)21 reported a maximum temperature of 58°C to obtain the highest phenolic content of Euterpe oleraeceae fruit. While Gan, C. et al (2011)22 have obtained a higher content of phenolics in the pod stinking beans at a temperature of 35°C. In addition, the extraction time used was 100 minutes. Increasing the extraction temperature will be useful to increase the extraction efficiency and to reduce the extraction time23.

 

Figure 3 illustrates the influence of time and temperature on the extraction of TPC. The linear effect of duration and quadratic effect of temperature have been clearly expressed. Note that the two factors (time and temperature) act independently on the TPC (Table 4).

 

The mass transfer of the plant material and solvent are related to the duration and temperature. For a long high temperature extraction period, the negative quadratic effect became significant. A higher extraction temperature above 36.9°C showed no significant improvement in the extraction of TPC. This can be attributed to thermal degradation at high temperature antioxidants, favoured by a long extraction24, indicating that the extracts contain heat sensitive compounds.

 

Effect of extraction conditions on flavonoid content and antioxidant activity:

According to the regression coefficients (Table 4) and three figures 1, 2 and 3, it is found that the duration and the methanol proportion positively affect the extraction of TF and antioxidant activity.

 

The TF and I% increased significantly with increasing extraction time of 20 minutes to 60 minutes. After 60 min, there was a slight decrease in TF and I%. This could be due to the decomposition of active compounds during the extraction process when extended25, 26, 27.

 

Whereas when the proportion of methanol increases from 60% to 100%, the TF and I% increase (Fig. 2). The significant (p <0.05) TF and I% values increase ​​with an increased content of methanol was expected and consistent with the findings of Yu J et al (2005)28 according to which a majority of phenolic compounds were extracted at higher rate in methanol. Thus, our results suggest that a higher concentration of methanol increases significantly the extraction of these phenolic compounds (flavonoids) that could effectively eliminate free radicals.

 

At high temperatures, extraction improves both the solubility of the solute and the diffusion coefficient (decreased solvent viscosity and increase the mobility of the molecules), but its elevation cannot indefinitely increase the yield of phenol extraction. In extreme temperatures, the yield may be reduced by chemical and thermal degradation of certain polyphenols, which explains the decrease in antioxidant activity29, favoured by degradation of certain heat-sensitive compounds24, 30.

 

CONCLUSION:

The Box-Behnken design has been successfully used to optimize the extraction of polyphenols, flavonoids and antioxidant activity of the aerial part of Ammosperma cinereum by maceration. The optimum conditions to maximize yields of each response have been proposed to be 36.9°C for 66.8 min with 93.1% methanol. In addition, reconciliation between the predicted responses and experimental results shows a satisfactory predictive ability of developed mathematical models. These proposed conditions present significant advantages in terms of short treatment time and low temperature.

 

CONFLICTS OF INTEREST:

The manuscript represents valid work, neither this manuscript nor one with substantially similar content under my authorship has been published or being considered to publication elsewhere. I confirm that work is an accurate representation of the trial results.

 

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Received on 11.11.2019                    Modified on 10.01.2020

Accepted on 25.02.2020                   ©AJRC All right reserved

Asian J. Research Chem. 2020; 13(1):01-06.

DOI: 10.5958/0974-4150.2020.00001.2