Acidic Mesoporous Zeolite ZSM-5 Supported Cu Catalyst with Good Catalytic Performance in the Hydroxysulfurization of Styrenes with Disulfides

Development of highly active heterogeneous catalysts is an effective strategy for modern organic synthesis chemistry. In this work, acidic mesoporous zeolite ZSM-5 (HZSM-5-M), acidic-free mesoporous zeolite TS-1 (TS-1-M), and basic ETS-10 zeolite supported metal Cu catalysts were prepared to investigate their catalytic performances in the hydroxysulfurization of styrenes with diaryl disulfides. The effect of pore size and acidities of the supports, as well as the Cu species electronic properties of the catalysts on reaction activity were investigated. The results show that Cu+ and Cu2+ binded on HZSM-5-M show the highest activity and product selectivity for the desired β-hydroxysulfides compounds.


Introduction
β-Hydroxysulfides are important intermediates for synthesis of various valuable biological active compounds, pharmaceuticals, and natural products, such as renin and leukotrienes [1][2][3]. Traditional methods for the preparation of β-hydroxysulfides involve the ring opening of epoxides with sulfenyl that comes from thiols in the homogenous metal-catalyzed reaction systems [4][5][6]. However, this protocol usually suffers from relatively low activity and undesirable side reaction [1]. To improve the reaction activity and product selectivity, many strategies have been developed. For example, various functional organic ligands were added into reaction mixtures for modification of the metals' electronic property to improve the reaction activity [7,8]; irradiation or peroxides were used in the reaction systems for the generation of sulfenyl radicals, improving the product selectivity [3,9,10]. Nevertheless, the product separation from the reaction mixture is complicated and catalyst reuse is difficult. From a sustainable and practical point of view, developing a highly efficient heterogeneous catalyst is significant for preparation of β-hydroxysulfide compounds.
It is well known that crystalline aluminosilicate zeolites have high surface area, tunable acidity, and unique framework structure [11], which as supports or catalysts show superior catalytic performance in many organic syntheses, such as carbon-carbon coupling [12], Knoevenagel [13], and oxidative coupling reactions [14]. As a continuous work focus on development of highly efficient heterogeneous catalyst for synthetic chemistry, in this work, H-form mesoporous zeolite ZSM-5 (HZSM-5-M) supported Cu catalyst (Cu/HZSM-5-M) was prepared and applied in the hydroxysulfurization of

Catalyst Preparation
The catalyst with Cu metal loading of 3 wt. % was prepared from incipient-wetness impregnation method. Typically, HZSM-5-M was impregnated with a solution containing an appropriate amount of Cu(NO 3 ) 2 ·6H 2 O, followed by drying at atmospheric temperature for 24 h and at 100 • C for 12 h. Finally, the dried sample was calcined at 450 • C for 4 h in air, and the obtained catalyst sample was denoted as Cu/HZSM-5-M. The Cu/HZSM-5, Cu/ETS-10, and Cu/TS-1-M catalysts were prepared using the same method. Additionally, Fe and Co supported on HZSM-5-M (Fe/HZSM-5-M and Co/HZSM-5-M) catalysts were also prepared by the same method except for using iron nitrate hydrate and cobalt nitrate hydrate, respectively.

Characterization
X-ray powder diffraction (XRD) pattern was obtained on a D/MAX 2500/PC powder diffractometer (Rigaku, Ltd., Tokyo, Japan) by using a Cu Kα radiation source. N 2 adsorption-desorption isotherms were measured at −196 • C on a Micromeritics ASAP2020M apparatus (Micromeritics Instrument Ltd., Darmstadt, Germany). The acidities of the supports were measured by ammonia temperatureprogrammed desorption (NH 3 -TPD) on a Micromeritics ASAP2920 instrument (Micromeritics Instrument Ltd., Darmstadt, Germany) according to previous work [15]. Total acidic site density of the support was determined by acid-base titration method [15]. The obtained NH 3 -TPD curve was deconvoluted at different maximum peak temperatures with a Gaussian function for fitting [17], and the peak areas were calculated. In this manner, the peak areas were correlated with the amount of adsorbed NH 3 in different temperature regions. The morphology and mesoporous structure of ZSM-5-M were observed by field-emission scanning electron microscope (SEM, SUPRA55, Zeiss Gruppe, Heidenheim, Germany) and transmission electron microscope (TEM, JEM-2100, JEOL Ltd., Tokyo, Japan), respectively. The electronic state of the Cu species in catalysts was analyzed by X-ray photoelectron spectroscopy (XPS) on an ESCALAB MK II system (VG Scientific Ltd., East Grinstead, UK). Cu content and atomic Si/Al(Ti) in the different samples were determined by inductively coupled plasma optical emission spectroscopy (ICP-OES) on a Perkin-Elmer 3300DV emission spectrometer (PerkinElmer, Waltham, MA, USA). The Cu content in Cu/ZSM-5-M, Cu/ZSM-5, Cu/TS-1-M, and Cu/ETS-10 catalysts was 3.0, 2.9, 3.0, and 2.9 wt. %, respectively (Table S1).

Catalyst Characterization
XRD patterns of ZSM-5-M and HZSM-5-M in Figure 1a give diffraction peaks at 2θ = 7.9°, 8.9°, 23°, 23.9°, and 24.5°, which is typical characteristics of ZSM-5 zeolite structure [15]. After loading of Cu on HZSM-5-M and calcination, the XRD diffraction peak position and intensity did not change, indicating that the ZSM-5 zeolite structure is well maintained for the Cu/HZSM-5-M sample. The diffraction peaks related with Cu species are not observed in the XRD pattern of Cu/HZSM-5-M, suggesting that small metal particles are dispersed in the Cu/HZSM-5-M sample. Similar phenomena were also observed in XRD patterns of TS-1-M and basic ETS-10 supported Cu catalysts ( Figure S1). Nitrogen adsorption-desorption isotherms of ZSM-5-M and Cu/HZSM-5-M samples give a steep step at relative pressure of 0.6-0.96 (Figure 1b), which is related to the presence of mesopores in the samples. Their corresponding mesopore size mainly centered at 22 and 21 nm ( Figure S2), respectively.  Figure 2a shows the SEM image of ZSM-5-M, giving a cylinder-like morphology with rough surface. The large cylinder-like particles are composed of nano-crystals with sizes of 50-150 nm. In this case, meso-macropores could be formed in the nanocrystal assemblies. The morphology of the TS-1-M, ZSM-5, and ETS-10 zeolites were also observed by SEM technique, and the results are shown in Figure S3. The SEM image reveals that the TS-1-M crystal particle exhibits a rough surface and has a particle size of 200-300 nm, while both of ZSM-5 and ETS-10 zeolite have a smooth surface with a large particle size.
The porous structure of the ZSM-5-M was characterized by TEM technique. It was observed that not only many intra-crystalline mesopores (white lines), but also abundant inter-crystalline mesopore and marcopores (light areas), are present in ZSM-5-M particles (Figure 2b).
The dispersion of metal partials on Cu/HZSM-5-M was observed by TEM technique, and the results are shown in Figure 3. The low-magnification TEM image shows that small metal particles (3-5 nm) highly disperse on the Cu/HZSM-5-M (Figure 3a). The high-magnification TEM image in Figure 3b displays that some metal particles with a lattice fringe of 0.21 and 0.22 nm corresponds to  (Table S1).

Catalyst Characterization
XRD patterns of ZSM-5-M and HZSM-5-M in Figure 1a give diffraction peaks at 2θ = 7.9°, 8.9°, 23°, 23.9°, and 24.5°, which is typical characteristics of ZSM-5 zeolite structure [15]. After loading of Cu on HZSM-5-M and calcination, the XRD diffraction peak position and intensity did not change, indicating that the ZSM-5 zeolite structure is well maintained for the Cu/HZSM-5-M sample. The diffraction peaks related with Cu species are not observed in the XRD pattern of Cu/HZSM-5-M, suggesting that small metal particles are dispersed in the Cu/HZSM-5-M sample. Similar phenomena were also observed in XRD patterns of TS-1-M and basic ETS-10 supported Cu catalysts ( Figure S1).    Figure S3. The SEM image reveals that the TS-1-M crystal particle exhibits a rough surface and has a particle size of 200-300 nm, while both of ZSM-5 and ETS-10 zeolite have a smooth surface with a large particle size.
The porous structure of the ZSM-5-M was characterized by TEM technique. It was observed that not only many intra-crystalline mesopores (white lines), but also abundant inter-crystalline mesopore and marcopores (light areas), are present in ZSM-5-M particles ( Figure 2b).
The dispersion of metal partials on Cu/HZSM-5-M was observed by TEM technique, and the results are shown in Figure 3. The low-magnification TEM image shows that small metal particles  In this case, meso-macropores could be formed in the nanocrystal assemblies. The morphology of the TS-1-M, ZSM-5, and ETS-10 zeolites were also observed by SEM technique, and the results are shown in Figure S3. The SEM image reveals that the TS-1-M crystal particle exhibits a rough surface and has a particle size of 200-300 nm, while both of ZSM-5 and ETS-10 zeolite have a smooth surface with a large particle size.
The porous structure of the ZSM-5-M was characterized by TEM technique. It was observed that not only many intra-crystalline mesopores (white lines), but also abundant inter-crystalline mesopore and marcopores (light areas), are present in ZSM-5-M particles ( Figure 2b).
The dispersion of metal partials on Cu/HZSM-5-M was observed by TEM technique, and the results are shown in Figure 3. The low-magnification TEM image shows that small metal particles  Figure 4 shows the NH3-TPD curves of the HZSM-5 and HZSM-5-H, giving similar NH3 desorption profile with peaks around 224, 326, and 421 °C, indicating that weak, medium, and strong acid sites are present in these samples. However, HZSM-5 has a large number of total acid site densities relative to HZSM-5-M. The acid-base titration results also demonstrated that the number of weak, medium and strong acid site on HZSM-5 is higher than that on HZSM-5-M ( Table 1). The NH3 desorption signal of TS-1-M sample was inconspicuous, indicating the absence of acidity on TS-1-M sample.  1 The weak, medium, and strong acid site is estimated from the corresponding area of the deconvoluted peaks, respectively, and the total acid site is determined by acid-base titration.
The chemical state of the Cu species on Cu/HZSM-5-M and Cu/TS-1-M catalysts was investigated by XPS. The Cu2p3/2 spectra in Figure 5 show two binding energies approximate 933.2 and 935.3 eV on Cu/HZSM-5-M catalyst corresponding to the Cu + and Cu 2+ species, respectively [19].  Figure 4 shows the NH3-TPD curves of the HZSM-5 and HZSM-5-H, giving similar NH3 desorption profile with peaks around 224, 326, and 421 °C, indicating that weak, medium, and strong acid sites are present in these samples. However, HZSM-5 has a large number of total acid site densities relative to HZSM-5-M. The acid-base titration results also demonstrated that the number of weak, medium and strong acid site on HZSM-5 is higher than that on HZSM-5-M ( Table 1). The NH3 desorption signal of TS-1-M sample was inconspicuous, indicating the absence of acidity on TS-1-M sample.  1 The weak, medium, and strong acid site is estimated from the corresponding area of the deconvoluted peaks, respectively, and the total acid site is determined by acid-base titration.
The chemical state of the Cu species on Cu/HZSM-5-M and Cu/TS-1-M catalysts was investigated by XPS. The Cu2p3/2 spectra in Figure 5 show two binding energies approximate 933.2 and 935.3 eV on Cu/HZSM-5-M catalyst corresponding to the Cu + and Cu 2+ species, respectively [19].  Figure 4 shows the NH 3 -TPD curves of the HZSM-5 and HZSM-5-H, giving similar NH 3 desorption profile with peaks around 224, 326, and 421 • C, indicating that weak, medium, and strong acid sites are present in these samples. However, HZSM-5 has a large number of total acid site densities relative to HZSM-5-M. The acid-base titration results also demonstrated that the number of weak, medium and strong acid site on HZSM-5 is higher than that on HZSM-5-M ( Table 1). The NH 3 desorption signal of TS-1-M sample was inconspicuous, indicating the absence of acidity on TS-1-M sample. The chemical state of the Cu species on Cu/HZSM-5-M and Cu/TS-1-M catalysts was investigated by XPS. The Cu2p 3/2 spectra in Figure 5 show two binding energies approximate 933.2 and 935.3 eV on Cu/HZSM-5-M catalyst corresponding to the Cu + and Cu 2+ species, respectively [19]. A similar phenomenon also existed on the Cu/TS-1-M catalyst. Meanwhile, the binding energies of the Cu + and Cu 2+ species on the Cu/HZSM-5-M catalyst are lower than those on Cu/TS-1-M catalyst. This could be due to the fact that the metal-support interaction on the Cu/HZSM-5-M is stronger than Cu/TS-1-M. In addition, the content of the Cu + species is higher than Cu 2+ species on both of Cu/HZSM-5-M and Cu/TS-1-M catalysts by XPS analysis (Table S2).

Catalytic Performance
To optimize the reaction conditions, the hydroxysulfurization of styrene with diaryl disulfides was carried out with various oxidants and solvents under different temperatures (Table S3). Preliminary solvent screening experimental results show that dimethylsulfoxide (DMSO)/H2O was the effective mixture solvent in the presence of iodine as oxidant at 80 °C, affording styrene conversion of 89% and 1-phenyl-2-(phenylthio)ethanol product selectivity of 63% (entries 1-6). After

Catalytic Performance
To optimize the reaction conditions, the hydroxysulfurization of styrene with diaryl disulfides was carried out with various oxidants and solvents under different temperatures (Table S3). Preliminary solvent screening experimental results show that dimethylsulfoxide (DMSO)/H2O was the effective mixture solvent in the presence of iodine as oxidant at 80 °C, affording styrene conversion of 89% and 1-phenyl-2-(phenylthio)ethanol product selectivity of 63% (entries 1-6). After

Catalytic Performance
To optimize the reaction conditions, the hydroxysulfurization of styrene with diaryl disulfides was carried out with various oxidants and solvents under different temperatures (Table S3). Preliminary solvent screening experimental results show that dimethylsulfoxide (DMSO)/H 2 O was the effective mixture solvent in the presence of iodine as oxidant at 80 • C, affording styrene conversion of 89% and 1-phenyl-2-(phenylthio)ethanol product selectivity of 63% (entries 1-6). After designation of DMSO/H 2 O as solvent, the influence of oxidant on reaction activity was investigated. Compared to t-butylhydroperoxide (TBHP) and H 2 O 2 , iodine proved to be the most efficient oxidant (entries 7 and 8). When using O 2 , K 2 S 2 O 8 , and KMnO 4 as oxidants, this reaction did not occur (entries 9-11). By optimization of the reaction temperature, it was found that the highest styrene conversion and the product selectivity at 80 • C were obtained (entries 12-15). Consequently, the reaction conditions were determined and followed as: styrene (1.0 mmol), diaryl disulfides (0.6 mmol), 0.2 mmol iodine, DMSO/H 2 O (1:1) as solvent, temperature of 80 • C. The good reaction activity was obtained by using iodine as an oxidant, which could be due to fact that iodine can promote the formation of sulfonium ions from dibenzyl disulfide [20].
The catalytic performance of different catalysts was performed at the optimized reaction conditions, and the results are shown in Table 2. Initially, acidic HZSM-5-M shows the highest reaction activity and 1-phenyl-2-(phenylthio)ethanol selectivity, as compared to mesopore-free HZSM-5 and acid-free TS-1-M catalysts (entries 1-4). These results suggest that the catalyst with acidity favors this reaction. Compared with HZSM-5-M, the product selectivity is further improved on the Cu/HZSM-5-M catalyst (entries 2 and 5). The catalytic performance of the Cu/HZSM-5-M catalyst is also superior to that of Fe/HZSM-5-M and Co/HZSM-5-M catalysts (entries 5-7). Notably, although Cu/HZSM-5 catalyst gives similar styrene conversion to that Cu/HZSM-5-M catalyst, the product selectivity over Cu/HZSM-5 is lower than that over Cu/HZSM-5-M (entry 8). This could be due to the difference in porous structure between Cu/HZSM-5 and Cu/HZSM-5-M catalysts. Cu/HZSM-5-M has a high mesoporous surface area of 182 m 2 /g and mesoporous volume of 0.35 cm 3 /g (Table S1). In contrast, Cu/HZSM-5 has only a low external area of 27 m 2 /g. The abundant mesopores in Cu/HZSM-5-M not only could be beneficial to the reactants accessible for active sites, but also favor the diffusion of the reactants, enhancing product selectivity. In addition, the acid-base property of the support strongly influences the reaction activity of their supported Cu catalysts. ETS-10 has strong basicity [13], and the Cu/ETS-10 catalyst only gives styrene conversion of 71% (entry 9), even lower than the reaction system without catalyst, suggesting that the catalyst with basicity inhibits this reaction. Acidic-free TS-1-M supported Cu catalyst (Cu/TS-1-M) presents comparable activity to that Cu/HZSM-5-M, but 1-phenyl-2-(phenylthio)ethanol product selectivity of Cu/TS-1-M (76%) is inferior to that of Cu/HZSM-5-M (84%, entry 10). designation of DMSO/H2O as solvent, the influence of oxidant on reaction activity was investigated. Compared to t-butylhydroperoxide (TBHP) and H2O2, iodine proved to be the most efficient oxidant (entries 7 and 8). When using O2, K2S2O8, and KMnO4 as oxidants, this reaction did not occur (entries 9-11). By optimization of the reaction temperature, it was found that the highest styrene conversion and the product selectivity at 80 °C were obtained (entries [12][13][14][15]. Consequently, the reaction conditions were determined and followed as: styrene (1.0 mmol), diaryl disulfides (0.6 mmol), 0.2 mmol iodine, DMSO/H2O (1:1) as solvent, temperature of 80 °C. The good reaction activity was obtained by using iodine as an oxidant, which could be due to fact that iodine can promote the formation of sulfonium ions from dibenzyl disulfide [20]. The catalytic performance of different catalysts was performed at the optimized reaction conditions, and the results are shown in Table 2. Initially, acidic HZSM-5-M shows the highest reaction activity and 1-phenyl-2-(phenylthio)ethanol selectivity, as compared to mesopore-free HZSM-5 and acid-free TS-1-M catalysts (entries 1-4). These results suggest that the catalyst with acidity favors this reaction. Compared with HZSM-5-M, the product selectivity is further improved on the Cu/HZSM-5-M catalyst (entries 2 and 5). The catalytic performance of the Cu/HZSM-5-M catalyst is also superior to that of Fe/HZSM-5-M and Co/HZSM-5-M catalysts (entries 5-7). Notably, although Cu/HZSM-5 catalyst gives similar styrene conversion to that Cu/HZSM-5-M catalyst, the product selectivity over Cu/HZSM-5 is lower than that over Cu/HZSM-5-M (entry 8). This could be due to the difference in porous structure between Cu/HZSM-5 and Cu/HZSM-5-M catalysts. Cu/HZSM-5-M has a high mesoporous surface area of 182 m 2 /g and mesoporous volume of 0.35 cm 3 /g (Table S1). In contrast, Cu/HZSM-5 has only a low external area of 27 m 2 /g. The abundant mesopores in Cu/HZSM-5-M not only could be beneficial to the reactants accessible for active sites, but also favor the diffusion of the reactants, enhancing product selectivity. In addition, the acid-base property of the support strongly influences the reaction activity of their supported Cu catalysts. ETS-10 has strong basicity [13], and the Cu/ETS-10 catalyst only gives styrene conversion of 71% (entry 9), even lower than the reaction system without catalyst, suggesting that the catalyst with basicity inhibits this reaction. Acidic-free TS-1-M supported Cu catalyst (Cu/TS-1-M) presents comparable activity to that Cu/HZSM-5-M, but 1-phenyl-2-(phenylthio)ethanol product selectivity of Cu/TS-1-M (76%) is inferior to that of Cu/HZSM-5-M (84%, entry 10). Based on our experiment result, it can be concluded that the Cu species and acidic sites on Cu/HZSM-5-M catalyst could enhance the catalytic performance. Our previous work demonstrated that acidic sites on zeolite can promote the adsorption of styrene through interaction of C=C bond with the acidic sites, resulting in the activation of the C=C bond, and the activated C=C bond readily was attacked by electrophilic species to form the desired product [15]. In this work, compared with acid-free TS-1-M supported Cu catalyst, large amounts of acidic sites on Cu/HZSM-5-M catalyst could benefit the adsorption of styrenes, improving the reaction performance in the hydroxysulfurization reaction of styrenes. On the other hand, the Cu + and Cu 2+ species in the catalyst could play an important role in this reaction. It has been reported that Cu salts acted on the disulfide as a Lewis acid or co-oxidant in air to give electrophilic sulfur species [8]. In our case, Cu + and Cu 2+ species in the catalyst could also facilitate the formation of electrophilic sulfur species [8], which could attack the styrene to form the target product.
The reaction scope of this reaction over Cu/HZSM-5-M catalyst was also examined, and the results are given in Table 3. Cu/HZSM-5-M catalyst tolerates styrenes with electron-donating (methyl and t-butyl) and electron-withdrawing (fluorine, chlorine, and bromine) substituents, affording the desired products in good yields (3b-3i). The substrate of 2-naphthylethylene can also be employed in this transformation, giving a relatively low yield (3j). Furthermore, employing propenyl benzene as a substrate, it affords the desired product 3k in a gratifying yield. Additionally, diaryl disulfides containing nitro and bromine substituents were smoothly reacted with p-methylstyrene, and a moderate yield was obtained with the expected products (3l and 3m). Moreover, using cyclic aliphatic alkene and diaryl disulfides as substrates, the reaction still smoothly proceeded and desired product 3n in good yield. Notably, when the reagent of 4-pentenoic acid with internal nucleophile was employed as substrate, the target product of 2-((phenylthio)methyl)tetrahydrofuran 3o also was obtained. These results demonstrated that the Cu/HZSM-5-M catalyst presents good functional group compatibility in hydroxysulfurization reaction. Based on our experiment result, it can be concluded that the Cu species and acidic sites on Cu/HZSM-5-M catalyst could enhance the catalytic performance. Our previous work demonstrated that acidic sites on zeolite can promote the adsorption of styrene through interaction of C=C bond with the acidic sites, resulting in the activation of the C=C bond, and the activated C=C bond readily was attacked by electrophilic species to form the desired product [15]. In this work, compared with acid-free TS-1-M supported Cu catalyst, large amounts of acidic sites on Cu/HZSM-5-M catalyst could benefit the adsorption of styrenes, improving the reaction performance in the hydroxysulfurization reaction of styrenes. On the other hand, the Cu + and Cu 2+ species in the catalyst could play an important role in this reaction. It has been reported that Cu salts acted on the disulfide as a Lewis acid or co-oxidant in air to give electrophilic sulfur species [8]. In our case, Cu + and Cu 2+ species in the catalyst could also facilitate the formation of electrophilic sulfur species [8], which could attack the styrene to form the target product.
The reaction scope of this reaction over Cu/HZSM-5-M catalyst was also examined, and the results are given in Table 3. Cu/HZSM-5-M catalyst tolerates styrenes with electron-donating (methyl and t-butyl) and electron-withdrawing (fluorine, chlorine, and bromine) substituents, affording the desired products in good yields (3b-3i). The substrate of 2-naphthylethylene can also be employed in this transformation, giving a relatively low yield (3j). Furthermore, employing propenyl benzene as a substrate, it affords the desired product 3k in a gratifying yield. Additionally, diaryl disulfides containing nitro and bromine substituents were smoothly reacted with p-methylstyrene, and a moderate yield was obtained with the expected products (3l and 3m). Moreover, using cyclic aliphatic alkene and diaryl disulfides as substrates, the reaction still smoothly proceeded and desired product 3n in good yield. Notably, when the reagent of 4-pentenoic acid with internal nucleophile was employed as substrate, the target product of 2-((phenylthio)methyl)tetrahydrofuran 3o also was obtained. These results demonstrated that the Cu/HZSM-5-M catalyst presents good functional group compatibility in hydroxysulfurization reaction. Based on our experiment result, it can be concluded that the Cu species and acidic sites on Cu/HZSM-5-M catalyst could enhance the catalytic performance. Our previous work demonstrated that acidic sites on zeolite can promote the adsorption of styrene through interaction of C=C bond with the acidic sites, resulting in the activation of the C=C bond, and the activated C=C bond readily was attacked by electrophilic species to form the desired product [15]. In this work, compared with acid-free TS-1-M supported Cu catalyst, large amounts of acidic sites on Cu/HZSM-5-M catalyst could benefit the adsorption of styrenes, improving the reaction performance in the hydroxysulfurization reaction of styrenes. On the other hand, the Cu + and Cu 2+ species in the catalyst could play an important role in this reaction. It has been reported that Cu salts acted on the disulfide as a Lewis acid or co-oxidant in air to give electrophilic sulfur species [8]. In our case, Cu + and Cu 2+ species in the catalyst could also facilitate the formation of electrophilic sulfur species [8], which could attack the styrene to form the target product.
The reaction scope of this reaction over Cu/HZSM-5-M catalyst was also examined, and the results are given in Table 3. Cu/HZSM-5-M catalyst tolerates styrenes with electron-donating (methyl and t-butyl) and electron-withdrawing (fluorine, chlorine, and bromine) substituents, affording the desired products in good yields (3b-3i). The substrate of 2-naphthylethylene can also be employed in this transformation, giving a relatively low yield (3j). Furthermore, employing propenyl benzene as a substrate, it affords the desired product 3k in a gratifying yield. Additionally, diaryl disulfides containing nitro and bromine substituents were smoothly reacted with p-methylstyrene, and a moderate yield was obtained with the expected products (3l and 3m). Moreover, using cyclic aliphatic alkene and diaryl disulfides as substrates, the reaction still smoothly proceeded and desired product 3n in good yield. Notably, when the reagent of 4-pentenoic acid with internal nucleophile was employed as substrate, the target product of 2-((phenylthio)methyl)tetrahydrofuran 3o also was obtained. These results demonstrated that the Cu/HZSM-5-M catalyst presents good functional group compatibility in hydroxysulfurization reaction. Table 3. Hydroxysulfurization reaction between alkenes and diaryl disulfides 1 .

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The reusable ability of Cu/HZSM-5-M catalyst was investigated (Table 4). Cu/HZSM-5-M catalyst exhibits relatively high activity and selectivity after it recycled seventh runs, nevertheless, the activity and product selectivity of Cu/HZSM-5-M were slightly reduced with an increase cycle times. This could be due to the fact that the leaching of Cu species in the Cu/HZSM-5-M catalyst occurred. When the Cu/HZSM-5-M was recycled seven times, the Cu content in the catalyst decreased from 3.0% for fresh one to 2.7 wt. % (Table S1). The reused Cu/HZSM-5-M catalyst was also characterized by TEM, XRD, and N 2 -adsorption. TEM image shows that the metal particles are still present on the reused Cu/HZSM-5-M sample ( Figure S4). The characteristic diffraction peaks in XRD pattern of the reused Cu/HZSM-5-M are the same as that of the fresh one ( Figure S5). The reused Cu/HZSM-5-M catalyst has high BET surface area (354 m 2 /g), external surface area (175 m 2 /g), and mesoporous volume (0.33 cm 3 /g, Table S1). These results suggest that Cu/HZSM-5-M exhibits good physico-chemical stability.

Conclusions
In conclusion, hierarchically porous zeolite ZSM-5 with cylinder-like morphology and micromeso-macroporous structure was synthesized by using cationic copolymer as mesoscale template. After loading metal Cu on the H-form ZSM-5-M, the obtained Cu/HZSM-5-M presents good catalytic performance in the hydroxysulfurization of styrenes with diaryl disulfides, as compared to acidic micropore ZSM-5, acid-free TS-1-M, and basic ETS-10 supported Cu catalysts. This feature should be attributed to the fact that numerous acidic sites and Cu + and Cu 2+ species in Cu/HZSM-5-M catalyst play a synergistic effect in improving the reaction activity and product selectivity. In addition, the prepared Cu/HZSM-5-M catalyst tolerates a variety of functional groups on both the styrenes and disulphide substrates, and has good reusability.

Conclusions
In conclusion, hierarchically porous zeolite ZSM-5 with cylinder-like morphology and micro-mesomacroporous structure was synthesized by using cationic copolymer as mesoscale template. After loading metal Cu on the H-form ZSM-5-M, the obtained Cu/HZSM-5-M presents good catalytic performance in the hydroxysulfurization of styrenes with diaryl disulfides, as compared to acidic micropore ZSM-5, acid-free TS-1-M, and basic ETS-10 supported Cu catalysts. This feature should be attributed to the fact that numerous acidic sites and Cu + and Cu 2+ species in Cu/HZSM-5-M catalyst play a synergistic effect in improving the reaction activity and product selectivity. In addition, the prepared Cu/HZSM-5-M catalyst tolerates a variety of functional groups on both the styrenes and disulphide substrates, and has good reusability.  (Table S1).

Catalyst Characterization
XRD patterns of ZSM-5-M and HZSM-5-M in Figure 1a give diffraction peaks at 2θ = 7.9°, 8.9°, 23°, 23.9°, and 24.5°, which is typical characteristics of ZSM-5 zeolite structure [15]. After loading of Cu on HZSM-5-M and calcination, the XRD diffraction peak position and intensity did not change, indicating that the ZSM-5 zeolite structure is well maintained for the Cu/HZSM-5-M sample. The diffraction peaks related with Cu species are not observed in the XRD pattern of Cu/HZSM-5-M, suggesting that small metal particles are dispersed in the Cu/HZSM-5-M sample. Similar phenomena were also observed in XRD patterns of TS-1-M and basic ETS-10 supported Cu catalysts ( Figure S1). Nitrogen adsorption-desorption isotherms of ZSM-5-M and Cu/HZSM-5-M samples give a steep step at relative pressure of 0.6-0.96 (Figure 1b), which is related to the presence of mesopores in the samples. Their corresponding mesopore size mainly centered at 22 and 21 nm ( Figure S2), respectively.  Figure 2a shows the SEM image of ZSM-5-M, giving a cylinder-like morphology with rough surface. The large cylinder-like particles are composed of nano-crystals with sizes of 50-150 nm. In this case, meso-macropores could be formed in the nanocrystal assemblies. The morphology of the TS-1-M, ZSM-5, and ETS-10 zeolites were also observed by SEM technique, and the results are shown in Figure S3. The SEM image reveals that the TS-1-M crystal particle exhibits a rough surface and has a particle size of 200-300 nm, while both of ZSM-5 and ETS-10 zeolite have a smooth surface with a large particle size.
The porous structure of the ZSM-5-M was characterized by TEM technique. It was observed that not only many intra-crystalline mesopores (white lines), but also abundant inter-crystalline mesopore and marcopores (light areas), are present in ZSM-5-M particles (Figure 2b).
The dispersion of metal partials on Cu/HZSM-5-M was observed by TEM technique, and the  Table S1: Texture parameters of the different samples; Table S2: The results of deconvolution of XPS Cu2p3/2 peak of Cu/HZSM-5-M and Cu/TS-1-M samples; Table S3: Optimization of reaction conditions.