key: cord-0920147-hesergkg
authors: Sharif Nasirian, Valeh; Shahidi, Seyed‐Ahmad; Tahermansouri, Hasan; Chekin, Fereshteh
title: Application of graphene oxide in the adsorption and extraction of bioactive compounds from lemon peel
date: 2021-06-02
journal: Food Sci Nutr
DOI: 10.1002/fsn3.2363
sha: 8abdb57c3beec57c8005dc07f029a8dd121e3b61
doc_id: 920147
cord_uid: hesergkg

The bioactive compounds like rutin, naringin, and gallic acid have been separated from lemon peel by graphene oxide (GO). The different influences such as pH values and separation conditions were investigated. Moreover, the samples were characterized by Fourier transform infrared spectroscopy, thermogravimetric analysis, scanning electron microscopy, UV‐Vis spectroscopy, and high‐performance liquid chromatography. The findings of high‐performance liquid chromatography revealed that the adsorbed proportion of rutin by GO was more than naringin and gallic acid so that 66.7% of rutin, 34% of naringin, and 19% of gallic acid from the extract were remarkably adsorbed and separated. Besides, adsorption percentage of these materials by GO was considered 74.8% after five cycles of adsorption–desorption process. On the other hand, we carried out batch experiments in order to study the adsorption mechanism of rutin on the GO since rutin was the highest quantity of bioactive substance in lemon peel. Pseudo‐second‐order kinetic model and Langmuir isotherm were the best models for describing adsorption process of rutin by GO. Adsorption capacity of rutin by GO was obtained about 21.08 mgg(−1). In addition, the physical adsorption of rutin by GO was confirmed by Dubinin–Radushkevich isotherm. This research confirmed that this method for separation of flavonoids is simple and less cost.

| 3853 SHARIF NASIRIAN et Al. were generally applied as antioxidant (El-desoky et al., 2018; Mallepu et al., 2018) . Moreover, a huge number of reports have been presented about the medical activities of naringin and rutin (El-desoky et al., 2018; Gullón et al., 2017) . As a result, the flavonoids have fascinated much attention of the scientists because they showed hepatoprotective activities and the therapeutic properties such as antioxidant, anti-inflammatory, anticarcinogenic, and antiaging (Chen et al., 2020; Jabeen et al., 2019; Maleki et al., 2019; Vukovic et al., 2018) . However, the peel of citrus fruits contains the abundant proportion of flavonoid as compared to other parts of the fruit. Unfortunately, it is thrown out as waste.

Meanwhile, gallic acid (3,4,5-trihydroxybenzoic acid) is a kind of polyphenol that there is in plants, foods, and beverages.

Furthermore, not only is it utilized for the biomedical fields, but also its antioxidant activities and the influence of corrosion protection on the steel surfaces have been studied (Ferraris et al., 2020) .

Therefore, the extraction of these bioactive compounds from peels is essential.

So far, the different approaches such as ultrasonic (Yu et al., 2019) , eutectic solvents (Ming-Zhua et al., 2020) , colorimetric (Huang et al., 2018) , supercritical fluids (Song et al., 2019) , and adsorption have been reported for their extraction.

Among these methods, adsorption is a simple and cost-effective technique in comparison with other procedures since they have the intricate operation and high costs of process (Liu et al., 2021; Yao et al., 2021) .

Graphene is a layered carbon nanostructure which sp 2 -bonded carbon atoms are hexagonally arranged in it. The excellent physical and chemical properties of graphene caused that a lot of reports were presented about its different applications. Additionally, graphene oxide (GO) is other shape of graphene which has attracted lots of attentions from researchers since it can be used as a precursor for the significant production of graphene-based materials . Meanwhile, GO has been introduced as an ideal adsorbent in the adsorption process of heavy metals and organic compounds from aquatic solutions since there are many functional groups such as, epoxy, hydroxyl, and carboxyl groups on it. In other words, the sorption sites on the GO are vast that can result in increasing adsorption capacity. Then, a large number of studies dedicated to this topic Mohseni et al., 2017) .

According to the main importance of adsorption process for phenolic compounds, we decided to present an easy and operative technique for the separation of bioactive compounds from lemon peel by GO. In fact, this project includes two steps. The first step involves adsorption and extraction of rutin, naringin, and gallic acid from lemon peel by GO. The second step includes the study of adsorption process of rutin by GO since it was the uppermost rate of flavonoid in lemon peel. Thus, the purpose of the present work was to compare sorption capacity of GO for the adsorption of bioactive materials in particular rutin from real sample (extract of the lemon peel) and the simulated rutin. Besides, the extracted flavonoids as antioxidant can be applied in future uses.

Citrus limetta was collected from local gardens. Rutin with HPLC grade, methanol, nitric acid, and acetic acid was purchased from Sigma-Aldrich Inc., and graphene oxide nanoplatelets (99%, Thickness 3.4-7 nm with 6-10 Layers) were used as received. Fourier transform infrared spectroscopy (FTIR) was recorded using KBr tablets on a Thermo Nicolet Nexus 870 FTIR spectrometer. Scanning electron microscope (SEM) was taken using an MIRA3\TESCAN-XMU model. The samples were studied by thermogravimetric analysis (TGA) (Netzsch TG 209 F1 Iris1) under nitrogen gas atmosphere (10℃/min). The concentration of flavonoids was measured by variable-wavelength UV-Vis spectrophotometry of Unico UV 2100 Model. High-performance liquid chromatography (HPLC) was performed with an Agilent Technologies 1200 liquid chromatograph which equipped to a quaternary solvent-delivery system (an auto sampler and a UV detector).

An Agilent Zorbax SB-C18 column (100 × 4.6 mm, 5 μm particle size) was used for all analyses. An ultrasonic bath with temperature control (Elmasonic, S60H) was used to disperse the GO in solution.

Lemons with an average weight of 100.0 ± 2.0 g were used. They were washed with the distilled water and then were manually peeled. The obtained peels were dried in an oven at 40℃ for 48 hr.

Thus, the dried peels were milled using a blender (Molinex) to produce the lemon peel powder (LPP). LPP was packed and kept in refrigerator at 4℃ for use.

5 g of LPP was blended with 30 ml of the ethanol-water mixture (70:30, v/v) as solvent. Then, the mixture was placed in the ultrasonic bath for 30 min at room temperature (25℃). The suspension was filtered with filter paper to remove the large particles, and the remaining powder was extracted for other two times using 25 ml of the ethanol-water mixture (70:30, v/v). After filtration, the filtrate was diluted to 100 ml in a volumetric flask (100 ml) by the ethanolwater mixture (70:30, v/v) and the color of the lemon peel extract was light yellow and the extract was stored at 4℃ for test.

Chromatographic analyses were performed under gradient conditions. The components of mobile phase were methanol (A) and 0.1% acetic acid (B). Separation was performed using a gradient program: 0-8 min: 0 min, 15% A and 85% B; 4 min, 30% A and 70% B; 8 min, 45% A, 55% B; 12 min, 65% A, 35% B; 16 min, 45% A, 55% B; 20 min, 30% A, 70% B; 24 min, 15% A and 85% B. In addition, the time of reequilibration between runs was 10 min. The analysis was achieved at 30℃ (column oven temperature), with a 0.6 ml/min flow rate, and the injection volume was 5 μl. Chromatography peaks were characterized by comparing their retention time with that of the standard samples. Furthermore, diode-array detection (DAD) in HPLC was used to make a spectral scan of the peaks (254-360 nm). All chromatography operations were carried out at ambient temperature and in triplicate. The linearity of the method was established using five standard solution levels for rutin (concentration range of 10-50 mg/L) evaluated in triplicate on three separate experiments.

Standard calibration curve of rutin was calculated with linear equation of Y = 1.7343X + 0.4292 and correlation coefficient (

where X is the content of the rutin and Y is the peak height.

To study the effects of pH on the sorption of flavonoids, 50 mg of GO was dispersed into 15 ml of extract. The initial pH values were adjusted from 1.0 to 9.0 using nitric acid and NaOH at 25 ± 1°C.

Then, the mixture was stirred for 5 min. As a result, their adsorption percentage was determined by UV-Vis spectroscopy. According to Equation (1), adsorption percentage can be calculated as follows:

where A 0 and A e are the initial and final absorptions of these compounds in the solution, respectively. The results are based on at least three replicate experiments for each pH value.

The adsorption was carried out in 15 ml of extract with 50 mg of GO at 298 K, and then, the mixture was stirred for 5 min (the dosage and contact time values were optimized). After filtration, the GO-flavonoids were immersed in 15 ml of ethanol-water (70:30, v/v) solution at pH = 9. Then, GO was separated from the solution and washed with water. Finally, the released flavonoid values in the solution were determined by HPLC. Figure 1 shows the procedure for the separation process of bioactive compounds, in particular flavonoids, by GO.

To study the effects of pH on the sorption of rutin, 50 mg of GO was dispersed into 15 ml solutions containing 100 mg/L of rutin with the various pH values (3-9) which these values were obtained by nitric acid and NaOH at 25 ± 1℃. The proportion of the absorbed rutin was calculated as the difference between the initial and final concentrations when the equilibrium was reached. The tests were done three times for each pH value. To evaluate the sorption capacity, 50 mg of GO was mixed with 15 ml of rutin solution (concentration range 10-100 mg/L). After 150 min, the rutin concentration in the aqueous solutions was determined by UV-Vis spectroscopy. The removal (%) and sorption capacity q e (mg/g) were acquired as follows in Equations (2) and (3) (1)

The procedure of the adsorption process of the different compounds from the extract of lemon peel by graphene oxide (GO) and the trend of getting UV-Vis, High-performance liquid chromatography (HPLC), and thermogravimetric analysis (TGA) analyses and HPLC which we explained in the report. FTIR spectrum of GO is shown in Figure S1 . As can be observed, the peaks at 3,427, 1,732, 1,620, and 1,000-13,00 cm −1 can be related to OH, C = O, C = C, and C-O stretching modes, respectively, that certainly indicated carboxylic and hydroxyl groups on the graphene. 

The adsorption-desorption processes are vital factors for an adsorbent since they can decline the entire price for efficiency of the adsorbents. On the basis of our previous article (Gholizadeh et al., 2020) , the best results of desorption were obtained when pH reached 9. Therefore, we carried out the desorption experiments at pH = 9. Figure 4 shows the results of the adsorptiondesorption cycles of GO. As can be seen in Figure 4 , GO can be reused for 4 cycle since the adsorption capacity of bioactive compounds decreased about 18 ± 2.9% up to cycle 4. In addition, it

can be perceived that GO with the remarkable steadiness till the third cycle can be utilized as an outstanding recyclable adsorbent for these substances.

The structures of bioactive compounds (naringin, rutin, and gallic acid) of extract along with the offered mechanism for the adsorption of them by GO are displayed in Figure 5 . As can be seen, there are a lot of polar functional groups such as hydroxyl and carbonyl in rutin, naringin, gallic acid, and GO. Hence, they tend to form hydrogen bonds together. In fact, one of the main mechanisms for the adsorption of bioactive compounds from extract is hydrogen bond. On the basis, adsorption process of bioactive compounds of extract by GO can be related to the hydrogen bond interactions between the oxygen of a bioactive compound and the hydrogen of an alcohol or carboxylic group of GO and vice versa. Additionally, the π-π interactions between the double bonds of graphene and aromatic ring of the bioactive compounds can be other factor for the adsorption process. These interactions are shown in Figure 5 . Then, these proposed mechanisms can culminate in the adsorption of rutin, naringin, and gallic acid by GO.

Graphene oxide performance for the separation of flavonoids was considered based on the rutin and naringin. The obtained HPLC data were shown in Figure 6 . As Figure 6a presented, the highest

The adsorption-desorption cycles of the different compounds by graphene oxide (GO) from extract flavonoid proportion of extract was rutin and that all of the bioactive compounds were well separated. Figure 6b ,c illustrates the HPLC results of the extract after the filtration of GO-flavonoids from solution and the standard samples, respectively. In relation to Figure 6c , the elution order was gallic acid, naringin, and rutin with the retention times at 2.8, 13.24, and 13.74 min, respectively.

As can be witnessed in Figure 6b, Although the naringin, rutin, and gallic acid were characterized, an unknown compound with the retention time at 19 min was meaningfully adsorbed by GO about 46.6% which it may be a flavonoid.

Totally, GO can significantly cause the extraction of the different flavonoids, which this is a great result.

Since the most significant rate of flavonoid in lemon peel was rutin, we decided to investigate the adsorption process for the simulated samples of it. In other words, our purpose is the study of the sorption mechanism of rutin on the GO and the comparison with the extract sample.

We studied pH effect on the adsorption of rutin by GO as was exhibited in Figure 7a . As can be understood in Figure 7a , we witnessed Furthermore, the existence of more soluble rutin at pH = 9 causes the strong interaction between adsorbate and water which it prevents adsorbing rutin by GO.

The influence of contact time on the adsorption of the rutin by GO was indicated in Figure 7b . At up to 20 min of initial contact time, the rutin adsorption rate was relatively rapid and then reached equilibrium at nearly 90 min. The final value of the adsorption capacity was found to be 20.62 mg/g at equilibrium time. As can be seen in Table 1 shows kinetic models for the adsorption process of rutin by GO (Zhao et al., 2020) . According to Table 1 , the pseudosecond-order model will be able to describe the adsorption process of rutin on the GO since this model showed the higher correlation coefficient (0.9994) than pseudo-first-order model (0.9694). Moreover, the adsorbed values of rutin at equilibrium (q e ) by GO were found 21.79 mg/g which significantly approved with the corresponded experimental data (q e,ex = 21.081). In addition, the plots of adsorption kinetic models were presented in Supplementary Data. 

We use adsorption isotherms, which are mathematical equations, whenever the relationship of the adsorbate concentrations in the solid and liquid media is important for us since they describe how the adsorbate species adsorbed to the adsorbent surface (Foo et al., 2010) . As a matter of fact, adsorption isotherms show that F I G U R E 6 Chromatograms were as follows: (a) the crude extract; (b) the extract after separation of GO-flavonoids from it; and (c) the standard references of samples when an equilibrium state is established in system, how a substance from the aqueous media transfers to a solid phase. Three adsorption isotherm models, Langmuir, Freundlich, and Dubinin-Radushkevich, have been utilized to describe the mechanism of adsorption.

Langmuir isotherm assumes monolayer adsorption of the molecules on the adsorbent surface with the same activation energy of adsorption. However, it is used for the homogeneous surface (Massoud et al., 2020) . Besides, multilayer adsorption and the heterogeneous surfaces with nonuniform distribution of adsorption heat are the features of Freundlich isotherms .

These models along with their calculated parameters, which describe the surface properties and affinity of the adsorbent, are indicated in Table 2 . All plots of adsorption isotherms are presented in Supplementary Data.

As Table 2 shows, Langmuir isotherm with high correlation coefficient (0.9934) better than Freundlich model (0.9659) described the adsorption process of rutin by GO. In other words, rutin adsorption was the monolayer and equal activation energy was considered for sorption of rutin molecules on the GO.

On the other hand, Dubinin-Radushkevich (D-R) isotherm describes a Gaussian energy distribution onto a heterogeneous surface which it is utilized to explain the adsorption mechanism (Brohi et al., 2020) . It can be expressed as follows in

Equations (4) and (5):

where q e (mg/g) is the volume of rutin adsorbed, q m (mg/g) is the maximum adsorption capacity of rutin, K DR (mol 2 /kJ 2 ) is the D-R isotherm constant, ε is Polanyi potential, R is the gas constant (0.008314 kJ/mol K), and T (K) is absolute temperature in Kelvin. Meanwhile, the constant K D presents the mean free energy, E (kJ/mol), of sorption per molecule of sorbate when it is transferred to the surface of the solid from infinity in the solution which can be estimated using the following Equation (6):

In fact, the E value describes whether the adsorption on the GO has happened as a physical or chemical process which it is important.

On the basis of some papers (Foo et al., 2010; Kausar et al., 2013) , the adsorption process can be considered as the physical adsorption if the calculated value of E is below 8 kJ/mol but the chemical adsorption occurs in the range of 8-16 kJ/mol. As can be seen in Table 2 , the calculated proportion of E was 3.9 kJ/mol. Then, it can be decided that physical adsorption may play a substantial role in the adsorption process of rutin by GO. 

The acquired findings showed that GO efficiency for rutin sorption from the simulated solution (standard solution: 100 ppm) and the lemon peel extract (32.97 ppm) was about 72 ± 1.6% and 67 ± 2.5%, respectively, since these experiments carried out in the same conditions (solution volume: 15 ml, dosage: 50 mg). With regard to the presence of the various compounds in lemon peel such as naringin, rutin, gallic acid, and even other materials, which did not determine, GO efficiency for rutin sorption can be suitable and worthwhile in the range of the considered concentrations since in addition to rutin, naringin, and gallic acid were also adsorbed and separated by GO.

In this project, we described a method for separation of flavonoids of lemon peel by GO. The desorption percentage of flavonoids was 74.8% after five cycle. Furthermore, the rutin quantity which was adsorbed from extract by GO was almost similar to that of the simulated rutin in terms of the adsorption percentage. These results may be able to be valuable in future applications. Moreover, we analyzed the process of rutin adsorption by GO. Langmuir isotherm meaningfully interpreted the adsorption process of rutin. The pseudo-secondorder kinetic showed the admissible description from the process.

The financial and encouragement support provided by Research Vice Presidency of Ayatollah Amoli branch, Islamic Azad University.

All authors declare that there is no conflict of interest.

Valeh Sharif Nasirian : Investigation (lead). Seyed-Ahmad Shahidi:

Supervision (equal). Hasan Tahermansouri: Project administration (equal); Supervision (lead). Fereshteh Chekin: Validation (equal).

This article does not contain any studies with human participants or animals performed by any of the authors.

Data available on request due to privacy/ethical restrictions.

Seyed-Ahmad Shahidi https://orcid.org/0000-0001-5667-2875

Hasan Tahermansouri https://orcid.org/0000-0003-4295-5238 TA B L E 1 The calculated parameters of pseudo-first-order and pseudo-second-order models of rutin sorption onto graphene oxide (GO)

The calculated parameters Plot q e,ex

Pseudo-first-order 21.08 log (q e − q t ) = log q e − k 1 2.303 t q e (mg/g) k 1 (min −1 ) R 2 log (q e -q t ) versus t 10.59 0.0375 0.9694

Pseudo-second-order t q t = 1 (k 2 q 2 e ) + 1 q e t q e (mg/g) k 2 (g/mg min −1 ) R 2 t/q t versus t.

21.79 0.0086 0.9994

Note: Temperature, 298 K; initial rutin concentration, 100 mg/L; mass of GO, 50 mg; volume of solution, 15 ml; and pH of the sample solution, 1.0.

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