- 1Key Laboratory of Coal Processing and Efficient Utilization of Ministry of Ministry of Education, Xuzhou, China
- 2School of Chemical Engineering and Technology, China University of Mining and Technology, Xuzhou, China
b-oriented ZSM-5 zeolite film was synthesized on the macropore α-quartz substrate modified with titanium dioxide (TiO2), polyvinyl acetate (PVA), and chitosan (CTS) by hydrothermal crystallization. By comparing the binding energy and b-oriented angle of zeolite film on each modified α-quartz substrate, the orientations, and combinations derived from structure-adsorption relationship were investigated with Material Studio simulation. Furthermore, the effects of calcination temperature and ultraviolet (UV) irradiation time on the surface structure and adsorption activity of TiO2 coating were studied. The increase adsorption potential energy and the formation of Ti-O-Si bind between zeolite crystal phase and substrate facilitate the continuous and uniform zeolite film growth. The TiO2 interlayer with anatase phase after UV irradiation presents a smooth surface with high Ti-OH density, consequently to high selectivity of b-orientation growth for the ZSM-5 crystals. Compared with the traditional ZSM-5, the higher stability has been exhibited with b-oriented ZSM-5 film /TiO2/α-quartz in the MTA reaction, and the methanol conversion and BTX selectivity remained higher than 90 and 70%, after 6 h reaction.
Highlights
- The b-oriented ZSM-5 zeolite film was prepared on the substrate of modified α-quartz.
- The modification-structure-adsorption relationship of modifiers and α-quartz surface were investigated.
- The orientations and combinations derived from structures and adsorption between modified α-quartz and ZSM-5-crystallites were studied.
Introduction
Aromatic hydrocarbons, especially light aromatic hydrocarbons such as benzene, toluene, and xylene (BTX) are important raw materials for organic chemicals and polymer industry (Ye et al., 2019). The production of light aromatic hydrocarbons BTX by methanol conversion (MTA) is of great significance to realize the low-cost synthesis of value-added chemicals via non-oil routes and to expand the application of methanol (Ali et al., 2015; Bozzano and Manenti, 2016; Mitsuyoshi et al., 2017).
At present, some MTA studies are reported and the main reaction catalysts are ZSM-5 (Na et al., 2018), ZSM-22 (Catizzone et al., 2017), MCM-22 (Lacarriere et al., 2011), MCM-36 (Lacarriere et al., 2011), and H-Beta molecular sieve (Svelle et al., 1999) etc. ZSM-5 exhibits excellent shape-selectivity catalysis for BTX aromatic hydrocarbons due to the suitable diameter of the tunnel, therefore it becomes the most widely studied catalyst for MTA reaction (Li et al., 2003; Khodakov et al., 2010). However, aromatic hydrocarbon selectivity and carbon deposition on ZSM-5 remain as the core issues which make it difficult to scale-up for MTA industry deployment.
Significant efforts have been attempted to address the carbon deposition issue on catalysts during MTA reaction, for example, some studies have proposed to synthesize nanometer acicular c-axis ZSM-5 catalyst (Shen et al., 2013). The length of the main reaction channel of a, b orientation is in favor of strengthen the diffusion process, thereby suppresses carbon deposition. For example, Shen et al. (2013, 2014). Used acid-treatment to slowly dissolve the aluminum and silicon from natural dolomite, and formed the Al–Si–O structural unit in the catalyst synthesis. Without directing agent, the Al-Si-O structural unit was self-assembled and crystallized into a ZSM-5 acicular nanometer powder along c-axis, The MTA reactivity of this acicular ZSM-5 nanoparticles was evaluated and it is found that the reaction molecules were able to rapidly diffuse through the micropores in the short axes of a and b, thus the diffusion limit is lowered. Compared with the traditional non-b-oriented ZSM-5, the residence time of the reaction molecules in the pores of this novel materials is shortened, therefore the carbon deposition on the catalyst is significantly reduced, which contributes to the prolonged catalyst life and improved BTX selectivity. However, the study also found that the crystals of acicular molecular sieves are so brittle, which limits their industrial application due to the difficulties for storage and transportation.
To solve above-mentioned issues, our group proposed to utilize the adsorption and diffusion advantages of ZSM-5 in the b-oriented straight channel (Lai et al., 2010; Zhou et al., 2013). The b-oriented ZSM-5 one-dimensional molecular sieve was loaded on the nanospheres with mesoporous pore structure to construct the b-oriented ZSM-5 nanosphere shell material with micro-mesoporous pore structure. The micropores of the material will become the active center of the MTA catalyst with excellent carbon deposition resistance and BTX selectivity, meanwhile the mesopores work as fast channels for the diffusion of aromatic BTX small molecules.
It was found that the pore structure and surface activity of the substrate exhibit significant effects on film orientation and adhesion strength (Wei and Yen, 2007). Therefore, to improve the binding force between the crystal nucleus and the substrate surface, some attempts are made to increase the surface activity and adsorption strength of the substrate by employing suitable coupling agents or modifiers. For example, Lee et al. (2000b) used 3-Aminopropyltriethoxysilane and 3-Glycidoxypropyltrimethoxysilane as coupling agents to synthesize the ZSM-5 with a great b-oriented crystal layer on the glass surface. In addition, this repeatable synthesis of the molecular sieve onto the substrate was demonstrated by similar mechanism (Lee et al., 2000a, 2001; Park et al., 2002; Jin et al., 2006). Yeung et al. (Jlh et al., 2000) assembled randomly oriented silicalite-1 molecular sieves on the surface of stainless steel. Fu et al. (2018) prepared a silicalite-1 molecular sieve onto the ceramic surface by manual assembly method, and obtained dense seed layer of b-oriented crystals. However, due to the lack of fundamental understanding, the research is still mainly in the sample screening stage with different substrates and modifiers via trail-and-error approach. Different from other chemical processes, the surface of the colloidal microspheres is not destroyed during the loading of the crystal nucleus on the surface of the substrate. The nanocrystal nucleus firstly adsorbs on the colloidal microsphere surface, whose structure and properties can then affect the formation process of ZSM-5 crystal nuclei. Therefore, the surface structure and properties of colloidal microspheres were introduced and investigated in the molecular design and synthesis system of microspheres with core-shell structure. The effects of the surface structure of colloidal microspheres, as well as the surface properties of nanocrystal cores and modifier molecules were studied. To achieve the fundamental understanding of the directed growth of molecular sieve crystals, the effect of structural on the b-oriented adsorption of nanocrystal nuclei on the surface of colloidal microspheres was investigated. It is of important significance for both the theoretical and practical design of novel core-shell molecular sieve.
In addition, another goal of synthesis the b-oriented ZSM-5 zeolite is to increase the bonding force of the crystal nucleus on the substrate surface. The substrate materials with limited pore channels are reported in most present studies, which greatly restricts the application of molecular sieve film in separation and catalysis. Therefore, the design strategy to obtain monodisperse oriented molecular sieve film on the multi-channel substrate surface has become a challenging and important research topic in the field of oriented film materials.
Furthermore, as for the preparation of b-oriented ZSM-5 zeolite film on the surface of macropore substrate, the influencing factors of the oriented growth and assembly of nanocrystalline core are regarded as the essential points for the preparation process. In this paper, a series of ZSM-5 zeolite films anchoring on the α-quartz substrate surface will be synthesized by hydrothermal crystallization. Both organic (polyvinyl acetate and chitosan) and inorganic (titanium dioxide) modifiers are applied to coat on the prepared samples. Considering the macropore α-quartz substrate, the effects of substrate surface structure and adsorption activity on the b-oriented adsorption of nanocrystal nuclei will be investigated.
Experimental Section
Simulation of Substrate Surface Modification and ZSM-5 Zeolite Combination Process
The inorganic modifier titanium dioxide (TiO2) and organic modifier polyvinyl acetate (PVA) and chitosan (CTS) were modeled by 3Dviewer in Material Studio software. In order to make the simulation conditions close to the molecular weight and polymerization degree of the organic modifier in the experiment, the polymerization degrees of PVA and CTS were set to 40 and 10 (Razmimanesh et al., 2015; Wei et al., 2017), respectively. The repeating unit of the TiO2 molecule was set to 100 (Baguer et al., 2009). The model is shown in Figure 1. Molecular dynamics simulation of the adsorption process of ZSM-5(010) crystal plane on the modified surface was performed under NVT system at 450 K, with a step size of 1 fs and simulation time of 1,000 ps using the Universal force field of Forcite module.
Figure 1. Schematic diagram of modifier model (a) Inorganic modifier TiO2, (b) grid structure organic modifier PVA, and (c) linear organic modifier CTS (Gray, white, red, and green represent C, H, O, and Ti, respectively).
Substrate Surface Modification Experiment
The surface of the substrate was modified by inorganic modifier (TiO2) and organic modifier (PVA and CTS). TiO2 (10wt.%, Hang Zhou Wan Jing new materials co., LTD.) precursor oxides sols were coated on the substrate surface by sol-gel method, and dried for 12 h at 50°C, then roasted for 2 h at 100oC. Chitosan (0.5 wt.%, Sinopharm Chemical Reagent Co., Ltd.) and PVA (4Wt.%, Sinopharm Chemical Reagent Co., Ltd.) were coated on the surface of the substrate for three times. It was dried at 30°C and 60% relative humidity for 12 h subsequently dried at 60°C for 2 h.
In order to study the effect of Ti-OH species and its concentration on the substrate surface of the supported ZSM-5 crystal layer, the samples substrate loaded with TiO2 coating was calcined in muffle furnace at 100, 300, 600, and 900oC, irradiated with UV for 2, 4, 6, and 8 h, respectively.
Preparation of b-Oriented ZSM-5 Zeolite Film
The ZSM-5 zeolite film was supported on the α-quartz substrate by hydrothermal synthesis. A prescribed amount of Tetrapropylammonium Hydroxide (TPAOH) (10 wt.%, Sinopharm Chemical Reagent Co., Ltd.) was added to the DI water followed by dropwise adding Ethyl Orthosilicate (TEOS) (Xiyu Chemical Co., Ltd.) and aluminum nitrate. Subsequently the mixture was aged for 24 h to obtain a clear and uniform solution. The synthesis mole composition was 0.32TPAOH: 1SiO2: 0.005Al2O3: 165H2O. The substrate was vertically inserted into a hydrothermal crystallization vessel with a Teflon liner, and the synthesis solution was added to the crystallization vessel without passing through the substrate. After heating to 165oC for 80 min, the obtained catalyst then is slowly rinsed for several times with DI water. Finally, the catalysts are calcinated at 550°C for 2 h in a tubular furnace with a heating rate of 0.5°C/min.
Characterizations
The microstructure of the modified substrate and the surface of the ZSM-5 film was characterized by scanning electron microscopy. Prior to the test, the sample was subjected to gold spray treatment. XRD data was obtained on a VERTEX 80v X-ray diffractometer using Cu Kα radiation (k = 0.15418 nm), scanning speed 2°/min, scanning range 5−50°, tube current and tube voltage of 150 mA, 40 kV, respectively. The contact angle was measured by the JC2000C4 contact angle meter and measured by a synthetic liquid solid drop method. Each contact angle was an average value of multiple measurements at different positions on the surface at room temperature. Nitrogen (N2) adsorption/desorption isotherms were measured with a physical adsorption instrument (ASAP2010) at −196°C. The textural properties of α-quartz substrate was determined by the high-performance automatic mercury intrusion meter (AutoPore IV 9510). The total pore volume (Vtotal) was derived from the amount of N2 adsorbed at p/p0 = 0.99, the BET method was applied to determine the total surface area (Stotal), the t-plot method is specifically used to identify micropores, and the BJH method was used to estimate the size distribution.
The Catalytic Activity and Selectivity of ZSM-5 Zeolite in MTA Reaction
The catalytic activity and selectivity in MTA reaction were studied in a fixed-bed reactor. 0.5 g of catalyst was carried out in a reaction tube with an inner diameter of 10 mm, the catalyst was activated for 2 h at 450°C, and the methanol was introduced at a space velocity (WHSV) of 2.85 h−1 under normal pressure at 470°C, the concentration of the components was analyzed using a gas chromatograph.
Results and Discussion
Effect of Modifier Species on Preparation of b-Oriented ZSM-5 Zeolite Film
Characterization of ZSM-5 Zeolite Film: Composition, Morphology
In this paper, TiO2, PVA, and CTS coatings were used to modify the surface of macropore α-quartz substrate, and the addition of intermediate oxide layer, to change the directional growth of ZSM-5 zeolite film on the substrate. Figure 2 shows the XRD patterns of ZSM-5 zeolite film with various coatings. There are five diffraction peaks at 2θ = 8.89°, 17.81°, 26.82°, 36.06°, and 45.46°, attributed to the (020), (040), (060), (080), and (0100) crystal faces of MFI zeolite. The results indicate that ZSM-5 zeolite film with b-oriented crystals perpendicular to the substrate surface was formed. Compared with the other three modifiers, Figure 2B (0h0) shows the strongest diffraction peak intensity, implying the TiO2 is more favorable for the growth of b-oriented ZSM-5 zeolite film. In addition, the uncoated substrate exhibits a weak characteristic peak at 2θ = 23.3° (Figure 2A), attributed to the (501) crystal plane which was identified as ZSM-5 in the a-axis (Chu et al., 2016), indicating the presence of the small amount of a-axis crystals.
Figure 2. XRD patterns of ZSM-5 zeolite film on (A) uncoated, (B) TiO2, (C) CTS, and (D) PVA coating.
Figure 3 shows SEM images of ZSM-5 zeolite film synthesized on the surface of substrates with different modifiers. Most of the ZSM-5 zeolite crystals grow in the b-orientation with coffin shape, and the effective TiO2 modification is clearly observed. Compared with the unmodified matrix (Figure 3A), others show that the ZSM-5 crystals increase significantly. This indicates that in the presence of the intermediate modification layer, the ZSM-5 molecular sieve nucleus can be more easily anchored and grown on the substrate, exhibiting higher coverage, and better film formation property. Moreover, the crystals on the substrate coated with organic modifiers (CTS and PVA) exhibit greater superposition and non-b-orientation than that with TiO2. Part of the ZSM-5 crystals are embedded in the intermediate modifier layer during growth, with the uneven crystals distribution and low coverage. Besides, the degree of orientation is inconsistent due to the difference in surface structure and adsorption activity between the surface of the ZSM-5 zeolite film and the substrate.
Substrate Surface Structure Analysis
It is found that the microstructure of the substrate is one of the important factors affecting the orientation growth of the crystal on the substrate. Figure 4 shows the SEM morphology of the substrates to analyze their microstructures with different coatings. The inorganic oxides in the nanosized particles can be effectively coated on flat surface (Figure 4B), in contrast the organic modifier film in a mesh or linear is tightly attached to form an uneven surface (Figures 4C,D), This observation indicates that the smooth nanocrystalline core-substrate interface promotes the growth of ZSM-5 zeolite film., Di et al. modified the surface of the smooth glass substrate by sol-gel method to obtain different surface coverages of silicalite-1 film (Di et al., 2011). Previous studies have shown that -OH-rich substrate with smooth surface does not own the effective adsorption through hydrogen bonding, and this may be cause by the structural differences between the surfaces of the material (Fu et al., 2018). We characterized a series of substrate materials (dispersed in deionized H2O) using ζ-potential measurements. It is found that both SiO2 and silicalite-1 exhibit negative surface charges, and the mixture of these two materials shows a −34.6 mV ζ-potential value, which lies between the values of their individual components, ζ-potential value of TiO2 is close to zero, revealing the weak interactions on adsorption. This electrostatic adsorption potential of smooth inorganic TiO2 surface results in the growth of ZSM-5 zeolite film. For organic modifiers, the film surface is positively charged and covered by large number of -OH and -NH2 active groups. In the meantime, the organic modifier is dehydrated during the coating process, the colloidal particles are aggregated due to the intermolecular force and chemical force, resulting in the uneven distribution of the surface active group on the matrix and different physical adsorptions. Thereby it further explains the degree of accumulation and aggregation of ZSM-5 crystals on the organic modifier surface.
Figure 4. SEM diagram of substrate coated with different modifiers (A) uncoated, (B) TiO2, (C) CTS, and (D) PVA.
Adsorption Activity
There is significant difference of the adsorption force (van der Waals force) between the modifier interface and the zeolite crystal phase (silica particles), this adsorption force can be characterized by non-zero frequency Hamaker constant Av>0 to evaluate the ability of various substrates to initiate surface gelation. According to the literature (Ji et al., 2012), the Hamaker constant Av>0 of SiO2-SiO2 and SiO2-TiO2 interaction are 0.35 × 10−20 and 3.1 × 10−20, respectively. The values suggest the silica–silica adsorption force is much weaker than silica–titanium adsorption force, which further explains that the poorer quality of the ZSM-5 film on substrate than that on TiO2 layer. According to the expressions and constants of the literature (Lai et al., 2000), we estimate the Hamaker constant Av>0 of SiO2-PVC and SiO2-CTS interaction are 1.82 × 10−20 and 1.53 × 10−20, respectively. By comparison, it is proved that the adsorption force of the substrate surface coated with TiO2 is obviously larger than that of the other modifiers. Thus, it can be concluded that the substrate with strong adsorption force is favorable for the loading of the crystals.
ZSM-5 was pre-planted in the b-direction on the surface of TiO2, CTS, and PVA coated substrates, the orientation angle are 43.19, 53.82, and 88.42° (Table 1), respectively, indicating that the orientation angles of ZSM-5 grown on the modifier in the b-orientation decreases in the order: TiO2 > CTS > PVA. The CTS and PVA are rich in -OH groups and -NH2 groups, which can generate hydrogen bonds at the interface between ZSM-5 and the substrate, thereby generating interaction forces. However, with the help of kinetic simulation in Figures 5C,D, it is found that although there is a strong interaction between macromolecules of CTS/PVA and the substrates, a small range of cross-linking or agglomeration will occur on the surface of the substrates. Therefore, the exposed surfaces of the CTS and PVA modifiers are always accompanied by a slight roughness, resulting in a certain inclination angle. As shown in Figure 5A, when the ZSM-5 coated with TiO2 modification on the substrate for the plant, ZSM-5 embedded in the modified layer with b-orientation. As small molecule, TiO2 does not agglomerate on the surface of the substrate, meanwhile a strong interaction force can be maintained between TiO2 molecules, thereby a dense and uniform modification layer can be formed on the substrate. Further, stable Ti-O-Si bond was formed due to the interaction between Ti-OH with Si-OH, which facilitated the ZSM-5 embedded in the TiO2 modified layer. However, the Si-O-Si bond was not formed at the uncoated substrate effectively, and the van der Waals force becomes the main adsorption force in the interfaces, resulting in failure to form an effective pre-planted (Figure 5B). Consequently, the b-oriented ZSM-5 is best pre-planted on the substrate coated by TiO2.
Table 1. Adsorption characteristics of ZSM-5 nanocrystalline crystal (010) surface and modifier surface/substrate.
Figure 5. Adsorption simulation of ZSM-5 nanometer crystal (010) on the surface of modifier (A) substrate, (B) TiO2, (C) CTS, and (D) PVA.
Meanwhile, even though the TiO2 modifier can provide the great b-oriented angle and maximum interaction energy, the Figure 3B shows that the ZSM-5 zeolite film still has a small amount of non-b-orientation ones, which may be caused by the differences in the species and density of -OH groups on the substrate surface. Moreover, the layer of TiO2 was modified to study the effect of Ti-OH species and their density on the crystal orientation as well as surface coverage of ZSM-5 zeolite film.
Effect of TiO2 Coating on Preparation of b-Oriented ZSM-5 Zeolite Film
Temperature of Calcination
The Ti-OH species on the substrate surface can be altered by calcining the TiO2/substrate. Figure 6 shows the XRD results, pure anatase peaks appear at 2θ = 25.4, 37.8, and 48.0° at 100°C, and the characteristic peak intensity increases with temperature. At 900°C, the diffraction peak is sharp and symmetrical, and the half-width β is narrowed. The crystal form of titanium oxide changes from anatase to rutile with increasing temperature (Liu et al., 2012; Mashimo et al., 2017). Anatase and rutile Ti-OH are more hydrophilic than Ti-OH in mixed crystalline form. The seeds of anatase and rutile TiO2 with strong hydrophilicity grow along high b-orientation, and the distribution of crystals on anatase TiO2 is very uniform (Figures 7A,B). The thermal treatment is capable of changing the crystal structure of TiO2, resulting in various Ti-OH species and different water molecules adsorption mechanisms. The mixed crystal phase (including anatase- and rutile-TiO2) is low hydrophilic, and when the temperature rises to 300°C, the intermolecular adsorption mode is converted from non-dissociative adsorption to dissociative adsorption. The TiO2 intermolecular force is reduced and partially dissociated, causing a relatively sparse density of TiO2 coating on the surface of the substrate. Eventually, the amount of anatase-type Ti-OH is reduced, resulting in partial nucleation to grow along non-b-orientation (Figures 7C,D).
Figure 7. SEM images of ZSM-5 zeolite film on TiO2 coating calcine under (A) 100°C, (B) 300°C, (C) 600°C, and (D) 900°C.
Time of UV Irradiation
The effect of surface Ti-OH density on the crystal orientation of ZSM-5 zeolite film is investigated in this section. According to research reports, the hydrophilicity of TiO2 films can be tuned by photocatalysis (Mohamad et al., 2015; Barbieriková et al., 2018). In detail, the Ti-OH concentration on the substrate surface was adjusted by irradiating the substrate with ultraviolet light (Wu et al., 2012; Lian and Park, 2016). With the increased UV treatment time, the contact angle of the TiO2 coating is gradually reduced, inferring the ultraviolet light irradiation can enhance the hydroxyl concentration on the substrate. Figure 8 shows the contact angle is the smallest when irradiated for 2 h, namely, the hydrophilicity of the substrate is the strongest. TiO2 is firstly excited by photons to generate hole-electron pairs (h+ and e−) (Equation 1), then the bridge oxygen and the positively charged holes (h+) react on the surface to cause the breakage of Ti-O bond, and later the bridge oxygens leave the surface to generate oxygen vacancies (Equation 2). At the same time, in order to maintain the surface electrical neutrality, Ti4+ is reduced to Ti3+(Equation 3), and then the water molecules enter the oxygen vacancy and react to form an adsorbed hydroxyl group (Equation 4). This reaction process can be expressed by the following equations:
Figure 9 shows SEM morphology of the crystal layer synthesized on the TiO2 coating irradiated by ultraviolet light at different times. As it can be seen from the figure, the zeolite film is highly uniform with b-orientation on the substrate. When the irradiation time reaches 8 h, a small part of the seed crystal grows on the substrate in the non-b- oriented direction. The extra irradiation results in a decrease in the hydroxyl concentration on the surface of the substrate (Ehhalt and Rohrer, 2000). From Figure 3B, the surface seed crystals without ultraviolet treatment are evenly distributed, but the crystals are not dense enough. In contrast, from Figure 9A, it is found that the crystals on the surface of the substrate are uniformly and densely formed after treated by 2 h ultraviolet irradiation. From Figure 8, it can be seen that under the condition of ultraviolet light irradiation for 2 h, the contact angle is the smallest and the surface hydrophilicity is the strongest, which greatly enhances the Ti-OH concentration and makes the b-oriented ZSM-5 crystal growth denser.
Figure 8. The relationship of UV irradiation time and the contact angles of synthesis solution droplets on TiO2 coated substrate.
Figure 9. SEM images of ZSM-5 zeolite film on TiO2 coated substrate after UV irradiation for (A) 2 h, (B) 4 h, (C) 6 h, and (D) 8 h.
In summary, surface structure and adsorption activity play a crucial role in the orientation and combination of ZSM-5 zeolite film. The introduction of TiO2 modification layer provides a great substrate-modification growth interface for ZSM-5 crystal, and enhances the adsorption activity on the substrate and promotes the b-oriented growth of the ZSM-5 zeolite film.
Textural Properties and Catalytic Performance of ZSM-5/TiO2/α-Quartz Zeolite
Textural Properties
The change in porosity of the ZSM-5/TiO2/α-quartz zeolite (FC) was confirmed by nitrogen adsorption and desorption, Table 2 summarizes the textural properties of the ZSM-5 zeolite before and after loading onto α-quartz substrate, a wide peak (centered around 103 nm) was observed clearly (Figure 10A), The macroporous α-quartz substrate provides a low-resistance mass transfer channel for the raw reactants and products. The FC zeolite exhibits a type IV nitrogen adsorption-desorption isotherm with a low uptake at low relative pressures (Figure 10B), which is consistent with the presence of micropores. And the ZSM-5 pore size distribution agrees with it (Figure 10C). At the same time, there is a typical H4 hysteresis loop in the isotherm at high relative pressure, which is the result of the adsorption and desorption of N2 in the mesoporous (Han and Liu, 2015; Chu et al., 2016). During the preparation of FC zeolite, the specific surface area (Stotal) and micropore volume (Vmicro) have different degrees of reduction, but the mesoporous specific surface area (Smeso) and mesopore volume (Vmeso) increased to 136.6 [m2 g−1], 0.3455 [m3 g−1], respectively, this can greatly facilitate the rapid diffusion of the product to the catalyst surface and reduce the formation of coke.
Figure 10. (A) Pore size distribution of α-quartz substrate, (B) N2 adsorption and desorption isotherm for FC zeolite, (C) Pore size distribution of ZSM-5 zeolite film.
Catalytic Performance
Figure 11 shows the methanol conversion and aromatics yield over ZSM-5 and FC zeolite with the reaction time in the MTA reaction. The methanol conversion was similar in the beginning of the reaction, however, after 6 h, the methanol conversion over ZSM-5 was rapidly decreased to 68%, while a slight decrease was observed over b-oriented ZSM-5. Meantime, the aromatics yield over b-oriented ZSM-5 (71%) was much higher than ZSM-5 (40%). The FC zeolite shortens the diffusion path and reduces diffusion resistance for the methanol, alkanes, and aromatic hydrocarbons to rapidly diffuses to the catalyst surface by the mesoporous. However, the single microporous structure has a negative impact on the ZSM-5 catalytic process due to its extremely narrow and elongated micro-channel arrangement which limits mass transfer and facilitated coke formation (Groen et al., 2010; Chu et al., 2019). The introduction of TiO2 coating greatly promotes the formation of a dense and uniform b-oriented ZSM-5 zeolite film. The suitable pore structure ensures that the reactants and products in the pore is more conducive to the formation of BTX hydrocarbons, short residence time can reduce the degree of side reaction, thereby maintaining high catalytic activity and selectivity.
Conclusion
Hydrothermal crystallization method was used to prepare the b-oriented ZSM-5 zeolite film material on the macropore α-quartz substrate. The effects of surface structure and adsorption activity on b-oriented implanting of ZSM-5 nucleus on porous α-quartz substrates were investigated. Simulations of the loading process of ZSM-5 on different modified substrates with TiO2, PVA, CTS modifiers were carried out by Forcite module in Material Studio. And we obtained the b-oriented angle and adsorption potential energy though simulations. In the presence of TiO2 coating, the ζ-potential energy of the interface of TiO2-substrate is zero, forming stable Ti-O-Si bond and strong adsorption potential energy, it turns out to be the most beneficial to ZSM-5 zeolite film loading and growth along the b-orientation.
Moreover, the TiO2 coating is subjected to different calcination temperature and ultraviolet irradiation time. With 100°C calcination temperature and 2 h irradiation time, the Ti-OH concentration in the anatase crystal phase reaches the maximum. It is conclusive that the TiO2 coating provides a smooth nucleus-substrate growth interface for ZSM-5 zeolite film. Consequently, the interaction between the substrate surface and the ZSM-5 zeolite film is increased and the uniform distribution of the ZSM-5 zeolite film growing along the b-oriented direction is obtained.
Finally, we successfully prepared a FC zeolite with a suitable micro-mesoporous structure. it exhibits excellent catalytic activity and selectivity in MTA reactions and will be valuable material for further application.
Data Availability Statement
The datasets generated for this study are available on request to the corresponding author.
Author Contributions
All authors have contributed in various degrees to the analytical methods used, to the research concept, to the experiment design, to the acquisition of data, or analysis, and interpretation of data, to draft the manuscript or to revise it critically for important intellectual content.
Funding
This work was supported by the Fundamental Research Funds for the Central Universities (2017XKQY067).
Conflict of Interest
The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
References
Ali, K. A., Abdullah, A. Z., and Mohamed, A. R. (2015). Recent development in catalytic technologies for methanol synthesis from renewable sources: a critical review. Renew. Sust. Energ. Rev. 44, 508–518. doi: 10.1016/j.rser.2015.01.010
Baguer, N., Georgieva, V., Calderin, L., Todorov, L., Gils, S. V., and Bogaerts, A. (2009). Study of the nucleation and growth of TiO 2 and ZnO thin films by means of molecular dynamics simulations. J. Cryst. Growth. 311, 4034–4043. doi: 10.1016/j.jcrysgro.2009.06.034
Barbieriková, Z., PliŽingrová, E., Motlochová, M., Bezdička, P., Boháček, J., Dvoranová, D., et al. (2018). N-doped titanium dioxide nanosheets: preparation, characterization and UV/visible-light activity. Appl. Catal. B Environ. 232, 397–408. doi: 10.1016/j.apcatb.2018.03.053
Bozzano, G., and Manenti, F. (2016). Efficient methanol synthesis: perspectives, technologies and optimization strategies. Prog. Energ. Combust. Sci. 56, 71–105. doi: 10.1016/j.pecs.2016.06.001
Catizzone, E., Cirelli, Z., Aloise, A., Lanzafame, P., Migliori, M., and Giordano, G. (2017). Methanol conversion over ZSM-12, ZSM-22 and EU-1 zeolites: from DME to hydrocarbons production. Catal. Today 304, 39–50. doi: 10.1016/j.cattod.2017.08.037
Chu, R., Wang, J., Meng, X., Yu, S., Zhang, G., Wang, M., et al. (2019). Molecular simulation of hydrodesulfurization of coal tar using Pd/ZSM-5/γ-Al2O3 catalyst. Asia-Pacific J. Chem. Eng. 14:e2304. doi: 10.1002/apj.2304
Chu, R., Xu, T., Meng, X., Hou, W., and Miao, Z. (2016). Improved catalytic performance of C-axis oriented HZSM-5 nanobunches synthesized by re-aging. Catal. Lett. 146, 1965–1972. doi: 10.1007/s10562-016-1835-1
Chu, R. Z., Xu, T. T., Meng, X. L., and Wu, G. G. (2016). Mechanism of reaction of CeO2-CaO-Pd/HZSM5 catalyst in the syngas process in the presence of sulfurcontaining impurities. Prog. React. Kinet. Mech. 41, 1965–1972. doi: 10.3184/146867816X14702288640948
Di, J., Cong, Z., Yan, W., Wang, X., Yu, J., and Xu, R. (2011). Direct in situ crystallization of highly oriented silicalite-1 thin films on a surface sol–gel process modified substrate. Microporous Mesoporous Mater. 145, 104–107. doi: 10.1016/j.micromeso.2011.04.032
Ehhalt, D. H., and Rohrer, F. (2000). Dependence of the OH concentration on solar UV. J. Geophys. Res. 105, 3565–3571. doi: 10.1029/1999JD901070
Fu, D., Schmidt, J. E., Pletcher, P., Karakiliç, P., Ye, X., Vis, C. M., et al. (2018). Uniformly oriented zeolite ZSM-5 membranes with tunable wettability on a porous ceramic. Angew. Chem. Int. Edn. 57, 12458–12462. doi: 10.1002/anie.201806361
Groen, J. C., Peffer, L. A., Moulijn, J. A., and Pérez-Ramírez, J. (2010). Mechanism of hierarchical porosity development in MFI zeolites by desilication: the role of aluminium as a pore-directing agent. Chem. A Eur. J. 11, 4983–4994. doi: 10.1002/chem.200500045
Han, J., and Liu, D. (2015). Influence of synthesis conditions on the mesopore distribution and morphology control of hierarchical ZSM-5 zeolites synthesized by double-acyloxy organosilane surfactants. Eur. J. Inorg. Chem. 2015, 5081–5088. doi: 10.1002/ejic.201500735
Ji, M., Liu, G., Chen, C., Wang, L., and Zhang, X. (2012). Synthesis of highly b -oriented ZSM-5 membrane on a rough surface modified simply with TiO 2 by in situ crystallization. Microporous Mesoporous Mater. 155, 117–123. doi: 10.1016/j.micromeso.2011.12.037
Jin, S. P., Lee, G. S., and Yoon, K. B. (2006). Micropatterned monolayer assembly of zeolite microcrystals on glass by ionic linkages. Microporous Mesoporous Mater. 96, 1–8. doi: 10.1016/j.micromeso.2006.06.002
Jlh, C., Tellez, C., Yeung, K. L., and Ho, K. (2000). The role of surface chemistry in zeolite membrane formation. J. Membrane Sci. 164, 257–275. doi: 10.1016/S0376-7388(99)00214-8
Khodakov, A. Y., Chu, W., and Fongarland, P. (2010). Advances in the development of novel cobalt fischer—tropsch catalysts for synthesis of long-chain hydrocarbons and clean fuels. Chem. Rev. 38, 1692–1744. doi: 10.1002/chin.200733255
Lacarriere, A., Luck, F., Swierczynski, D., Fajula, F., and Hulea, V. (2011). Methanol to hydrocarbons over zeolites with MWW topology: effect of zeolite texture and acidity. Appl. Catal. A Gen. 402, 208–217. doi: 10.1016/j.apcata.2011.06.003
Lai, R., Yan, Y., and Gavalas, G. R. (2000). Growth of ZSM-5 films on alumina and other surfaces. Microporous Mesoporous Mater. 37, 9–19. doi: 10.1016/S1387-1811(99)00188-2
Lai, Z. P., Tsapatsis, M., and Nicolich, J. P. (2010). Siliceous ZSM-5 membranes by secondary growth of b-oriented seed layers. Adv. Funct. Mater. 14, 716–729. doi: 10.1002/adfm.200400040
Lee, G. S., Lee, Y. J., Choi, S. Y., Park, Y. S., and Yoon, K. B. (2000a). Self-assembly of β-glucosidase and d-glucose-tethering zeolite crystals into fibrous aggregates. J. Am. Chem. Soc. 122, 12151–12157. doi: 10.1021/ja0028222
Lee, G. S., Lee, Y. J., Ha, K., and Yoon, K. B. (2000b). Orientation-controlled monolayer assembly of zeolite crystals on glass using terephthaldicarboxaldehyde as a covalent linker. Tetrahedron 56, 6965–6968. doi: 10.1016/S0040-4020(00)00517-2
Lee, G. S., Lee, Y. J., and Yoon, K. B. (2001). Layer-by-Layer assembly of zeolite crystals on glass with polyelectrolytes as ionic linkers. J. Am. Chem. Soc. 123, 9769–9779. doi: 10.1021/ja010517q
Li, S., Demmelmaier, C., Itkis, M. E., Liu, Z., Haddon, R. C., and Yan, Y. (2003). Micropatterned oriented zeolite monolayer films by direct in situ crystallization. Chem. Mater. 15, 2687–2689. doi: 10.1021/cm034362s
Lian, X., and Park, S. S. (2016). Preparation of titanium dioxide films on etched aluminum foil by vacuum infiltration and anodizing. Appl. Surf. Sci. 388, 245–251. doi: 10.1016/j.apsusc.2016.01.166
Liu, F., Liu, C. L., Hu, B., Kong, W. P., and Qi, C. Z. (2012). High-temperature hydrothermal synthesis of crystalline mesoporous TiO2 with superior photo catalytic activities. Appl. Surf. Sci. 258, 7448–7454. doi: 10.1016/j.apsusc.2012.04.059
Mashimo, T., Bagum, R., Ogata, Y., Tokuda, M., Okube, M., Sugiyama, K., et al. (2017). Structure of single-crystal rutile (TiO2) prepared by high-temperature ultracentrifugation. Cryst. Growth Des. 17, 1460–1464. doi: 10.1021/acs.cgd.6b01818
Mitsuyoshi, D., Kuroiwa, K., Kataoka, Y., Nakagawa, T., Kosaka, M., Nakamura, K., et al. (2017). Shape selectivity in toluene disproportionation into para-xylene generated by chemical vapor deposition of tetramethoxysilane on MFI zeolite catalyst. Microporous Mesoporous Mater. 242, 118–126. doi: 10.1016/j.micromeso.2017.01.022
Mohamad, M., Haq, B. U., Ahmed, R., Shaari, A., Ali, N., and Hussain, R. (2015). A density functional study of structural, electronic and optical properties of titanium dioxide: characterization of rutile, anatase and brookite polymorphs. Mater. Sci. Semiconduct. Process. 31, 405–414. doi: 10.1016/j.mssp.2014.12.027
Na, L., Chen, M., and Liu, D. (2018). Deactivation kinetics with activity coefficient of the methanol to aromatics process over modified ZSM-5. Fuel 233, 283–290. doi: 10.1016/j.fuel.2018.06.044
Park, J. S., Lee, G. S., Lee, Y. J., Park, Y. S., and Yoon, K. B. (2002). Organization of microcrystals on glass by adenine–thymine hydrogen bonding. J. Am. Chem. Soc. 124, 13366–13367. doi: 10.1021/ja0270569
Razmimanesh, F., Amjad-Iranagh, S., and Modarress, H. (2015). Molecular dynamics simulation study of chitosan and gemcitabine as a drug delivery system. J. Mol. Model. 21:165. doi: 10.1007/s00894-015-2705-2
Shen, K., Ning, W., Qian, W., Cui, Y., and Wei, F. (2014). Atmospheric pressure synthesis of nanosized ZSM-5 with enhanced catalytic performance for methanol to aromatics reaction. Catal. Sci. Technol. 4, 3840–3844. doi: 10.1039/C4CY01010H
Shen, K., Qian, W., Wang, N., Zhang, J., and Wei, F. (2013). Direct synthesis of c-axis oriented ZSM-5 nanoneedles from acid-treated kaolin clay. J. Mater. Chem. A 1, 3272. doi: 10.1039/c3ta01479g
Svelle, S., Joensen, F., Nerlov, J., Olsbye, U., Lillerud, K. P., Kolboe, S., et al. (1999). The conversion of methanol to hydrocarbons over zeolite H-beta. Microporous Mesoporous Mater. 29, 173–184. doi: 10.1016/S1387-1811(98)00329-1
Wei, C., and Yen, J. Y. (2007). Effect of film thickness and interlayer on the adhesion strength of diamond like carbon films on different substrates. Diamond Relat. Mater. 16, 1325–1330. doi: 10.1016/j.diamond.2007.02.003
Wei, Q., Zhang, Y., Wang, Y., and Yang, M. (2017). A molecular dynamic simulation method to elucidate the interaction mechanism of nano-SiO 2 in polymer blends. J. Mater. Sci. 52, 12889–12901. doi: 10.1007/s10853-017-1330-0
Wu, M. C., Tóth, G., Sápi, A., Leino, A. R., Kónya, Z., Kukovecz, A., et al. (2012). Synthesis and photocatalytic performance of titanium dioxide nanofibers and the fabrication of flexible composite films from nanofibers. J. Nanosci. Nanotechnol. 12, 1421–1424. doi: 10.1166/jnn.2012.4655
Ye, J., Bai, L., Liu, B., Tian, H., Hu, J., Polo-Garzon, F., et al. (2019). Fabrication of a pillared ZSM-5 framework for shape selectivity of ethane dehydroaromatization. Ind. Eng. Chem. Res. 58, 7094–7106. doi: 10.1021/acs.iecr.8b04965
Keywords: b-oriented ZSM-5 zeolite film, α-quartz substrate, modification, surface structure, adsorption activity
Citation: Chu R, Yang D, Meng X, Yu S, Wan Y, Wu J and Wang J (2019) Effect of Surface Structure and Adsorption Activity on Implanting of b-Oriented ZSM-5 Zeolite Film on Modified α-Quartz Substrate. Front. Chem. 7:636. doi: 10.3389/fchem.2019.00636
Received: 19 June 2019; Accepted: 04 September 2019;
Published: 18 September 2019.
Edited by:
Qiang Wang, Beijing Forestry University, ChinaReviewed by:
Zifeng Yan, China University of Petroleum, ChinaTao Zhu, School of Chemical and Environmental Engineering, China University of Mining and Technology (Beijing), China
Copyright © 2019 Chu, Yang, Meng, Yu, Wan, Wu and Wang. This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.
*Correspondence: Xianliang Meng, bWVuZzI3JiN4MDAwNDA7Y3VtdC5lZHUuY24=