Simultaneous Removal of Cr(VI) and Phenol from Water Using Silica-di-Block Polymer Hybrids: Adsorption Kinetics and Thermodynamics

Heavy metal ions and organic pollutants often coexist in industrial effluents. In this work, silica-di-block polymer hybrids (SiO2-g-PBA-b-PDMAEMA) with two ratios (SiO2/BA/DMAEMA = 1/50/250 and 1/60/240) were designed and prepared for the simultaneous removal of Cr(VI) and phenol via a surface-initiated atom-transfer radical polymerization process using butyl methacrylate (BA) as a hydrophobic monomer and 2-(Dimethylamino)ethylmethacrylate (DMAEMA) as a hydrophilic monomer. The removal efficiency of Cr(VI) and phenol by the hybrids reached 88.25% and 88.17%, respectively. The sample with a larger proportion of hydrophilic PDMAEMA showed better adsorption of Cr(VI), and the sample with a larger proportion of hydrophobic PBA showed better adsorption of phenol. In binary systems, the presence of Cr(VI) inhibited the adsorption of phenol, yet the presence of phenol had a negligible effect on the adsorption of Cr(VI). Kinetics studies showed that the adsorption of Cr(VI) and phenol fitted the pseudo-second-order model well. Thermodynamic studies showed that the adsorption behavior of Cr(VI) and phenol were better described by the Langmuir adsorption isotherm equation, and the adsorption of Cr(VI) and phenol were all spontaneous adsorptions driven by enthalpy. The adsorbent still possessed good adsorption capacity for Cr(VI) and phenol after six adsorption–desorption cycles. These findings show that SiO2-g-PBA-b-PDMAEMA hybrids represent a satisfying adsorption material for the simultaneous removal of heavy metal ions and organic pollutants.


Introduction
Water pollution is a worldwide problem that requires urgent attention and prevention. Heavy metal ions [1,2] and organic pollutants [3,4] are common pollutants in water which pose a serious threat to human health and the ecological environment. The most commonly toxic heavy metal ions in water include Cr(VI) [5][6][7], As(III) [8], Cd(II) [9], Hg(II) [10], Pb(II) [11], Cu(II) [12], Zn(II) [13], etc. The main organic pollutants include phenolic compounds [14,15], benzene compounds [16,17], halohydrocarbons [18,19] and so on. Among various water purification and recycling technologies, adsorption is a fast, effective, easy to operate, inexpensive, and a universal method [20,21]. Current research on adsorbent development mainly focuses on the adsorption of a certain type of pollutant like heavy metal ions or organic pollutants. But in practical application, adsorption materials are required to have good adsorption performance for different types of pollutants [22,23]. Therefore, it is urgent to design a new type of adsorption material which can adsorb metal ions and organic molecules simultaneously and efficiently.
Organic/inorganic nano-hybrids have significant advantages in terms of having inorganic nanoparticles with high specific surface area, high mechanical strength, high atoms into SiO2-NH2. An amount of 0.5 g SiO2-NH2 and 10 mL THF was added into a dried Schlenk flask and dispersed by ultrasound for 30 min. Under the condition of an ice bath, the Schlenk flask was filled with N2 via three vacuum/N2 cycles and the suspension was stirred for 30 min. An amount of 1.5 mL TEA was added subsequently and then mixed with the solution of 3 mL BiBB and 40 mL THF was injected dropwise into the flask to react for 4 h in an ice bath followed by 48 h of reaction in a water bath at 35 ℃. After centrifugation, the lower solid layer was alternately washed and centrifuged with water and ethanol. The silica surface-initiator (SiO2-Br) was obtained after vacuum-drying at 50 ℃ for 36 h with a yield of 72%. The synthesis scheme of the silica initiator SiO2-Br is given in Scheme 1.

Preparation of SiO2-g-PBA-b-PDMAEMA Hybrids by SI-ATRP
SiO2-g-PBA-b-PDMAEMA hybrids were obtained via a one-step ATRP. CuCl and CuCl2 were added into a dried Schlenk flask, and the flask was sealed with a rubber septum prior to three vacuum/N2 cycles. BA and PMDETA were injected into the flask, followed by the suspension of SiO2-Br dispersed in cyclohexanone; the reaction was performed at 90 ℃ for 24 h. After cooling to 70 ℃, the cyclohexanone solution of DMAEMA was injected, and the reaction was performed at 70 ℃ for 24 h. SiO2-g-PBA-b-PDMAEMA was finally obtained by centrifugation and washing with THF. The synthesis scheme of SiO2-g-PBA-b-PDMAEMA is also given in Scheme 1, and the detailed recipes of polymerization are listed in Table 1.

Characterization of Initiator and Hybrids
The chemical structures for SiO2-Br and SiO2-g-PBA-b-PDMAEMA were characterized by Fourier transform infrared spectroscopy (FTIR, Nicolet-380, Thermo Electron Corporation, USA) in a spectral range of 4000-400 cm −1 . The molecular weights of PBA-b-Scheme 1. Synthesis of SiO 2 -g-PBA-b-PDMAEMA.

Preparation of SiO 2 -g-PBA-b-PDMAEMA Hybrids by SI-ATRP
SiO 2 -g-PBA-b-PDMAEMA hybrids were obtained via a one-step ATRP. CuCl and CuCl 2 were added into a dried Schlenk flask, and the flask was sealed with a rubber septum prior to three vacuum/N 2 cycles. BA and PMDETA were injected into the flask, followed by the suspension of SiO 2 -Br dispersed in cyclohexanone; the reaction was performed at 90 • C for 24 h. After cooling to 70 • C, the cyclohexanone solution of DMAEMA was injected, and the reaction was performed at 70 • C for 24 h. SiO 2 -g-PBA-b-PDMAEMA was finally obtained by centrifugation and washing with THF. The synthesis scheme of SiO 2 -g-PBA-b-PDMAEMA is also given in Scheme 1, and the detailed recipes of polymerization are listed in Table 1.

Characterization of Initiator and Hybrids
The chemical structures for SiO 2 -Br and SiO 2 -g-PBA-b-PDMAEMA were characterized by Fourier transform infrared spectroscopy (FTIR, Nicolet-380, Thermo Electron Corporation, USA) in a spectral range of 4000-400 cm −1 . The molecular weights of PBA-b-PDMAEMA cleaved from SiO 2 -g-PBA-b-PDMAEMA by hydrofluoric acid were measured by gel permeation chromatograph (GPC, PL-GPC50, Agilent, USA), equipped with the PL gel-MIXEDC chromatographic column and were calibrated by polystyrene standards. THF was used as the eluent, and the flow rate was 0.5 mL·min −1 . The particles of SiO 2 -g-PBA-b-PDMAEMA were observed by transmission electron microscopy (TEM, Talos F200X, FEI, Czech Republic) at an acceleration voltage of 200 kV. Samples were ultrasounded in water for 30 min before measurement. The surface-grafted density of SiO 2 -Br was obtained by thermogravimetric analyzer (TGA, STA449, NETZSCH, Germany) under N 2 atmosphere using a heating rate of 10 • C·min −1 from 25 • C to 1000 • C.

Batch Adsorption Study
The batch mode adsorption studies were carried out by adding 0.05 g SiO 2 -g-PBAb-PDMAEMA into 50 mL Cr(VI) aqueous solutions (prepared by dissolving K 2 Cr 2 O 7 in deionized water and mostly existing as HCrO 4 − and CrO 4 2− [43]) or 50 mL phenol aqueous solutions on a shaker at 120 rpm under controlled pH of 6. After thermostatic shaking for a certain period of time, supernatant obtained by centrifugation was analyzed to detect the concentration of Cr(VI) or phenol residues.
The concentration of residue Cr(VI) was determined using a ultraviolet-visible spectrophotometer (UV-Vis, Cary 5000, Agilent, USA) and developing a purple-violet color with 1,5-diphenyl carbazide in acidic solution as a complexing agent [44,45]. The absorbance of the purple-violet colored solution was read at 540 nm after 10 min of color development.
The concentration of phenol residue was determined using a UV-Vis spectrophotometer with maximum absorption wavelength of 270 nm [46,47].
The equilibrium adsorption amount Q e (mg·g −1 ) of SiO 2 -g-PBA-b-PDMAEMA of Cr(VI) or phenol was calculated according to Equation (1) [48]. The percentage removal η(%) was calculated according to Equation (2) [4]: where C 0 (mg·L −1 ) and C t (mg·L −1 ) are the initial concentrations and equilibrium concentrations of Cr(VI) or phenol, respectively, and V (L) is the volume of the solution and W (g) is the weight of the adsorbent.

Adsorption Kinetics
Adsorption kinetics were investigated to evaluate both the rate of Cr(VI) or phenol adsorption and the equilibrium time required for the adsorption isotherm. Experiments were conducted under an initial Cr(VI) or phenol concentration of 100 mg·L −1 , a controlled temperature of 298 K, and a controlled time t (5 min, 10 min, 20 min, 30 min, 60 min, 90 min, 120 min, 180 min, and 240 min).
Adsorption rate was analyzed using two kinetic models, i.e., the pseudo-first-order model and pseudo-second-order model. The pseudo-first-order kinetic model is expressed by Equation (3) [48]: where Q e (mg·g −1 ) and Q t (mg·g −1 ) are the amount of Cr(VI) or phenol adsorbed at the equilibrium and time t (min), respectively, and k 1 (min −1 ) is the pseudo-first-order rate constant for the adsorption process. Values of k 1 were calculated from the slope of the ln(Q e −Q t ) vs. t plot. Values of Q e were calculated from the intercept of the ln(Q e −Q t ) vs. t plot.
where Q e (mg·g −1 ) and Q t (mg·g −1 ) are the amount of Cr(VI) or phenol adsorbed at the equilibrium and time t (min), respectively, and k 2 (g·mg −1 ·min −1 ) is the pseudo-secondorder rate constant for the adsorption process. Values of k 2 and Q e were calculated from the slope and intercept of the t/Q t vs. t plot.
Two isotherm models were investigated, i.e., the Langmuir model and the Freundlich model. The Langmuir model is expressed by Equation (5) [48]: C e /Q e = 1/(Q m K L ) + C e /Q m (5) where Q e is the equilibrium adsorption capacity (mg·g −1 ), C e is the equilibrium concentration in the solution (mg·L −1 ), Q m is the maximum adsorption capacity (mg·g −1 ), and K L is the Langmuir adsorption isotherm constant (L·mg −1 ). Values of Q m were calculated from the slope of the C e /Q e vs. C e plot. Values of K L were calculated from the intercept of the C e /Q e vs. C e plot. The Freundlich model is expressed by Equation (6) [48]: lnQ e = lnK f + (1/n)lnC e (6) where Q e is the equilibrium adsorption capacity (mg·g −1 ) and C e is the equilibrium concentration in the solution (mg·L −1 ). K f is the Freundlich adsorption isotherm constant [(mg·g −1 ) (L·mg −1 ) 1/n )]. The term 1/n is related to the magnitude of the adsorption driving force. Values of n were calculated from the slope of the lnQ e vs. lnC e plot. Values of K f were calculated from the intercept of the lnQ e vs. lnC e plot.
∆G was calculated according to Equation (7) [48][49][50]: where R is the universal gas constant (8.314 J·mol −1 ·K −1 ), T is the absolute temperature (K), and K is the derived Langmuir equilibrium constant. ∆H and ∆S were calculated according to the van't Hoff equation, which is expressed by Equation (8) [48]: where K is the derived Langmuir equilibrium constant, R is the gas constant (8.314 J·mol −1 ·K −1 ), and T is the absolute temperature (K). According to Equation (8), a linear relationship exists between lnK and 1/T. ∆H and ∆S were calculated from the slope and the intercept of the lnK vs. 1/T plot, respectively.

Recovery Experiments
Six adsorption-desorption cycles were carried out to evaluate the recovery performance of the adsorbent. The adsorption of Cr(VI) or phenol was conducted at an initial concentration of 100 mg·L −1 , a controlled pH of 6, and a controlled temperature of 298 K. After adsorption equilibrium, the adsorbed Cr(VI) was removed from the adsorbent using 0.1 mol·L −1 nitric acid. The adsorbent was washed with deionized water and vacuumdried before use. The adsorbed phenol was removed from the adsorbent using ethanol. The adsorbent was washed with deionized water and vacuum-dried before use.

Binary Systems Competitive Adsorption
The binary-system adsorption studies were carried out using batch mode adsorption to understand the competitive behavior between Cr(VI) and phenol onto SiO 2 -g-PBA-b-PDMAEMA. The adsorption experiments were conducted by controlling the initial Cr(VI) concentration of 100 mg·L −1 and varying the initial phenol concentration stepwise or by controlling the initial phenol concentration of 100 mg·L −1 and varying the initial Cr(VI) concentration stepwise. The concentration of Cr(VI) residue was measured according to the diphenyl carbazide spectrophotometric method using a UV-Vis spectrophotometer at a wavelength of 540 nm. The concentration of phenol residue was determined using a UV-Vis spectrophotometer at a wavelength of 270 nm. The equilibrium adsorption amount Q e (mg·g −1 ) was calculated according to Equation (1).

Adsorbent Characterizations
The preparation of the silica initiator SiO 2 -Br was confirmed by FTIR and TGA analysis shown in Figure 1. The new peaks in the FTIR spectrum of SiO 2 -NH 2 at 2926 cm −1 , 2854 cm −1 , and 1466 cm −1 were attributed to the C-H vibration of APTES, which proved the grafting of APTES to SiO 2 . Compared with the FTIR spectrum of SiO 2 -NH 2 , the new peak in the spectrum of SiO 2 -Br at 1735 cm −1 was attributed to the C=O vibration of BiBB, which proved the grafting of BiBB onto SiO 2 -NH 2 . Furthermore, the TGA curves showed that the weight loss from 100 • C to 1000 • C for SiO 2 , SiO 2 -NH 2 , and SiO 2 -Br was 5.16%, 7.88%, and 21.93%, respectively; the weight loss below 100 • C was owed to the removal of the water absorbed physically. According to these results, the graft density was calculated at 0.81 mmol·g −1 for SiO 2 -Br by the content of Br in SiO 2 -Br. The binary-system adsorption studies were carried out using batch mode adsorption to understand the competitive behavior between Cr(VI) and phenol onto SiO2-g-PBA-b-PDMAEMA. The adsorption experiments were conducted by controlling the initial Cr(VI) concentration of 100 mg·L −1 and varying the initial phenol concentration stepwise or by controlling the initial phenol concentration of 100 mg·L −1 and varying the initial Cr(VI) concentration stepwise. The concentration of Cr(VI) residue was measured according to the diphenyl carbazide spectrophotometric method using a UV-Vis spectrophotometer at a wavelength of 540 nm. The concentration of phenol residue was determined using a UV-Vis spectrophotometer at a wavelength of 270 nm. The equilibrium adsorption amount Qe (mg·g −1 ) was calculated according to Equation (1).

Adsorbent Characterizations
The preparation of the silica initiator SiO2-Br was confirmed by FTIR and TGA analysis shown in Figure 1. The new peaks in the FTIR spectrum of SiO2-NH2 at 2926 cm −1 , 2854 cm −1 , and 1466 cm −1 were attributed to the C-H vibration of APTES, which proved the grafting of APTES to SiO2. Compared with the FTIR spectrum of SiO2-NH2, the new peak in the spectrum of SiO2-Br at 1735 cm −1 was attributed to the C=O vibration of BiBB, which proved the grafting of BiBB onto SiO2-NH2. Furthermore, the TGA curves showed that the weight loss from 100 ℃ to 1000 ℃ for SiO2, SiO2-NH2, and SiO2-Br was 5.16%, 7.88%, and 21.93%, respectively; the weight loss below 100 ℃ was owed to the removal of the water absorbed physically. According to these results, the graft density was calculated at 0.81 mmol·g −1 for SiO2-Br by the content of Br in SiO2-Br.  The verification of BA and DMAEMA grafting onto the silica surface was obtained by the FTIR and GPC analysis of SiO 2 -g-PBA-b-PDMAEMA shown in Figure 2. The peaks in the FTIR spectrum at 2958 cm −1 and 2821 cm −1 were attributed to the stretching vibration of C-H in the PBA and PDMAEMA chains. The peaks at 1732 cm −1 were attributed to the stretching vibration of C=O. The peaks at 1105 cm −1 were attributed to the stretching vibration of Si-O-Si. The FTIR spectrum of SiO 2 -g-PBA-b-PDMAEMA showed that PBA and PDMAEMA chains were successfully grafted onto the silica initiator SiO 2 -Br. Furthermore, after etching by hydrofluoric acid, the molecular weights (M n ) of PBA-b-PDMAEMA cleaved from SiO 2 -g-PBA-b-PDMAEMA were 32,930 g·mol −1 for S1 and 38,420 g·mol −1 for S2, which were close to the theoretical value for the single arm (45711 g·mol −1 for S1 and 45,421 g·mol −1 for S2, calculated from Table 1). The polydispersity indexes (PDIs) were 1.304 for S1 and 1.391 for S2, which revealed the narrow distribution of the molecular weights. GPC results illustrated that the polymerizations initiated by SiO 2 -Br were all typically controllable ATRP, and the PBA-b-PDMAEMA chains were grafted as expected.
TEM images of SiO 2 and SiO 2 -g-PBA-b-PDMAEMA at 100 nm are shown in Figure 3. The particle size of SiO 2 was about 20 nm. After grafting via PBA-b-PDMAEMA chains, the silica-di-block polymer hybrids formed spherical particles with a significantly increased diameter of 35-40 nm. Since the PBA-b-PDMAEMA chains stretched in water to some extent, the contact between the pollutants and the adsorbent in water could be improved.
PDMAEMA cleaved from SiO2-g-PBA-b-PDMAEMA were 32,930 g·mol −1 for S1 and 38,420 g·mol −1 for S2, which were close to the theoretical value for the single arm (45711 g·mol −1 for S1 and 45,421 g·mol −1 for S2, calculated from Table 1). The polydispersity indexes (PDIs) were 1.304 for S1 and 1.391 for S2, which revealed the narrow distribution of the molecular weights. GPC results illustrated that the polymerizations initiated by SiO2-Br were all typically controllable ATRP, and the PBA-b-PDMAEMA chains were grafted as expected. TEM images of SiO2 and SiO2-g-PBA-b-PDMAEMA at 100 nm are shown in Figure 3. The particle size of SiO2 was about 20 nm. After grafting via PBA-b-PDMAEMA chains, the silica-di-block polymer hybrids formed spherical particles with a significantly increased diameter of 35-40 nm. Since the PBA-b-PDMAEMA chains stretched in water to some extent, the contact between the pollutants and the adsorbent in water could be improved.   TEM images of SiO2 and SiO2-g-PBA-b-PDMAEMA at 100 nm are shown in Figure 3. The particle size of SiO2 was about 20 nm. After grafting via PBA-b-PDMAEMA chains, the silica-di-block polymer hybrids formed spherical particles with a significantly increased diameter of 35-40 nm. Since the PBA-b-PDMAEMA chains stretched in water to some extent, the contact between the pollutants and the adsorbent in water could be improved.

Single Systems Adsorption Kinetics
Single system adsorption kinetics curves are shown in Figure 4. As a comparison, adsorption using bare nano-silica was also discussed. It could be seen from Figure 4a that Cr(VI) was adsorbed by SiO 2 -g-PBA-b-PDMAEMA rapidly within 0-20 min, and the removal efficiency of Cr(VI) tended to be a constant after 60 min. The removal efficiency vs. t plot suggested to us that it took about 60 min for Cr(VI) to reach adsorption equilibrium on the surface of the adsorbent. The removal efficiency of Cr(VI) on S1 was 88.25%, which was more than 17-times higher than the removal efficiency using bare nano-silica (5.01%). In addition, the removal efficiency of Cr(VI) on S1 was higher than that of Cr(VI) on S2 (79.88%). This was probably because of the larger proportion of PDMAEMA in S1, which might have a stronger affinity for water-soluble ions. Figure 4b shows that phenol was adsorbed by SiO 2 -g-PBA-b-PDMAEMA rapidly within 0-30 min, and the removal efficiency of phenol tended to be constant after 120 min. This suggested to us that the adsorption equilibrium was achieved within 120 min for phenol on the adsorbent. The removal efficiency of phenol on S2 was 88.17%, which was more than 9-times higher than the removal efficiency using bare nano-silica (9.09%) and was higher than the removal efficiency of phenol on S1 (80.44%). The adsorption capacity of SiO 2 -g-PBA-b-PDMAEMA for phenol greatly improved after functionalization, and the larger proportion of hydrophobic PBA in S2 might be more conducive to the absorption of organic pollutants. efficiency of phenol tended to be constant after 120 min. This suggested to us that the adsorption equilibrium was achieved within 120 min for phenol on the adsorbent. The removal efficiency of phenol on S2 was 88.17%, which was more than 9-times higher than the removal efficiency using bare nano-silica (9.09%) and was higher than the removal efficiency of phenol on S1 (80.44%). The adsorption capacity of SiO2-g-PBA-b-PDMAEMA for phenol greatly improved after functionalization, and the larger proportion of hydrophobic PBA in S2 might be more conducive to the absorption of organic pollutants. The adsorption kinetics data obtained experimentally were fitted to the pseudo-firstorder and pseudo-second-order models. The fitting results are shown in Figure 5 and Table 2.
The pseudo-second-order model showed much better fitting to Cr(Ⅵ), and phenol adsorption data with higher correlation coefficients (R 2 > 0.99) and a better agreement between experimental (Qe,exp) and calculated (Qe,cal) values is also exhibited in Table 2. This indicated that the adsorption rates of Cr(Ⅵ) and phenol onto SiO2-g-PBA-b-PDMAEMA were controlled by chemical processes [9]. The rate constant k2 of Cr(Ⅵ) on S1 (0.00242 g·mg −1 ·min −1 ) was relatively higher than that of Cr(Ⅵ) on S2 (0.00167 g·mg −1 ·min −1 ), indicating a faster uptake of Cr(Ⅵ) onto S1. Similarly, the rate constant k2 of phenol on S2 (0.00054 g·mg −1 ·min −1 ) was relatively higher than that of phenol on S1 (0.00038 g·mg −1 ·min −1 ), indicating a faster uptake of phenol onto S2. The adsorption kinetics data obtained experimentally were fitted to the pseudo-firstorder and pseudo-second-order models. The fitting results are shown in Figure 5 and Table 2.

Single Systems Adsorption Isotherms and Thermodynamic Study
The adsorption isotherms of Cr(Ⅵ) or phenol in aqueous solution by SiO2-g-PBA-b-PDMAEMA at different temperatures are shown in Figure 6. The equilibrium adsorption capacity of Cr(Ⅵ) or phenol rose with the increase of Cr(Ⅵ) or phenol equilibrium concentration and then tended to be constant, i.e., the saturated adsorption capacity. On the other hand, the equilibrium adsorption capacity of Cr(Ⅵ) or phenol decreased with the increase in adsorption temperature, indicating that the adsorption of Cr(Ⅵ) and phenol were all exothermic processes under experimental conditions. Decreasing the temperature was favorable for the adsorption of Cr(Ⅵ) or phenol on SiO2-g-PBA-b-PDMAEMA.   The pseudo-second-order model showed much better fitting to Cr(VI), and phenol adsorption data with higher correlation coefficients (R 2 > 0.99) and a better agreement between experimental (Q e,exp ) and calculated (Q e,cal ) values is also exhibited in Table 2. This indicated that the adsorption rates of Cr(VI) and phenol onto SiO 2 -g-PBA-b-PDMAEMA were controlled by chemical processes [9]. The rate constant k 2 of Cr(VI) on S1 (0.00242 g·mg −1 ·min −1 ) was relatively higher than that of Cr(VI) on S2 (0.00167 g·mg −1 ·min −1 ), indicating a faster uptake of Cr(VI) onto S1. Similarly, the rate constant k 2 of phenol on S2 (0.00054 g·mg −1 ·min −1 ) was relatively higher than that of phenol on S1 (0.00038 g·mg −1 ·min −1 ), indicating a faster uptake of phenol onto S2.

Single Systems Adsorption Isotherms and Thermodynamic Study
The adsorption isotherms of Cr(VI) or phenol in aqueous solution by SiO 2 -g-PBA-b-PDMAEMA at different temperatures are shown in Figure 6. The equilibrium adsorption capacity of Cr(VI) or phenol rose with the increase of Cr(VI) or phenol equilibrium concentration and then tended to be constant, i.e., the saturated adsorption capacity. On the other hand, the equilibrium adsorption capacity of Cr(VI) or phenol decreased with the increase in adsorption temperature, indicating that the adsorption of Cr(VI) and phenol were all exothermic processes under experimental conditions. Decreasing the temperature was favorable for the adsorption of Cr(VI) or phenol on SiO 2 -g-PBA-b-PDMAEMA.

Single Systems Adsorption Isotherms and Thermodynamic Study
The adsorption isotherms of Cr(Ⅵ) or phenol in aqueous solution by SiO2-g-PBA-b-PDMAEMA at different temperatures are shown in Figure 6. The equilibrium adsorption capacity of Cr(Ⅵ) or phenol rose with the increase of Cr(Ⅵ) or phenol equilibrium concentration and then tended to be constant, i.e., the saturated adsorption capacity. On the other hand, the equilibrium adsorption capacity of Cr(Ⅵ) or phenol decreased with the increase in adsorption temperature, indicating that the adsorption of Cr(Ⅵ) and phenol were all exothermic processes under experimental conditions. Decreasing the temperature was favorable for the adsorption of Cr(Ⅵ) or phenol on SiO2-g-PBA-b-PDMAEMA.   Fitting curves and adsorption isotherm constants for Cr(Ⅵ) adsorption on S1 are shown in Figure 7 and Table 3. According to the desired R 2 greater than 0.99, the adsorption behavior of Cr(VI) on the adsorbent surface is deemed to be better described by the Langmuir adsorption isotherm equation, indicating that Cr(VI) was mainly adsorbed by monolayer. This was because, after the monolayer adsorption of Cr(VI) on the surface of Fitting curves and adsorption isotherm constants for Cr(VI) adsorption on S1 are shown in Figure 7 and Table 3. According to the desired R 2 greater than 0.99, the adsorption behavior of Cr(VI) on the adsorbent surface is deemed to be better described by the Langmuir adsorption isotherm equation, indicating that Cr(VI) was mainly adsorbed by monolayer. This was because, after the monolayer adsorption of Cr(VI) on the surface of the adsorbent, the excess Cr(VI) did not easily approach the surface of the adsorbent due to the existence of electrostatic repulsion. According to the fitting parameters in Table 3, the saturated adsorption capacity of Cr(VI) at 298 K reached 174.22 mg·g −1 . The n values fitted by the Freundlich adsorption isotherm equation were all greater than 1, indicating that the adsorption of Cr(VI) on S1 were beneficial adsorption processes [51]. At 298 K, the n value was between 2 and 10, indicating that the adsorption of Cr(VI) on S1 more easily occurred at room temperature [52].
Polymers 2022, 14, x FOR PEER REVIEW 10 of 16 the adsorbent, the excess Cr(VI) did not easily approach the surface of the adsorbent due to the existence of electrostatic repulsion. According to the fitting parameters in Table 3, the saturated adsorption capacity of Cr(VI) at 298K reached 174.22 mg·g −1 . The n values fitted by the Freundlich adsorption isotherm equation were all greater than 1, indicating that the adsorption of Cr(VI) on S1 were beneficial adsorption processes [51]. At 298 K, the n value was between 2 and 10, indicating that the adsorption of Cr(VI) on S1 more easily occurred at room temperature [52]. According to the Langmuir adsorption isotherm constant KL, the thermodynamic equilibrium constant K was obtained by getting rid of the unit. The plot of ln K vs. 1/T for thermodynamic parameter calculation is shown in the inset picture of Figure 7(a). The thermodynamic parameters calculated for Cr(Ⅵ) adsorption on S1 are shown in Table 3.  Table 3. Adsorption isotherm constants and thermodynamic parameters for Cr(VI) adsorption on S1 and phenol adsorption on S2.

Systems
Temperature /K According to the Langmuir adsorption isotherm constant K L , the thermodynamic equilibrium constant K was obtained by getting rid of the unit. The plot of ln K vs. 1/T for thermodynamic parameter calculation is shown in the inset picture of Figure 7a. The thermodynamic parameters calculated for Cr(VI) adsorption on S1 are shown in Table 3. ∆H < 0 indicated that the adsorption was an exothermic process. Reducing the temperature was conducive to adsorption, and the adsorption was enthalpy-driven adsorption-type behavior. ∆S < 0 indicated that the adsorption of Cr(VI) on S1 reduced the disorder degree of the system, and the adsorption was not entropy-driven adsorption-type behavior. ∆G ranged from −23.41 kJ·mol −1 to −22.58 kJ·mol −1 . The negative values of ∆G indicated that the adsorption was a spontaneous process. Moreover, it could be inferred that the adsorption driving force was more than the typical physical interactions since studies have shown that the ∆G of physical adsorption was −20-0 kJ·mol −1 and the ∆G of chemical adsorption was −400-−80 kJ·mol −1 [53]. ∆G of between −40 kJ·mol −1 and −20 kJ·mol −1 suggested to us that the main adsorption force might have been the electrostatic coulombic attraction [54]; this was consistent with our previous work on the adsorption of Cr(VI) to PDMAEMA chains [28].

Langmuir Freundlich Thermodynamic Parameters
Fitting curves and adsorption isotherm constants for phenol adsorption on S2 are shown in Figure 8 and Table 3. According to the desired R 2 (R 2 > 0.99), the adsorption behavior of phenol on the adsorbent surface could be better described by the Langmuir adsorption isotherm equation. The thermodynamic parameters calculated for phenol adsorption on S2 are shown in Table 3. ∆H < 0, ∆S < 0, ∆G < 0, indicated that the adsorption was spontaneous adsorption, driven by enthalpy. As ∆H=−36.5 kJ·mol −1 , which was a within the range of hydrogen bond adsorption enthalpy (2-40 kJ·mol −1 ) [55], it could be inferred that the adsorption of S2 to phenol might be dominated by the hydrogen bond adsorption of the carbonyl group to phenol. Because of the directivity and saturation of the hydrogen bond, the adsorption of phenol on the adsorbent surface was mainly monolayered. The n values fitted by the Freundlich adsorption isotherm equation were all above 1, indicating that the adsorption of phenol on S2 was a beneficial adsorption process. At 298 K, the n value was 2.0211, indicating that the adsorption of phenol on S2 could easily occur at room temperature.
inferred that the adsorption of S2 to phenol might be dominated by the hydrogen bond adsorption of the carbonyl group to phenol. Because of the directivity and saturation of the hydrogen bond, the adsorption of phenol on the adsorbent surface was mainly monolayered. The n values fitted by the Freundlich adsorption isotherm equation were all above 1, indicating that the adsorption of phenol on S2 was a beneficial adsorption process. At 298 K, the n value was 2.0211, indicating that the adsorption of phenol on S2 could easily occur at room temperature.

Recovery Performance
Six adsorption-desorption cycles were carried out to evaluate the recyclability of the adsorbent, which is an important point for practical applications. Figure 9 represents the adsorption-desorption cycle of Cr(Ⅵ) on S1 and phenol on S2. For the first three cycles, the adsorption amount of Cr(Ⅵ) was 87.92 mg·g −1 , 87.91 mg·g −1 , and 85.32 mg·g −1 , respectively, which showed stable adsorption performance of the hybrids to Cr(Ⅵ). After six adsorption-desorption cycles, the adsorption amount of Cr(Ⅵ) was 62.25 mg·g −1 , which accounted for 70.80% of the initial adsorption amount. These results indicated that the adsorbent still possessed an adequate adsorption capacity toward Cr(Ⅵ) after six cycles. For phenol adsorption, the adsorption amounts were 87.02 mg·g −1 , 86.98 mg·g −1 , and 85.43 mg·g −1 for the first three cycles, respectively, which also showed stable adsorption performance of the hybrids toward phenol. After six adsorption-desorption cycles, the adsorption amount for phenol was 72.79 mg·g −1 , which

Recovery Performance
Six adsorption-desorption cycles were carried out to evaluate the recyclability of the adsorbent, which is an important point for practical applications. Figure 9 represents the adsorption-desorption cycle of Cr(VI) on S1 and phenol on S2. For the first three cycles, the adsorption amount of Cr(VI) was 87.92 mg·g −1 , 87.91 mg·g −1 , and 85.32 mg·g −1 , respectively, which showed stable adsorption performance of the hybrids to Cr(VI). After six adsorption-desorption cycles, the adsorption amount of Cr(VI) was 62.25 mg·g −1 , which accounted for 70.80% of the initial adsorption amount. These results indicated that the adsorbent still possessed an adequate adsorption capacity toward Cr(VI) after six cycles. For phenol adsorption, the adsorption amounts were 87.02 mg·g −1 , 86.98 mg·g −1 , and 85.43 mg·g −1 for the first three cycles, respectively, which also showed stable adsorption performance of the hybrids toward phenol. After six adsorption-desorption cycles, the adsorption amount for phenol was 72.79 mg·g −1 , which accounted for 83.65% of the initial adsorption amount. These results indicated that the adsorbent also possessed a good adsorption capacity toward phenol after six cycles. Cr(Ⅵ) phenol Cycle number Figure 9. Adsorption-desorption cycle of Cr(Ⅵ) on S1 and phenol on S2

Binary Systems Competitive Adsorption Behavior
The effect of the initial concentration of phenol on Cr(Ⅵ) adsorption is shown in Figure 10(a). Phenol had little influence on the adsorption effect of Cr(Ⅵ). This was because when the pH ＜ 7.8 [28,56], amino existed in the form of quaternary ammonium, and strong electrostatic attraction could have happened between the quaternary ammonium in SiO2-g-PBA-b-PDMAEMA and Cr(VI) (in the forms of HCrO4 − and CrO4 2− ). The presence of phenol almost did not affect the electrostatic adsorption of Cr(Ⅵ) on the quaternary ammonium groups. The effect of the initial concentration of Cr(Ⅵ) on phenol adsorption is shown in Figure 10(b). With the increase of the initial concentration of Cr(Ⅵ), the adsorption capacity of phenol decreased gradually. This might be because potassium Figure 9. Adsorption-desorption cycle of Cr(VI) on S1 and phenol on S2.

Binary Systems Competitive Adsorption Behavior
The effect of the initial concentration of phenol on Cr(VI) adsorption is shown in Figure 10a. Phenol had little influence on the adsorption effect of Cr(VI). This was because when the pH < 7.8 [28,56], amino existed in the form of quaternary ammonium, and strong electrostatic attraction could have happened between the quaternary ammonium in SiO 2g-PBA-b-PDMAEMA and Cr(VI) (in the forms of HCrO 4 − and CrO 4 2− ). The presence of phenol almost did not affect the electrostatic adsorption of Cr(VI) on the quaternary ammonium groups. The effect of the initial concentration of Cr(VI) on phenol adsorption is shown in Figure 10b. With the increase of the initial concentration of Cr(VI), the adsorption capacity of phenol decreased gradually. This might be because potassium ion in potassium dichromate can form co-ordination bonds with carbonyl groups, which compete may have competed with phenol and reduced the adsorption active site for phenol. The presumed adsorption mechanism is shown in Figure 11. Strong electrostatic attraction between the positively charged quaternary ammonium in the PDMAEMA blocks and Cr(VI) existed as oxygen anion, as the main driving force for the Cr(VI) adsorption. Hydrogen bonds between ester groups in SiO 2 -g-PBA-b-PDMAEMA and phenol are the main driving forces for phenol adsorption. Generally, the silica-di-block polymer hybrids (SiO 2 -g-PBA-b-PDMAEMA) showed good adsorption performance toward Cr(VI) as well as phenol in both the single and binary systems. The adsorption capacity of the hybrids compared to other materials is given in Table 4 [5-7,14,57-60].

Binary Systems Competitive Adsorption Behavior
The effect of the initial concentration of phenol on Cr(Ⅵ) adsorption is shown in Figure 10(a). Phenol had little influence on the adsorption effect of Cr(Ⅵ). This was because when the pH ＜ 7.8 [28,56], amino existed in the form of quaternary ammonium, and strong electrostatic attraction could have happened between the quaternary ammonium in SiO2-g-PBA-b-PDMAEMA and Cr(VI) (in the forms of HCrO4 − and CrO4 2− ). The presence of phenol almost did not affect the electrostatic adsorption of Cr(Ⅵ) on the quaternary ammonium groups. The effect of the initial concentration of Cr(Ⅵ) on phenol adsorption is shown in Figure 10(b). With the increase of the initial concentration of Cr(Ⅵ), the adsorption capacity of phenol decreased gradually. This might be because potassium ion in potassium dichromate can form co-ordination bonds with carbonyl groups, which compete may have competed with phenol and reduced the adsorption active site for phenol. The presumed adsorption mechanism is shown in Figure 11. Strong electrostatic attraction between the positively charged quaternary ammonium in the PDMAEMA blocks and Cr(VI) existed as oxygen anion, as the main driving force for the Cr(Ⅵ) adsorption. Hydrogen bonds between ester groups in SiO2-g-PBA-b-PDMAEMA and phenol are the main driving forces for phenol adsorption. Generally, the silica-di-block polymer hybrids (SiO2-g-PBA-b-PDMAEMA) showed good adsorption performance toward Cr(Ⅵ) as well as phenol in both the single and binary systems. The adsorption capacity of the hybrids compared to other materials is given in Table 4 [5][6][7]14,[57][58][59][60].

Conclusions
In this work, silica-di-block polymer hybrids, SiO 2 -g-PBA-b-PDMAEMA, with two ratios (SiO 2 /BA/DMAEMA = 1/50/250 and 1/60/240) were obtained via SI-ATRP methodology. All the results of the experimental studies can be summarized as follows: (1) The results of FTIR and GPC proved that the SiO 2 -g-PBA-b-PDMAEMA hybrids were generated as expected; (2) The adsorbent had excellent adsorption effects for Cr(VI) as well as for phenol. Furthermore, changing the proportion of hydrophilic and hydrophobic chain segments allowed for the adjustment of the adsorption performance of the adsorbents for watersoluble ions and organic pollutants. S1 (SiO 2 /BA/DMAEMA = 1/50/250) showed a higher removal efficiency of Cr(VI) (88.25%) than S2 (SiO 2 /BA/DMAEMA = 1/60/240, 79.88%), and S2 showed a higher removal efficiency of phenol (88.17%) than S1 (80.44%); (3) Kinetics studies showed that the adsorption of Cr(VI) and phenol fitted the pseudosecond-order model well; (4) The thermodynamic studies showed that the adsorption of Cr(VI) and phenol were all exothermic processes; therefore, decreasing the temperature was favorable for the adsorption of Cr(VI) and phenol on SiO 2 -g-PBA-b-PDMAEMA. The adsorption behavior of Cr(VI) and phenol was better described by the Langmuir adsorption isotherm equation, indicating that Cr(VI) and phenol were mainly adsorbed by monolayer. Thermodynamic parameters showed that the adsorptions were all spontaneous adsorption driven by enthalpy; (5) The thermodynamic parameters suggested that the driving force of Cr(VI) adsorption on S1 was mainly the electrostatic attraction of anions by the quaternary ammonium of the PDMAEMA chains, while the adsorption of S2 to phenol was dominated by the hydrogen bond adsorption of carbonyl groups to phenol.
Further research will be conducted on simultaneous adsorption of various pollutants.