Degradation of textile dyes from aqueous solution using tea-polyphenol/Fe loaded waste silk fabrics as Fenton-like catalysts.

In this study, waste silk fabrics (SF) were modified with tea-polyphenols (TPs) and then iron (Fe2+). The modified silk fabrics (TP-SF/Fe) were characterized via Fourier-transform infrared (FTIR), energy dispersive spectroscopy (EDS), scanning electron microscopy (SEM), and X-ray photoelectron spectroscopy (XPS) analysis. TP-SF/Fe was used in the Fenton-like removal of dyes (methylene blue, reactive orange GRN, and cationic violet X-5BLN) from aqueous solutions with catalyst-like activity. The effects of different catalyst samples, contact time, H2O2 concentration, initial dye concentration, and pH values on dye removal were investigated. The results showed that the dye removal percentages with the TP-SF/Fe-H2O2 sample reached 98%, 97%, and 95% in 5-40 min for methylene blue, reactive orange GRN, and cationic violet X-5BLN, respectively. Different thermodynamic and kinetic models were used to check the best fit of the adsorption data. The results indicated that the Freundlich isotherm and pseudo first-order kinetics models were the best fits. Moreover, it was also proved that TP-SF/Fe would be quite an effective and economical adsorbent for the treatment of textile dye wastewater. This work provides the basis for waste silk application in the removal of dyes from wastewater. This journal is © The Royal Society of Chemistry.

Introduction

Dyeing wastewater from the textile industries produces highly polluted effluents and is a serious concern for the environment and human beings.[1-3] Approximately ten thousand different dyes are currently used in the textile industries and the amount of wastewater is huge.[4,5] Compared with natural dyes, the dyeing wastewater from synthetic dyes rapidly increases pollution levels because of their low synthesis cost,[6] high toxicity,[7] good chemical stability,[8,9] strong bioaccumulation and color diversity. They have strong resistance to conventional treatment methods[10-12] and sunlight and they cause serious damage to aquatic life when discharged into water.[13,14] Dye wastewater causes many human diseases such as lung cancer, skin irritation, allergy, heart disease, chromosomal aberrations, kidney and liver damage, and respiratory diseases.[15-18] Therefore, it is necessary to remove these dyes from wastewater before it is discharged into the water system.

In recent years, researchers have developed various methods and techniques to remove toxic pollutants from the wastewater of textile industries.[19-22] Among those efforts, various techniques have been considered to remove dyes from wastewater such as coagulation, adsorption, membrane filtration, biological processes, microextraction, photocatalysis, Fenton-like removal and electrochemical methods.[23-26] Among these technologies, Fenton-like removal technology has attracted wide attention due to its high degradation capability, low cost and environmental friendliness although the reaction mostly requires H2O2 and Fenton or Fenton-like reagents. In addition, during the treatment process, the Fenton or Fenton-like reaction directly breaks down dye molecules without post-processing.[27,28]

Currently, the Fenton process is attracting more interest for the degradation of dyes.[29,30] In this process, hydroxyl radicals (˙OH) are produced, which are highly reactive and powerful oxidants capable of degrading organic and inorganic compounds into water.[31,32] However, the homogeneous Fenton process also has some drawbacks from the perspective of practical application and this system has some limitations such as acidic pH conditions, a huge amount of final sludge, time-consuming processes and high cost.[33,34] Immobilization of iron particles (Fe) may be a suitable and stable remediation technique to overcome these limitations. The immobilization of iron has garnered a great deal of interest in the prevention of secondary water pollution due to its potential for having lower costs, higher reactivity and wider uses compared to other treatments.[35,36] However, this research was inspired by our previous study on immobilizing the iron (Fe) particles of a Fenton-like removal process on activated silk fiber for heterogeneous catalytic applications.[37]

Silk is a standard natural fibrous protein fiber widely used in textiles and biomedical applications due to its slow degradation, excellent biocompatibility and mechanical properties.[38-40] Moreover, silk is more extensively used in the textile industries to meet consumer demands and at the same time, lots of fabric is wasted in the processes.[41,42] Waste silk fabric samples that cannot be used for any other purpose are a worldwide concern. An alternative use of waste silk fabric provided through this work could be a sustainable remedy.

Polyphenol is a very effective component and can be used for different purposes. The structure of polyphenol compounds is considered to have an effective influence on improving the surface reactivity of hydrophobic and hydrophilic surfaces as well as other functional groups.[43-45] Tea is a compound widely used in the world and tea leaves are rich in natural polyphenolic compounds. Tea polyphenols (TPs) are used in beverage and food industries, as well as being investigated in health, biological and medicine services.[46,47] Tea polyphenols are also used in textile industries for coloration.[48,49] However, TPs are extensively used in dye adsorption, heavy metal adsorption, antibacterial, antimicrobial, UV protective and super-hydrophobic fields due to their strong functional properties.[50-52] The properties of TPs are similar to dopamine, but their cost is relatively low. Thus, TPs can be used as effective components in the coloration and functional modification of textiles.

In this present work, waste silk fabric was coated using TPs by rapid oxidative polymerization and iron particles (Fe2+) were effectively immobilized onto the fabric surface, which was used for the Fenton-like degradation of methylene blue, reactive orange GRN and cationic violet X-5BLN dyes from aqueous solution, as shown in Fig. 1. The TPs grafted iron-loaded silk fabric (TP-SF/Fe) was characterized by using several instrumental techniques such as SEM and XPS. Moreover, the degradation process was investigated by various parameters, including different catalyst samples, contact time, H2O2 concentration, initial dye concentration and pH values. The isotherm and kinetics models of dye degradation were also analyzed.

Fig. 1

A schematic diagram of TP-SF/Fe preparation and its adsorption of dyes.

Materials and methods

Materials

In this study, waste silk fabric (48 g m−2) was provided by Huzhou Jiangnan Hengsheng Refining and Dyeing Co., Ltd. (China). Tea polyphenols (TPs) (purity 98.5%) were purchased from Shanghai Yuanye Biotechnology Co. Analytical grade sodium perborate (NaBO3·4H2O), ferric chloride hexahydrate (FeCl3·6H2O), hydrogen peroxide (H2O2, 33%), and ferrous sulfate heptahydrate (FeSO4·7H2O) were obtained from Shanghai Lingfeng Chemical Reagent Co., Ltd. (Shanghai, China). Methylene blue (MB), reactive orange GRN (GRN) and cationic violet X-5BLN (BLN) dyes were purchased from Tianjin Tianshun Chemical Dyestuff Co., Ltd (Tianjin, China).

Preparation of the functional silk fabrics

In this work, silk fabric (15 × 15 cm2) was immersed in 150 mL of deionized water containing 2 g L−1 tea polyphenol and 2 mmol L−1 ferric chlorides (FeCl3·6H2O) and placed in a shaking water bath for 20 min at 50 °C. Then 12 mmol L−1 of sodium perborate (NaBO3·4H2O) was added and the final solution was stirred for 40 min. The resultant coated silk fabric (TP-SF) was removed and rinsed using deionized water then dried in air. Afterward, the coated dried silk fabric was directly put into 1400 mL deionized water containing 40 mmol L−1 FeSO4·7H2O for 24 h at room temperature. Finally, the TP-SF/Fe sample was taken out and rinsed with deionized water and dried overnight in ambient condition. The chemical structure of the three dyes (cationic blue, anionic orange and cationic based violet dyes) are shown in Fig. 2.

Fig. 2

The chemical structure of (i) methylene blue, (ii) reactive orange GRN, and (iii) cationic violet X-5BLN dyes.

Characterization of TP-SF/Fe

Fourier transform infrared (FTIR) spectroscopy of TP-SF/Fe was performed using a Nicolet-5700 Fourier transform infrared spectrometer in the range of 400–4000 cm−1. The surface morphology of silk fabric was analyzed by scanning electron microscopy (SEM, Hitachi S-4800). The elemental detection of the silk fabric and its percentage atomic weight was carried out by energy dispersive X-ray spectroscopy (EDS) using BRUKNER axes EDS analyzer mounted with SEM. The surface elements of TP-SF/Fe were verified by X-ray photoelectron spectra (XPS) through a Thermo ESCALAB 250XI spectrometer (Thermo Fisher Scientific, USA) using an Al Kα X-ray source (1484.6 eV). The degradation of TP-SF/Fe was measured using a double beam UV-Vis spectrophotometer (Hitachi UH-4150) in the wavelength range 300–800 nm at room temperature.

Dye degradation procedure and analysis

The TP-SF/Fe was evaluated by the heterogeneous Fenton-like removal of (methylene blue, reactive orange GRN and cationic violet X-5BLN) dyes in the presence of hydrogen peroxide (H2O2). In the rotatory shaker, 0.1 g TP-SF/Fe (adsorbent) was added into 70 mL aqueous solution with 20 mg L−1 of dyes for 40 min at 50 °C with stirring. In this experiment, the concentrations of dyes in the solutions were measured every 5 min until degradation was complete and the remaining amount of dyes in the aqueous solution was determined by UV-spectrophotometer. The dye removal percentage (R) and removal capacity (qe) was calculated using the following equations:where C0 is the initial concentration of dye and Ce is the concentration of dyes at different time intervals, qe (mg g−1) is the amount of dye removal capacity, V (L) is the volume of the solution and m (g) is the mass of adsorbent. The maximum absorption wavelength of the dye in the visible region was calculated by C/C0 at λmax: (664, 591 and 475 nm for methylene blue, reactive orange GRN and cationic violet X-5BLN). Dye removal is influenced by different factors such as the effect of contact time (5 to 40 min), H2O2 concentration (0.01 to 5 mmol L−1), dye concentration (10 to 80 mg L−1) and pH (3 to 11). The pH was adjusted by using 0.1 mol L−1 HNO3 and 0.1 mol L−1 NaOH solutions.

Degradation mechanism

Based on the results described in the section above, the proposed mechanism of MB, GRN and BLN dye degradation by TP-SF/Fe is presented in Fig. 3. Ferrous ions can be mineralized into FeOOH by TP-SF like PDA-SF.[53] The TP-SF/Fe-H2O2 catalyst can efficiently degrade dyes due to the presence of hydroxyl ions on the surface of TPs. The TP-SF/Fe-H2O2 was considered for the Fenton-like reaction in the presence of H2O2 which can catalyze the production of hydroxyl ˙OH radicals from H2O2.[54,55] The hydroxyl ˙OH radicals can break the existing azo bond in dye molecules, thus destroying the structure of dyes.

Fig. 3

A schematic diagram of the postulated mechanism of the degradation of the dyes.

The postulated reaction mechanism is shown in the three following steps:

(i) The process of producing the reactive speciesFeFeOOH + H

(ii) The process of color removal of the dyesDyes + ˙OH → reaction intermediates

(iii) The process of mineralizationReaction intermediates + ˙OH → CO

Results and discussion

Characterization

FTIR analysis

To determine the presence of active molecules in the stabilization of Fe2+ ions in SF, Fourier transform infrared spectroscopy (FTIR) of SF and TP-SF/Fe was conducted. It can be observed from Fig. 4 that the absorption peaks appearing at 3278, 2961 and 2933 cm−1 were attributed to the –OH and C–H stretching vibration belonging to polyphenols present in waste silk, respectively.[56,57] The band at 1617 cm−1 was attributed to the stretching vibration of –CO indicating bending of the untreated and treated waste silk fabric. The band peaks appearing at 1511, 1439, 1225 and 1062 cm−1 represented the bending vibrations of N–H, C–N, O–H and C–O–C, respectively.[52] Moreover, the FT-IR spectra of TP-SF/Fe with band peaks at 1261, 1156, 1093, 1018 and 798 cm−1 indicated the formation of Fe–O due to the presence of TPs which confirms the loading of the iron particles.

Fig. 4

Infrared spectra of untreated and treated silk.

EDS analysis

The elemental composition on the fiber surface before and after treatment was evaluated using EDS analysis (see Fig. 5 and 6). The major elements of C, N, and O were observed in the EDS spectra. It is obvious from the EDS spectra and maps that there are different surface element compositions on the treated and untreated samples. After loading of iron, the EDS spectrum showed the peak intensity of the Fe element confirming the formation of TP-SF/Fe. Fig. 6(b) shows the iron element of TP-SF/Fe, which is derived from the presence of some Fe-oxides in tea-phenols.

Fig. 5

Energy dispersive spectra of (a) SF and (b) TP-SF/Fe.

Fig. 6

Energy dispersive spectra of (a) SF and (b) TP-SF/Fe with different element mapping images.

SEM analysis

The surface morphology of the waste silk before and after modification was investigated through SEM analysis as shown in Fig. 7. It is clear from the SEM pictures that the surface of the SF is very smooth as shown in Fig. 7(a) and (b). Conversely, the SEM image of the surface of TP-SF/Fe was more rough (Fig. 7(c) and (d)), indicating that the modified silk fabric is successfully covered by the tea-phenols/Fe coating.[58,59] However, it can be considered that the presence of functional groups on the surface of tea-phenols/Fe silk fabric could be chosen as a research model for further studies.

Fig. 7

SEM images of SF (a, b) and TP-SF/Fe (c, d) at different magnifications

XPS analysis

X-ray photoelectron spectroscopy (XPS) was performed to compare and verify the oxidation states of elements present on the surface of the fabric before and after treatment as shown in Fig. 8(a)–(d) and Table 1. It can be seen from Fig. 8(a) that C, N, and O element peaks appear in the XPS spectrum of SF and TP-SF/Fe samples, but a peak corresponding to the iron (Fe) element appears on the surface spectrum of TP-SF-Fe. In addition, Fig. 8(b) and (c) display the C 1s spectra of the surface of the SF and TP-SF/Fe samples, and the C 1s XPS spectra are fitted to the absorption peaks at 284.7, 285.7, 286.5 and 288.1 eV, corresponding to the C–C, C–N, C–OH, and O–C O bonds, respectively.[60-62] Furthermore, Fig. 8(d) shows the core-level Fe 2p on the surface of the TP-SF-Fe, and the characteristic peaks are attributed to Fe 2p3/2 (711.1 eV) and Fe 2p1/2 (724.5 eV), respectively. Therefore, the XPS results indicated that iron mineralization on the tea-phenol coated silk fibers existed in the oxidation state.

Fig. 8

(a) Wide-scan XPS spectra of the silk fabrics, high-resolution C 1s spectra of (b) SF and (c) TP-SF/Fe, and (d) the core-level Fe 2p spectrum of TP-SF/Fe.

Surface elemental compositions (atomic weight percentage) of silk fabric samples

Surface element	Sample (%)
	SF	TP-SF/Fe
N	10.94	6.41
O	17.84	29.95
C	70.75	61.02
Fe	0.46	2.62

Factors influencing the removal of dyes from aqueous solution

The effect of different catalyst systems

The effect of different samples for adsorption of methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes was evaluated for the Fe, Fe-H2O2, TP-SF, TP-SF-H2O2, TP-SF/Fe, and TP-SF/Fe-H2O2 samples, in which the same amount of Fe2+ or TP was applied. Fig. 9 shows that TP-SF/Fe-H2O2 is the most effective at degrading dyes and the highest efficiency is about 98% for methylene blue, 99% for reactive orange GRN, and 96% for cationic violet X-5BLN dyes. The TP-SF and TP-SF-H2O2 dye removal rate is lower and could not meet the requirements. In addition, the dye removal efficiency for Fe and Fe-H2O2 is much lower and does not show sufficient change. High efficiency removal of dyes can be obtained with a high dosage of H2O2 in the traditional Fenton reaction. It can be seen from Fig. 9 that TP-SF/Fe resulted in a lower degradation rate; on the other hand, TP-SF/Fe with a small amount of H2O2 (0.1 mmol L−1) generated a strong reaction system, which effectively increased the release rate of hydroxyl radicals and degraded most of the dyes in a short time. This signifies that the TP-SF/Fe-H2O2 samples are stable and can be used for dye degradation experiments.

Fig. 9

Evolution over time of C/C0 for different catalyst samples in three dye solutions: (a) methylene blue, (b) reactive orange GRN, and (c) cationic violet X-5BLN (sample: 0.1 g, H2O2 concentration: 0.1 mmol L−1, dye concentration: 20 mg L−1, time: 40 min, and T: 50 °C).

Effects of contact time for the degradation of dyes

The function of contact time on dye removal is a vital factor for cost minimization in industrial usage. In this work, Fenton-like degradation of aromatic dyes (methylene blue, reactive orange GRN and cationic violet X-5BLN) was carried out with different contact times and analyzed by UV-Vis spectrophotometry. The Fenton-like reaction was constructed with iron loaded silk and hydrogen peroxide (H2O2) for degrading organic pollutants. As shown in Fig. 10(a)–(c), the contact time for the dye removal process was kept at 40 min to optimize the adsorption uptake with 0.1 g of sample, initial dye concentration of 20 mg L−1 and at 50 °C. It can be seen from Fig. 10(a) that the MB dye exhibits the maximum absorption peak intensity at 664 nm observed with the function of the reaction time and after 40 minutes the most degradation is achieved.[63] Furthermore, Fig. 10(b) and (c) shows that the reactive orange GRN and cationic violet X-5BLN dyes exhibit the maximum absorption peak intensity at 591 nm and 475 nm after 40 min of stirring, respectively.[64-66] It can be concluded that Fenton-like removal experiments using TP-SF/Fe can reach sufficient degradation effects within 40 min.

Fig. 10

UV-visible spectral changes for the degradation of dyes: (a) methylene blue, (b) reactive orange GRN, and (c) cationic violet X-5BLN dye degradation as a function of time (TP-SF/Fe = 0.1 g, dye concentration = 20 mg L−1, H2O2 concentration = 1.0 mmol L−1, and T = 50 °C).

Effects of H2O2 concentration

The degradation of (methylene blue, reactive orange GRN and cationic violet X-5BLN) dyes were carried out using different concentrations of H2O2 (0.05, 0.1, 0.5, 1, 3, and 5 mmol L−1) and the results are illustrated in Fig. 11(a)–(c). The dye removal capacity was evaluated by the terms of C/C0 after reaction with different doses of H2O2. Fig. 11 shows that, with an increase in H2O2 dose from 0.5 to 5 mmol L−1, the dye removal efficiency increased respectively within 40 min of reaction due to the enhanced production of hydroxyl radicals, and when the dose of H2O2 was 0.05 and 0.1 mmol L−1, the dye degradation rate was insufficient. However, the dose of 1 mmol L−1 of H2O2 was appropriate, and the maximum degradation efficiency was obtained within 40 min in comparison to the other high concentration doses. Furthermore, this phenomenon clearly indicated that high concentrations of H2O2 cannot increase the degradation efficiency.[67,68]

Fig. 11

Evolution over time of C/C0 for the degradation of dye: (a) methylene blue, (b) reactive orange GRN, and (c) cationic violet X-5BLN dye degradation as a function of H2O2 concentration (TP-SF/Fe = 0.1 g, dye concentration = 20 mg L−1, time = 40 min, T = 50 °C).

Effects of initial dye concentration

The wastewater from textile industries typically has a wide range of color concentration, which is extremely harmful to the environment. The effect of initial dye concentration on the degradation of methylene blue, reactive orange GRN and cationic violet X-5BLN dyes was investigated at different times from 5 to 40 min with an adsorbent dose of 0.1 g and H2O2 concentration of 1 mmol L−1 at 50 °C. As shown in Fig. 12(a)–(c), different dye concentrations (10, 20, 40, 60 and 80 mg L−1) are used to determine the effect of dye concentration on the removal of dyes. The results presented in Fig. 12(a) show that the maximum dye removal efficiency of the initial concentration from 10–20 mg L−1 is obtained after reaction time at 40 min. As shown in Fig. 12(b) and (c), a similar character has been found in the other two dyes (reactive orange GRN and cationic violet X-5BLN) as a function of time.[60] However, it can be observed that as the concentration of the dye solution increases, the final degradation rate gradually reduces. Although for a maximum dye concentration of 80 mg L−1, the degradation efficiency was the lowest compared with other concentrations, but it still stayed over 91%, 83% and 91%, respectively. This phenomenon could be due to the fact that in the case of high dye concentration, the TP-SF/Fe catalyst can form a stable reaction system with H2O2. At this time, the hydroxyl radicals were not easy to neutralize, which increased the possibility of contact with the dyes and eventually led to a high removal.[69,70] These results suggested that a 20 mg L−1 concentration could be the optimum dye concentration for the highest removal rate.

Fig. 12

Evolution over time of C/C0 for the degradation of dyes: (a) methylene blue, (b) reactive orange GRN, and (c) cationic violet X-5BLN dye degradation as a function of dye concentration (TP-SF/Fe = 0.1 g, H2O2 concentration = 0.1 mmol L−1, time = 40 min, and T = 50 °C).

Effects of pH

The dyeing wastewater from the dyeing process of textiles has a wide range of pH values. The pH has an important role both in the characteristics of textile waste and the generation of hydroxyl radicals, which is greatly influenced in Fenton-like removal experiments by the surface of the catalyst.[71,72] The effect of the pH on the degradation experiments was investigated by using different pH values in the range of 3–10. The results obtained by the effect of pH on the degradation efficiency of dyes are shown in Fig. 13. The pH of the working solutions was maintained by using different amounts of 0.1 mol L−1 NaOH and 0.1 mol L−1 HNO3. It is apparent from the results in Fig. 13(a) and (c) that the degradation efficiency is high in acidic and basic conditions and the degradation is most rapid at pH 3 and 11. In addition, Fig. 13(b) shows that the degradation efficiency gradually decreases at higher pH and most of the dyes are degraded at pH 3. Strong acidic conditions are conducive for the generation of hydroxyl radical groups, which favor dye degradation and also the characteristics of the Fenton reaction. However, under strong acidic conditions, the SF catalyst surface takes a negative charge and can adsorb more cationic dyes, which could explain the result of Fig. 13(a) and (c).

Fig. 13

Evolution over time of C/C0 for the degradation of dyes: (a) methylene blue, (b) reactive orange GRN, and (c) cationic violet X-5BLN dye degradation as a function of pH (TP-SF/Fe = 0.1 g, H2O2 concentration = 0.1 mmol L−1, dye concentration = 20 mg L−1, time = 40 min, T = 50 °C).

Theory of adsorption isotherms

The analysis of isotherms methods is an important way to accurately represent the relationship between adsorbent and adsorbate for methylene blue, reactive orange GRN and cationic violet X-5BLN. In this work, the models of Langmuir and Freundlich isotherms are applied to recognize the range and degree of favourability of adsorption.

Langmuir isotherms

The analysis is based on the Langmuir isotherm models, which assume a homogeneous surface with uniform adsorption energy and exclusive coverage of the adsorbent. The linearized form of the Langmuir isotherm model is expressed by the following eqn (3):In this equation, qe (mg g−1) is the absorbed amount of the dyes (methylene blue, reactive orange GRN and cationic violet X-5BLN) at equilibrium, Ce (mg L−1) is the equilibrium concentration of the dye solution, KL is the Langmuir constant connected to the free energy of adsorption, and qm (mg g−1) is the maximum adsorption capacity at a complete monolayer.[73,74] The Langmuir isotherm parameters are determined from linear isotherm plots and the corresponding data are given in Fig. 14 and Table 2. The results obtained from the correlation coefficient (R2 values) show that the Langmuir isotherm parameters are acceptable and fit for the dyes (methylene blue, reactive orange GRN and cationic violet X-5BLN) and the maximum adsorption capacity is 13.0993 mg g−1 for the methylene blue dyes.

Fig. 14

Langmuir adsorption isotherms for methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes.

Langmuir adsorption constants of dyes on TP-SF/Fe

Type of dye	q m (mg g−1)	K L	R 2
Methylene blue	13.0993	1.9131	0.91012
Reactive orange GRN	5.2260	3.1307	0.9070
Cationic violet X-5BLN	6.1376	2.4449	0.9420

Freundlich isotherm

The Freundlich model is applied to describe the adsorption of dye on a heterogeneous surface by multilayer adsorption. The linearized Freundlich isotherm adsorption model is exposed by eqn (4):where qe (mg g−1) is the amount of dye adsorbed per unit weight of adsorbent, n is the Freundlich constant indicative of adsorption concentration of the adsorbents, and Kf is the Freundlich coefficient related to the adsorption capacity of the dye adsorbed onto the adsorbent per unit equilibrium concentration. Freundlich parameters can be calculated and the values of n and Kf are achieved from the linear isotherm plots of log qeversus log Ce curves[75,76] and their values are given in Fig. 15 and Table 3. Furthermore, the results indicate that the correlation coefficient values (R2 values) are fitted for the methylene blue, reactive orange GRN and cationic violet X-5BLN dyes. This also suggests that dye removal on TP-SF/Fe may be multilayer coverage.

Fig. 15

Freundlich adsorption isotherms for methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes.

Freundlich adsorption constants of the dyes on TP-SF/Fe

Type of dye	n	K f	R 2
Methylene blue	1.714	2.5307	0.9619
Reactive orange GRN	2.1728	1.7759	0.9953
Cationic violet X-5BLN	1.3887	2.1644	0.9991

Adsorption kinetics

It is important to study the adsorption kinetics in dye removal from aqueous solutions. The kinetics of adsorption can be helpful to determine the adsorption capacity of dyes by TP-SF/Fe. The adsorption kinetics of methylene blue, reactive orange GRN and cationic violet X-5BLN dyes at different times were analyzed by applying pseudo-first order and pseudo-second order kinetic models to recognize the solute absorption rate and transient behavior of the adsorption process.

Pseudo-first order kinetics

The linearized form of pseudo-first order is given by eqn (5):where qe (mg g−1) is the equilibrium adsorption capacity, q (mg g−1) is the adsorption capacity at time t, and k1 is the rate constant of the pseudo-first order model. The values of k1 and adsorption capacity qe can be obtained from the slopes and intercepts of the plots of ln(qe − q) against t, respectively. Moreover, the resultant parameters show that the correlation coefficient values of different dyes for the pseudo-first order model are acceptable and fitted (Fig. 16 and Table 4), indicating that pseudo-first order kinetics could be sufficient to describe the adsorption mechanism of dyes on the surface of TP-SF/Fe adsorbents.[77,78]

Fig. 16

Pseudo-first order kinetics for methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes.

Pseudo-first order kinetics parameters for methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes on TP-SF/Fe

Type of dye	q m (mg g−1)	k 1	R 2
Methylene blue	1.5582	0.07217	0.9686
Reactive orange GRN	1.159	0.04364	0.9976
Cationic violet X-5BLN	1.0122	0.0385	0.9916

Pseudo-second order kinetics

The linearized form of pseudo-second order is given by eqn (6):where qe (mg g−1) and q (mg g−1) is the adsorption capacity at time t and at equilibrium, respectively and k2 (g mg−1 min−1) is the pseudo-second order rate constant. The values of the pseudo-second order rate constant k2 and equilibrium adsorption volume qe can be determined from the slopes and intercepts of the plots of t/qversus t, respectively. The resultant parameter indicates that the correlation coefficient values of different dyes for the pseudo-second order model are also acceptable and fitted (Fig. 17 and Table 5). Moreover, the analysis of kinetics studies confirmed that the pseudo-first equation model could fit better than the pseudo-second order equation for the dye adsorption.[79,80]

Fig. 17

Pseudo-second order kinetics for methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes.

Pseudo-second order kinetics parameters for methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes on TP-SF/Fe

Type of dye	q m (mg g−1)	k 2	R 2
Methylene blue	2.153	0.0738	0.9136
Reactive orange GRN	1.5049	0.1345	0.9598
Cationic violet X-5BLN	1.0299	0.1236	0.9039

Reusability study

Reusability is an important factor in the dye removal process to evaluate experimental uses with a cost-effective method. Fig. 18 shows the effect of reusability cycles on the removal of methylene blue, reactive orange GRN and cationic violet X-5BLN dyes and five successive adsorption cycles are observed. In the study, the recyclability of TP-SF/Fe for the degradation of dyes was determined in the presence of 0.1 g of TP-SF/Fe and 0.1 mmol L−1 of H2O2 with a time of 30 min at pH 3, respectively. After every experimental run, the TP-SF/Fe was washed with deionized water and dried in a vacuum oven for repeated use. It was observed that the reusability cycle of TP-SF/Fe on dye removal for the 5th cycle was 98% for methylene blue, 79% for reactive orange GRN and 78% for cationic violet X-5BLN dyes. The reason may be that the small molecular products of dye degradation are adsorbed or complexed on the surface of TP-SF/Fe, which prevents them from catalyzing the decomposition of H2O2 to produce hydroxyl radicals. However, these results propose that the modified waste silk can be used for dye removal activities.

Fig. 18

Reusability analysis for the adsorption of methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes.

Furthermore, this research shows that the adsorption capacity of TP-SF/Fe for methylene blue is higher than many adsorbents explored in the literature. It may well be used in textile dye removal activities for its eco-friendliness, low-cost and satisfactory adsorption ability. The comparative results are listed in Table 6.

A comparison of adsorption capacities for methylene blue dyes using different adsorbents from previous research

Adsorbent	q e (mg g−1)	Reference
TP-SF/Fe	13.09	Present study
Orange peel	5.87	7
Titanate nanotubes (TNT24)	5.644	15
Polyethylene glycol 400 (Sn-PEG4)	7.3	16
Marine seaweed	5.23	36
Cu2O nanoparticles	2.08	56
Sawdust	4.89	74
Rice husk	9.83	75
Bamboo dust carbon	9.66	79

Conclusions

In this study, tea-phenol grafted waste silk fibers loaded with iron particles (TP-SF/Fe) were successfully used as an adsorbent for the efficient removal of methylene blue, reactive orange GRN, and cationic violet X-5BLN dyes from aqueous solution. The surface properties of TP-SF/Fe were investigated via FT-IR, SEM, EDS, and EDX analyses, which confirmed the successful loading of iron particles on the surface of TP-coated waste silk fibers. The TP-SF/Fe sample is a potential catalyst for the Fenton-like removal of aromatic dyes. The experimental results showed that pH is an important factor in the removal of dyes, and the maximum adsorption (99%) of dyes was achieved at 30 min. Moreover, the elevated results of the adsorption of dyes can be better explained based on the Freundlich adsorption isotherm model and pseudo-second order kinetics. The catalyst was reused five times for each dye. Therefore, waste silk can be used as a fiber-based catalyst for the Fenton-like removal of toxic pollutants from water.

Conflicts of interest

The authors declare that they have no conflicts of interest with respect to the research, authorship, and/or publication of this article.