Diabetes mellitus (DM), one of the most difficult health issues of the 21st century, is a sign of hyperglycaemia brought on by insufficient insulin production or decreased insulin sensitivity (Schmidt and Hickey, 2009). DM can result in numerous consequences, including diabetic ketoacidosis and cardiovascular disease and so on, if adequate therapy is not provided (Cambell, 2011). As is common knowledge, managing blood glucose levels is essential for DM therapy. Additionally, the postprandial digestive enzymes α-amylase and α-glucosidase play crucial roles in the breakdown of carbohydrates, which raises blood sugar levels (Joshi et al., 2015). The α-glucosidase inhibitor acarbose is useful in reducing postprandial hyperglycaemia. However, the use of acarbose inevitably causes some side effects (Deng et al., 2015). Therefore, finding natural sources of α-glucosidase and α-amylase inhibitors with no or relatively fewer adverse effects has become a research priority in treating DM (Kwon et al., 2006).
In the present study, a three-level, three-variable (solvent concentration, ultrasonic time and liquid–solid ratio) Box–Behnken design (BBD) of response surface methodology (RSM) was employed to further optimise UAE conditions for MELTF. The total flavonoids that were extracted were then refined using AB-8 macroporous resin. The extracted anti-diabetic total flavonoids’ inhibitory effects on α-glucosidase and α-amylase were also identified.
Fresh leaves of
For the experiment’s UAE protocol, we followed the one created by Mai et al. (2020) with minor modifications. The required quantity of powdered dried
With certain modifications, the technique outlined by Li et al. (2019) was used to examine the MELTFC. In brief, 200 mL of 5% NaNO2 solution and 100 mL of the supernatant were combined, and left for 6 min. A total of 200 μL of a 10% Al(NO3)3 solution was then added, and the mixture was maintained for 6 min. Subsequently, 200 μL of a 4% NaOH solution was added and then mixed to obtain the test solution. Rutin was used as a standard to evaluate the test solution’s absorbance at 510 nm. The total flavonoids content of the leaves of
where C is the concentration of the MELTFC according to the standard curve (mg · mL−1); V is the volume of the extract extraction solution (mL); N is the dilution multiple; and M is the sample weight (g).
A one-way test was used to obtain a preliminary range of extraction variables using the total flavonoid yield of
According to the results of the single-factor test, the main influencing factors for the extraction rate of MELTF were ethanol concentration (X1, %), sonication time (X2, min) and liquid-to-material ratio (X3, mL · g−1). A three-factor (Table 1), three-level BBD of RSM response surface method was used for the optimisation of the extraction process of MELTF, with MELTF extraction rate as the index. Each variable was assigned three levels, coded as +1, 0 and −1 to indicate high, medium and low values, respectively.
The coded values and corresponding actual values of the optimisation parameters.
Code | Solvent concentration (%) | Ultrasonic time (min) | Liquid-solid ratio (mL · g-1) |
---|---|---|---|
−1 | 60 | 30 | 15 |
0 | 70 | 45 | 20 |
1 | 80 | 60 | 25 |
Two grams of the required material were weighted and placed into a conical flask. The flask was then filled with 40 mL of ethanol and left to soak for 1 hr. The solution in the flask was then centrifuged at 4,390 g for 5 min to determine how many total flavonoids were present in the supernatant (MELTFC). Following response surface optimisation, the yields of the MELTF extracted by ultrasonic extraction and ethanol leaching extraction were compared.
After being soaked in 95% ethanol for 24 hr, AB-8 macroporous resin was packed onto a glass column (20 mm × 40 cm). Since the resin’s height was determined to be 18 cm, its bed volume (BV) was around 60 mL. The macroporous resin was washed with 95% ethanol until the effluent mixed with water (1:5) did not become white and turbid. After that, deionised water was used to wash the column until the smell of ethanol was completely gone.
The purification of total flavonoids was ascertained according to the method reported by Yao et al. (2013), with certain modifications. Following the packing of the column with 1 BV of the sample solution, the column was washed with 3 BV of deionised water at a flow rate of 1.5 BV · hr−1. After that, a flow rate of 1.5 BV · hr−1 of 60% ethanol was used to elute the column. The effluents were collected, and the quantity of flavonoids present, as well as the combined, concentrated and lyophilised effluents inclusive of the total flavonoid content, was ascertained based on studying the colour reaction between NaNO2-Al(NO3)3 and NaOH. The combined, concentrated and lyophilised effluents that included total flavonoids. For the next assays, the purified total flavonoids [MELTF after purification (MELPTF)] were kept in a freezer at 4 °C. The total flavonoids purity of the leaves of
where C is the concentration of the total flavonoids of the leaves of
The literature was used to evaluate the α-glucosidase inhibitory activity with a little modification (Striegel et al., 2015). A 96-well plate was incubated for 5 min at 37 °C with a combination of 40 μL of sample at various concentrations (0, 0.1, 0.2, 0.4, 0.8, 1.6, and 3.2 mg · mL−1, dissolved in 0.1 M phosphate buffer) and 40 μL of α-glucosidase solution (1 U · mL−1, dissolved in 0.1 M phosphate buffer). A total of 50 μL of PNPG (10 mM, dissolved in 0.1 M phosphate buffer) was then added, and the mixture was left at 37 °C for 30 min. A total of 90 μL of Na2CO3 solution (0.1 M) was added to end the catalytic process. The positive control was acarbose. The absorbance was measured at 405 nm with a microplate reader, and the inhibition percentage was calculated as follows:
where AS represents the absorbance of the sample reaction solution; AB is the absorbance of the reaction system without α-glucosidase; and A0 is the absorbance of the reaction system without sample.
The α-amylase inhibitory activity was determined according to a previously published method (Eleazu et al., 2016). A 96-well plate was incubated at 37 °C for 15 min with a combination of 40 μL of sample at various concentrations (0, 0.1, 0.2, 0.4, 0.8, 1.6, and 3.2 mg · mL−1, dissolved in 0.1 M phosphate buffer) and 40 μL of α-amylase (0.5 mg · mL−1, dissolved in 0.1 M phosphate buffer). Thereafter, 20 μL of 1% starch solution (dissolved in 0.1 M phosphate buffer) was added, and it was left at 37 °C for 15 min. A total of 100 μL of 3,5-dinitrophenylsalicylic acid was then added and heated for 15 min. Subsequently, the mixture was cooled to room temperature. The positive control was acarbose. The absorbance was measured at 540 nm with a microplate reader, and the inhibition percentage was calculated as follows:
where AS represents the absorbance of the sample reaction solution; AB is the absorbance of the reaction system without α-amylase; and A0 is the absorbance of the reaction system without sample.
In assessing the DPPH-scavenging activity of MELTF and MELPTF, an approach presented in the literature (Chen et al., 2019) was adopted after carrying out a slight modification. We combined all the test samples and DPPH solution (180 μL, 0.2 mM, absolute ethanol) with vitamin C (VC, 20 μL, 0–3.2 mg · mL−1, distilled water). After the reaction was allowed to take place at room temperature for 20 min in the dark, the absorbance was measured at 517 nm on a microplate reader. The formula for calculating the DPPH· scavenging rate is as follows:
where A0 is the absorbance of DPPH· mixed with distilled water; A1 is the absorbance of DPPH· mixed with the sample; and A2 is the absorbance of anhydrous ethanol mixed with the sample.
The literature-based methodology used to determine ABTS·+ scavenging ability has been somewhat changed (Rozi et al., 2019). To create an ABTS·+ stock solution, 7 mM ABTS and 2.45 mM potassium persulphate were combined in an equal volume and heated to 25 °C for 12 hr in the dark. The stock solution was diluted to have an absorbance between 0.2 and 0.8 at 734 nm. Thereafter, we combined all of the samples or the VC (100 μL, 0–3.2 mg · mL−1) with the diluted ABTS·+ solution (100 μL). The reaction was permitted to take place at 25 °C for 20 min in the dark, and upon its completion, the absorbance was measured at 734 nm. The formula for calculating the ABTS·+ scavenging rate is as follows:
where A0 is the absorbance of ABTS·+ mixed with distilled water; A1 is the absorbance of ABTS·+ mixed with the sample; and A2 is the absorbance of anhydrous ethanol mixed with the sample.
SPSS 25.0 software (SPSS Inc., Chicago, IL, USA) was used to analyse the bioactivity experiments and single-factor data. For the determination of the experimental design and regression analysis of the experimental data, Design-Expert 10.0.7 (trial version, Stat-Ease Inc., Minneapolis, MN, USA) was used.
The cavitation action of ultrasound can encourage the collision of the extracts, resulting in speedy and complete dissolution of the active components in the solvent (Senrayan and Venkatachalam, 2020). While maintaining the solvent concentration, liquid–solid radio, ultrasonic power and ultrasonic duration at 60%, 40 mg · mL−1, 240 W, and 30 min, respectively, the current study examined the effects of various ultrasonic temperature points within 40–80 °C employed on the extraction yield of MELTF. The MELTF concentration in the extract test rose as the ultrasonic temperature climbed from 40 °C to 60 °C, as shown in Figure 1A, and peaked at around 60 °C. However, increasing the temperature further led to a reduction in the amount of MELTF in the extract. The extraction yield of the MELTF was observed to undergo a gradual rise with the increase of temperature below 60 °C, as a result of the thermal movement of the molecules intensifying with temperature, which is favourable for the exudation and diffusion of flavonoids (Pompeu et al., 2009). Contrastingly, when the temperature exceeded 60 °C, the extraction yield of total flavonoids dropped, and this is likely attributable to the role played by high temperatures in degrading the flavonoid glycosides in
The effect of different ultrasonic temperature (A), ultrasonic power (B), ultrasonic time (C), solvent concentration (D) and liquid–solid ratio (E) on the extraction yield of MELTF.
It is crucial to maintain the ultrasonic-extraction appliance at its ideal working power for the extraction of total flavonoids (Ma et al., 2009). While maintaining the solvent concentration, liquid–solid radio, ultrasonic temperature and ultrasonic time at 60%, 40 mg · g−1, 60 °C and 30 min, respectively, in the present investigation, the influence of various ultrasonic power points within 200–360 W, employed on the extraction yield of MELTF, was examined. As can be seen in Figure 1B, the amount of MELTF in the extract assay rose as the ultrasonic power increased from 200 W to 240 W, peaking at about 240 W. The faster the flavonoids in
In the case of all flavonoids, a high extraction efficiency was achieved owing largely to ultrasonic time (Silva et al., 2007). It will have an impact on the ultimate MELTF output as well as the cost of energy and extraction efficiency. In this study, MELTF extraction increased as ultrasonic duration increased from 15 min to 75 min, peaking at 45 min. However, as ultrasonic time increased further, MELTF content decreased (Figure 1C). It might be because certain flavonoids’ structures change as ultrasounds get longer (Liyanapathirana and Shahidi, 2005). Based on statistical analysis, it was determined that there were significant differences for the ultrasonic time examined (
A high extraction efficiency for total flavonoids was achieved owing largely to solvent concentration (Lin et al., 2005). The impact of solvent concentration on extraction yield was examined in this work, as seen in Figure 1D. The yield of total flavonoids extracted from the
In the UAE, the liquid–solid ratio played a crucial role in achieving a high extraction efficiency for total flavonoids (Lai et al., 2014). A liquid–solid ratio range of 5–25 mL · g−1 was examined, with the ultrasonic power, solvent concentration, ultrasonic temperature and ultrasonic duration all maintained at 240 W, 70%, 60 °C and 45 min, respectively, to examine the impact of liquid–solid ratio on the extraction yield of MELTF. MELTF extraction might be improved by increasing the measured ratio of ethanol to raw material (from 5 mL · g−1 to 25 mL · g−1); however, the improvement levelled out at 20 mL · g−1 (Figure 1E). A quicker exudation of the flavonoids is observed at this juncture, which is possibly attributable to the attendant higher liquid–solid ratio, as well as to the increased surface area of the
As shown in Table 2, the extraction yield of MELTF values varied from 4.39 mg · g−1 to 8.38 mg · g−1. The results of extraction yield affected by solvent concentration, ultrasonic time and liquid–solid ratio were fitted to a second-order polynomial equation, and the values of regression coefficients were calculated. The effects of the three variables on the extraction yield of MELTF were highly significant (Table 3). The predicted model of the extraction yield value was obtained using the following second-order polynomial equation:
The coded experimental and predicted values for RSM design using ethanol as solvent.
Run | X1 | X2 | X3 | Extraction yield (mg · g−1) | |
---|---|---|---|---|---|
Experimental | Predicted | ||||
1 | −1 | −1 | 0 | 5.71 | 5.29 |
2 | 0 | 1 | 1 | 8.33 | 8.26 |
3 | 0 | 0 | 0 | 7.42 | 8.00 |
4 | 0 | 1 | −1 | 6.85 | 6.62 |
5 | 0 | −1 | −1 | 5.71 | 5.79 |
6 | 1 | −1 | 0 | 6.53 | 6.64 |
7 | 0 | 0 | 0 | 7.74 | 8.00 |
8 | 0 | 0 | 0 | 8.30 | 8.00 |
9 | 1 | 0 | −1 | 7.62 | 7.43 |
10 | −1 | 0 | −1 | 4.39 | 4.73 |
11 | 0 | 0 | 0 | 8.38 | 8.00 |
12 | 0 | −1 | 1 | 6.43 | 6.65 |
13 | −1 | 0 | 1 | 6.63 | 6.83 |
14 | −1 | 1 | 0 | 6.11 | 6.00 |
15 | 1 | 1 | 0 | 7.95 | 8.37 |
16 | 1 | 0 | 1 | 8.17 | 7.83 |
17 | 0 | 0 | 0 | 8.14 | 8.00 |
RSM, response surface methodology.
Analysis of variance (ANOVA) for the effects of solvent concentration (X1), ultrasonic time
Source | Sum of squares | Df | Mean square | F-value | Significanta | |
---|---|---|---|---|---|---|
Model | 20.16 | 9 | 2.24 | 10.82 | 0.0024 | |
X1 | 6.88 | 1 | 6.88 | 33.24 | 0.0007 | |
X2 | 2.97 | 1 | 2.97 | 14.36 | 0.0068 | ** |
X3 | 3.13 | 1 | 3.13 | 15.11 | 0.0060 | *** |
X1X2 | 0.26 | 1 | 0.26 | 1.26 | 0.2987 | ** |
X1X3 | 0.72 | 1 | 0.72 | 3.49 | 0.1038 | ** |
X2X3 | 0.15 | 1 | 0.15 | 0.71 | 0.4273 | * |
X12 | 2.53 | 1 | 2.53 | 12.23 | 0.0100 | * |
X22 | 1.77 | 1 | 1.77 | 8.53 | 0.0223 | |
X32 | 1.14 | 1 | 1.14 | 5.49 | 0.0516 | |
Residual | 1.45 | 7 | 0.21 | |||
Lack of fit | 0.79 | 3 | 0.26 | 1.58 | 0.3255 | Not significant |
Pure Error | 0.66 | |||||
Cor total | 21.61 | 4 | ||||
0.9329 | 16 | |||||
0.8467 |
ANOVA, analysis of variance; MELTF,
***significant at
According to the data obtained (Table 3), the
The graphical representations of the regression equation were the 3D response surface and the 2D contour plots. They offered a means to show the interactions between two test factors, as well as the relationship between responses and experimental levels of each variable. The circular or elliptical contour plots show whether or not there are substantial mutual interactions between the variables. The elliptical contour map shows strong interactions between the relevant variables, whereas the circular contour plot shows minor interactions between the corresponding variables. In this study, the results of extraction yield of MELTF affected by solvent concentration, liquid–solid ratio and ultrasonic time are presented in Figure 2 and Figure 3.
Response surface (3D) plots showing the effect of solvent concentration and ultrasonic time (A), solvent concentration and liquid–solid ratio (B), and ultrasonic time and liquid–solid ratio (C) on extraction yield of MELTF.
Contour plot showing the effect of solvent concentration and ultrasonic time (A), solvent concentration and liquid–solid ratio (B), and ultrasonic time and liquid–solid ratio (C) on extraction yield of MELTF.
As shown in Figure 2A, the 3D response surface plot of ethanol concentration was steeper than that of ultrasonic time, indicating that the ethanol concentration has a greater influence on the extraction yield of the MELTF than that of ultrasonic time, which is consistent with the conclusion drawn by the statistical and model-fitting analyses. As shown in Figure 3A, the contour plot was similar to an ellipse, indicating that the ethanol concentration and ultrasonic time have a certain interactive effect on the extraction yield of the MELTF.
As shown in Figure 2B, the 3D response surface plot of ethanol concentration was steeper than that of the liquid–solid ratio, which shows that the influence of ethanol concentration on the extraction yield of total flavonoids is greater than that of the liquid–solid ratio, which is the same as the conclusion drawn from the statistical and model-fitting analyses. The contour plot in Figure 3B presented an ellipse, which shows that the interaction between the liquid–solid ratio and the ethanol concentration has a greater impact on the extraction yield of the total flavonoids from the leaves of
As shown in Figure 3C, the steepness of the 3D response surface plot of the liquid–solid ratio in Figure 2C was similar to that of ultrasonic time, which indicates that the two factors have similar effects on the MELTF, which demonstrates consistency with the conclusion drawn from the statistical analysis presented in Table 3 (liquid–solid ratio,
In comparison to the conventional single parameter optimisation, response surface optimisation is more favourable since it conserves time, space and raw materials. Response surface analysis was conducted through Design-Expert, and the optimised extraction conditions were a solvent concentration of 75.72%, an ultrasonic time of 54.84 min and a liquid–solid ratio of 22.44 mL · g−1. In order to validate the adequacy of the model equations, a verification experiment was carried out under the actual optimal conditions, namely the following: a solvent concentration of 76%, an ultrasonic time of 55 min and a liquid–solid ratio of 22 mL · g−1, considering the feasibility of actual operation. As shown in Table 4, the RSM model was validated by the mean extraction yield (8.59 ± 0.34 mg · g−1), which was derived from actual trials. The MELTF had an estimated extraction yield of 8.62 mg · g−1. The validation result showed no discernible discrepancy between experimental and projected values, indicating that the response model was sufficient for capturing the anticipated optimisation and that the model presented in Eq. (7) is reliable and accurate. So, the response surface method is a reliable means for optimisation of the extraction process of
Result of model validation experiments.
No. | Optimum conditions | Extraction yield (mg · g−1) | |||
---|---|---|---|---|---|
Solvent concentration (%) | Ultrasonic time (min) | Liquid-solid radio (mL · g−1) | Experimental | Predicted | |
1 | 76 | 55 | 22 | 8.79 | 8.62 |
2 | 76 | 55 | 22 | 8.28 | 8.62 |
3 | 76 | 55 | 22 | 8.39 | 8.62 |
4 | 76 | 55 | 22 | 8.56 | 8.62 |
5 | 76 | 55 | 22 | 8.93 | 8.62 |
Average | 8.59 | ||||
Ethanol leaching extraction | |||||
6 | 0 | 20 | 20 | 3.38 | |
7 | 0 | 20 | 20 | 3.28 | |
8 | 0 | 20 | 20 | 3.42 | |
Average | 3.36 |
The goal of this experiment is to present a reasonably effective and straight-forward extraction method for the production and application of
The collected 60% ethanol eluate was developed using the colour reaction with NaNO2-Al(NO3)3-NaOH to monitor the total flavonoid content. The elution profile was obtained based on the volume of elution and the concentration of solute therein and is given in Figure 4. It can be seen from Figure 4 that the total flavonoids were completely eluted by approximately 90 mL eluent at a flow rate of 1.5 BV · hr−1. So the elution volume of 60% ethanol is determined to be 1.5 BV. As compared to the purity of the unpurified total flavonoids (MELTF), the purity of the total flavonoids of
Elution profile of MELPTF on AB-8 macroporous resin column. MELPTF, MELTF after purification.
Since α-glucosidase inhibitors may considerably lower postprandial blood glucose levels, which is a critical component in the treatment of DM, the inhibition percentage of α-glucosidase can be used to quantify the anti-diabetic impact of medications (Ademiluyi et al., 2014). Acarbose, MELTF and MELPTF were tested for their ability to inhibit glucosidase, and the findings are displayed in Figure 5. As shown in Figure 5, the total flavonoids of the leaves of
α-Glucosidase inhibitory activities of MELTF and MELPTF. MELTF,
Dietary starch and glycogen can be broken down by the α-amylase to provide glucose and maltose. As a result, delaying a rise in the blood glucose level through inhibition of α-amylase activity is crucial for the treatment of DM (Lordan et al., 2013). Acarbose, MELTF and MELPTF were tested for their ability to inhibit amylase, and the findings are displayed in Figure 6. As shown in Figure 6, the α-amylase inhibitory activities of all samples correlated positively with increasing concentrations in the range of 0.1–3.2 mg · mL−1. The IC50 values of acarbose, MELTF and MELPTF were determined to be 0.043, 0.199 and 0.094 mg · mL−1, respectively. As compared to MELTF, MELPTF had higher α-amylase inhibitory activity, with an IC50 value of 0.094 mg · mL−1, which was 2.12 times higher than that of MELTF (0.199 mg · mL−1). MELPTF strongly inhibited α-amylase, with an IC50 value of 0.094 mg · mL−1, which was close to that of acarbose (0.043 mg · mL−1). In the range of 0.1–3.2 mg · mL−1, the inhibition percentage of acarbose reached 92.45%, and the inhibition percentage of MELPTF was 71.13% at a concentration of 3.2 mg · mL−1, which was close to that of acarbose. As compared to MELTF, MELPTF had a higher α-amylase inhibitory activity, with an inhibition percentage of 71.13%, which was higher than that of MELTF (64.28%) at 3.2 mg · mL−1. Following purification, the MELTF showed better inhibition percentages, and these percentages were reasonably high, indicating that the MELTF have potential for development as α-amylase inhibitors. At the same dose, MELPTF showed exceptional amylase inhibitory action, outperforming certain flavonoids that had been previously reported (Liu et al., 2013; Wang et al., 2018).
α-Amalyse inhibitory activities of MELTF and MELPTF. MELTF,
A traditional technique used in the food business and agriculture to assess the antioxidant potential of foods is the DPPH-scavenging experiment. Figure 7 displays the findings from the analysis of the DPPH-scavenging abilities of VC, MELTF and MELPTF. When the concentration of total flavonoids was between 0.1 mg · mL−1 and 3.2 mg · mL−1, as seen in Figure 7, the total flavonoids of
DPPH-scavenging activities of MELTF and MELPTF. DPPH, 1,1-diphenyl-2-picrylhdrazyl; MELTF,
It is possible for flavonoids to scavenge ABTS·+, a specific kind of free radical. VC, MELTF and MELPTF were tested for their ability to scavenge ABTS·+, and the findings are displayed in Figure 8. All samples had ABTS·+ scavenging activities that increased in a positive correlation with concentrations between 0.1 mg · mL−1 and 3.2 mg · mL−1, as shown in Figure 8. The IC50 values of VC, MELTF and MELPTF were determined to be 0.047, 0.201 and 0.113 mg · mL−1, respectively. As compared to MELTF, MELPTF had a higher ABTS·+ scavenging activity, with an IC50 value of 0.113 mg · mL−1, which was 1.78 times higher than that of MELTF (0.201 mg · mL−1). MELPTF strongly scavenged ABTS·+, with an IC50 value of 0.094 mg · mL−1, which was close to that of VC (0.043 mg · mL−1). In the range of 0.1–3.2 mg · mL−1, the scavenging rate of VC reached 100.00%, and the scavenging rate of MELPTF was 98.95% at a concentration of 3.2 mg · mL−1, which was close to that of VC. As compared to MELTF, MELPTF had higher ABTS·+ scavenging activity, with an scavenging rate of 98.95%, which was higher than that of MELTF (87.59%) at 3.2 mg · mL−1. The total flavonoids from
ABTS·+ scavenging activities of MELTF and MELPTF. ABTS, 2,2′-Azino-bis (3-ethylbenzthiazoline-6-sulphonic acid); MELTF,
The leaves of