Advanced Nanomaterials for Green GrowthView this Special Issue
Synthesis of SAPO-34 Using Different Combinations of Organic Structure-Directing Agents
The effects of different mixtures of organic structure-directing agents (OSDAs) on the formation of SAPO-34 structure have been investigated. Different OSDAs, namely, triethylamine (TEA), tetraethylammonium hydroxide (TEAOH), and morpholine (Mor) and their combinations were used to synthesize SAPO-34 by a hydrothermal method. The template concentration was optimized by eliminating the competing phases to obtain the purest form of SAPO-34 phase. The as-synthesized samples were analyzed by XRD, FE-SEM/EDS, FT-IR, surface area/pore volume measurements, NH3-TPD, TG/DTA, and 29Si NMR MAS. The selection of template notably impacts the crystal size and physicochemical characteristics of as-synthesized SAPO-34. The sample prepared with 3 Mor : 3 TEA : 1 TEAOH exhibited the highest total acidity, smallest crystal size below 3 µm, and high surface area up to 697 m2/g.
Silicoaluminophosphate (SAPO) is a related grade of microporous material applied mostly in the scope of catalysis of processes such as hydro-isomerization of n-hexane, gas separations, methanol conversion to light olefins (MTO), pyrolysis reaction, or removal of NOx by selective catalytic reduction with ammonia (NH3-SCR). SAPO-34 is such an exciting catalyst in the SAPO generation. Since being discovered in the 1980s, large chabazite (CHA) with small channel systems, eight-membered rings (3.8 Å × 3.8 Å), and 9.4 Å in diameter cage called SAPO-34 has received significant attention, thanks to its high selectivity to light gases separation [1, 2].
Normally, SAPO-34 is prepared from a gel containing sources of an alumina source, a phosphorus source, a silica source, and leastwise one template source by using a hydrothermal method [3, 4]. The OSDA leads an essential duty in the synthesis of SAPO materials. Therefore, suitable OSDAs perform an indispensable role in the preparation of SAPO-34 involving in structure-directing, charge-compensating, and space-filling. Several organic amine compounds are used as a/an OSDA(s) in SAPO-34 syntheses, for example, tetraethylammonium hydroxide (TEAOH), morpholine (Mor), triethyl amine (TEA), dipropyl amine (DPA), and diethyl amine (DEA) [5–10]. The combination of OSDA surveyed in the preparation of SAPO-34 aims to increase the qualities as well as the catalytic performance of SAPO-34 [11, 12]. Between these OSDAs, the nanoparticle size of SAPO-34 can be achieved by using the quaternary ammonium compound TEAOH as a template, so TEAOH is the most commonly used compound to synthesize SAPO-34. Reducing the particle size of SAPO-34 enhanced its catalytic behavior in many previous reports. Hirota et al.  increased the catalyst lifespan in the methanol-to-olefin reaction by using the SAPO-34 material, which synthesized nanocrystals with particle sizes of 75 nm compared to that with bigger sizes of 800 nm. Using the sonochemical method with TEAOH as OSDA, Askari et al.  also observed 50 nm-sized SAPO-34 nanocrystals, which were active for a long time in the same reaction. However, the high cost of TEAOH limits its industrial applications [15, 16]. Compared to TEAOH, Mor is much cheaper. However, the use of Mor as an OSDA leads to the creation of materials which have large particle sizes and bad catalytic behavior in conversion reactions such as MTO [7, 15]. When TEAOH and Mor were combined as the binary OSDAs for the synthesis of SAPO-34, the obtained catalyst had a smaller crystal size and a larger surface area, thereby improving the performance of SAPO-34 catalyst in the methanol conversion reaction . A similar behavior was reported by Sedighi et al.  who used different combinations of TEAOH and Mor to synthesize SAPO-34 and obtained the catalyst with the most extended lifetime with optimal crystal size and acidity for MTO reaction. TEA is reported to favor the formation of a SAPO-5 impurity phase, although it costs considerably lower compared to TEAOH. However, until now, synthesizing SAPO-34 with a combination of templates containing TEA in the previous reports is relatively rare. Applying combined OSDAs, for instance, adding more than one directing agent into the initial solution to lead the creation of molecular sieve, has demonstrated to be an effective and cost-down method to synthesize SAPO-34 catalysts with nanoparticle size .
Furthermore, SAPO-34 with nanoparticle size and higher acid properties also was the most favorite parent zeolite of copper ion-exchanged SAPO-34 catalysts for NH3-SCR of NOx since their Brønsted acid sites represent a coordinate role with the Cu2+ active sites in this reaction . In SAPO-34, the substitution of aluminum and phosphorus atoms in the neutral aluminophosphate (AlPO-34) structural framework by silicon atoms will appear in Brønsted acid sites . Therefore, the interactions between OSDAs and the structure of SAPO materials and the Si content in the initial mixture influence the Si contribution, resulting in the alteration of the acid properties.
The purpose of this research is the preparation at the optimal TEAOH/Mor/TEA molar ratio of the SAPO-34 material with smaller particle size and high acid properties for further catalytic application in NH3-SCR of NOx reaction. In this study, the combination of OSDAs between TEA, Mor, and TEAOH was applied to prepare SAPO-34, and the influences of the molar ratio of TEA/Mor/TEAOH on the element composition, morphology, topology, and SAPO-34 zeolite were investigated in detail.
2. Materials and Methods
2.1. Synthesis of SAPO-34 Molecular Sieve
SAPO-34 molecular sieves were synthesized via the regular hydrothermal method. The material was prepared from a mixture gel with a molar composition of 1 Al2O3 : 0.6 SiO2 : 1 P2O5 : X OSDA(s) : 110 H2O, wherein X is shown in Table 1. Firstly, aluminum isopropoxide (98%, Merck) was mixed with distilled water, and phosphoric acid (85%, aqueous solution, Merck) was added dropwise. The mixture was stirred for one hour until completely dissolved, then tetraethyl orthosilicate TEOS (98%, Sigma) was added and stirred. After one hour, the templates including morpholine (99%w/w, ACS Reagent, Sigma), tetraethylammonium hydroxide (25%w/w, Sigma), and triethylamine (98%, Merck) were added to the solution. The resulting synthesis gel was further stirred for 6 hours until a uniform reaction mixture was formed and then aged for 12 hours. The obtained gel was crystallized at 200°C for 48 hours in a Teflon-lined autoclave. The as-synthesized sample was filtered, washed, and then dried at 120°C for 6 hours. The obtained sample was heated at 1°C/min and calcinated at 550°C for 6 h to remove the organic compound from template agents.
2.2. Characterization of Samples
The power X-ray diffraction (XRD) data of catalysts were procured by a powder X-ray diffractometer Bruker D8 at room temperature using Cu anode and Kα radiation at λ = 1.54 Å in the angular scale of 5–90° and scanning mode at 0.02° per step.
The morphology of the samples was observed by the field emission scanning electron microscope (FE-SEM) on a Hitachi S-4800 (Japan). The chemical composition of the catalysts was determined by the Hitachi system (S-4800 model) scanning electron microscope equipped with a dispersive energy X-ray (EDX) spectrometer.
Fourier-transform infrared (FT-IR) experiments were carried out with a JASCO FT/IR-4600 (Japan) infrared spectroscopy. For the identification of the functional groups or organic compounds in the catalyst, the sample and the KBr powder were mixed and milled in a mortar, with the component ratio of KBr and the catalyst at 100 : 1.
The nitrogen adsorption-desorption isotherms measurements were performed on a Micromeritics 2020 analyzer. Firstly, the as-synthesized catalyst was degassed under vacuum at 300°C and then measured at the boiling point of nitrogen (−195°C). The total surface area was determined based on the Brunauer–Emmett–Teller (BET) theory. The external surface area, micropore surface area, and micropore volume were analyzed by using the t-plot method.
The surface acidity determination was performed on temperature-programmed desorption with ammonia (NH3-TPD) experiments by using the Micromeritics Auto Chem 2920 instrument. In all of the analyses, 0.1 g of the catalyst sample was placed on a quartz fixed-bed U-shaped microreactor and degased in a continuous-flow nitrogen gas of 50 mL/min for 1 hour at 300°C. The sample was then cooled down to 100°C and then exposed to NH3 (helium-ammonia 10%) for 1 hour and thereafter fluxed with helium air at 100°C for 1 hour to remove any physiosorbed ammonia. The progress is continued until a stable baseline is acquired. Then, the NH3-TPD measurements were carried out from 100°C to 550°C at a fixed heating rate of 10°C/min. Finally, the spectrum through desorption of NH3 was recorded.
The detection of thermal amine compound decomposition of as-synthesized samples was performed by the thermal analysis method by using the thermogravimetric analysis (TGA) and differential scanning calorimeter/thermal analysis (DSC/DTA) instruments (PerkinElmer Pyris-1 TGA and DTA-7) under an airflow of 100 mL/min at a heating rate of 20°C/min from room temperature up to 800°C.
The solid state of 29Si NMR (nuclear magnetic resonance) spectroscopy with MAS (magic-angle spinning) experiments were carried out on a Bruker AV-300 NMR spectrometer (Ettlingen, Germany). To be more specific, the spinning rate was 6 kHz at the magic angle while the recycling rate was 5 s. For the chemical shift, C6H15NaO3SSi sodium salt (DSS) was used as the reference material.
3. Results and Discussion
In the preparation of the SAPO-34 material, the crystallization process depends importantly on the type of organic structure-directing agents because of their interaction with inorganic species and the alkalinity, which have influence on both the nucleation and crystal growth rates.
Figure 1 shows the structure parameters and phase purity of the as-synthesized catalysts prepared by different component ratios of templates through X-ray diffraction spectroscopy. The XRD patterns of all the prepared samples match well with SAPO-34 structures, except for sample M1, which was synthesized with only TEA as a template. That means both single Mor and TEAOH and a mixture with different OSDAs can be used to synthesize SAPO-34. The template TEA was preferable to synthesize SAPO-5 molecular sieves at 2θ = 7.5, 11.1, 14.9, 19.8, 21.1, and 22.5. The template Mor, TEAOH, or mixture with TEA/Mor/TEAOH was the most appropriate template for SAPO-34 which is characterized by diffraction peaks at 2θ = 9.6, 15.9, 19.2, 21.7, and 27.6. In Figure 1, all the as-synthesized samples obtained typical diffraction peaks of the trigonal phase, respectively, for the chabazite structure of SAPO-34 as OSDAs. However, the reflection intensity and the width of peaks were different and depended on the templates. The peaks of the as-synthesized samples with a single template, especially with TEAOH, were sharp and strong, indicating its better crystallinity and phase purity compared to those of the mixed template-prepared samples. The higher intensity and broader width of peaks from the sample prepared with Mor suggest the larger crystallite size of this sample. The least intense reflection of sample M8 indicates a loss of crystallinity and the decrease of crystal size due to the incorporation of Mor with TEAOH and TEA.
Figure 2 illustrates the FE-SEM photographs of synthesized samples prepared by different components of template agents. FE-SEM images clearly show different morphologies and crystal sizes of these samples (as seen in Figure S1, supplementary data). SAPO-5 crystals were obtained when using TEA as a template (M1 sample) which had hexagonal and plate-like morphology, a variation of the particle size from 10–20 µm. Using Mor, TEAOH could observe SAPO-34 which had cube-like rhombohedra morphology with different crystal sizes. M2 and M3 samples obtained perfect crystallization and could be very similar to natural chabazite with, respectively, crystal size varying from 20–45 µm and from 3–8 µm as well. These results are in agreement with their crystallinity and phase purity from XRD.
A mixture of Mor or TEA with TEAOH has shown the cube-like morphology which is the specific characteristic of SAPO-34 with impurities. FE-SEM photographs of M4 and M5 samples exhibited that SAPO-34 crystallization by TEA/TEAOH caused the presence of more impurity and larger particles about 5 μm, whereas using Mor/TEAOH as a templating agent resulted in good material purity with mean crystallite size less than 9 μm. The use of TEA or TEAOH as a sample in the initial synthetic gel may have a favorable effect in reducing the crystal size. The presence of TEAOH compared to TEA in preparation gel caused significant particle size reduction. Besides, using Mor as a subtemplate probably supports the formation of the purity phase of SAPO-34. The results are in complete agreement with the previous publications [20, 21].
The formation of SAPO-34 morphology could be determined by using different kind of templates. M6 and M7 samples have not only same crystallinity which can be seen on XRD pattern but also similar crystal shape of cube-like agglomerating to sphere. This means that TEA and Mor can cause the agglomeration of cubic particles to form a bigger sphere-like particle. The extent of the agglomeration depends on the ratio between templates. The morphology of M6 and M7 suggests that increasing the amount of TEA in the original gel results in the aggregation of cubic crystal into spherical particles. Moreover, combinations of TEA and the other templates lead to the formation of impurity phases . TEAOH template seems to be stronger than morpholine in competition with TEA and directing structure. While the particles synthesized with the mixture of TEAOH and TEA (M5 sample) only contain fewer impurities on the surface but not agglomerated, the crystals of M6 with cube-like morphology appear in competition with the cubic crystals of SAPO-34 including some impurities from the AFI structure. Sample M7 synthesized with a higher amount of TEA than that of Mor has a dominant spherical morphology. In the formation of SAPO-34 catalysts, with the combination of TEA and morpholine, the morphology evolves from spherical agglomerates consisting of micrometer-sized cubic crystals to self-assemblies of spherical nanosheets spliced by nanosquare pieces .
Compared to a single and binary template(s), the mixture of tri-templating provides smaller particles of SAPO-34 below 3 µm. Three templates, including both TEAOH and TEA as agents for monitoring the crystal size, result in a decrease in particle size.
Therefore, nucleation enhancement is probably liable for crystal size reduction . Mixing different OSDAs leads to the reduction in particle size as well as proper arrangement in size distribution and formation of a pure SAPO-34 structure. They can be enhanced by the presence of TEAOH even in little amount. This fact can be explained by the role of structure-directing substances to fill the space and impact between three different types of OSDA, including TEA, Mor, and TEAOH. Furthermore, using more than one OSDA could narrow space-filling around the molecule templates, leading to a rise in the number of small crystal seeds in the nucleation process.
Table 2 shows the final elemental composition of production evaluated by the EDS analysis. The final SAPO-34 compositions concerning aluminum, silicon, and phosphorous elementals based on (AlXPYSiZ)O2 formula were achieved by the mole percentage of each atom. Compared to all starting gel ratio Si/(Al + P + Si) of 0.13 (the Si content is 13%), this proportion in products was higher than 13% after crystallization. The samples synthesized by a single template showed the highest composition of Si element. The composition of Si element in samples synthesized by a single template was the highest, while that of samples prepared by mixture of OSDAs were lower. This could be attributable to alkaline environment coming from structure-directing agents and the fundamental interactions between templates and structure of SAPO materials. The influence of Si distribution by the number of framework charges are due to not only Si atoms introduced into SAPO-34 channels but also the number of OSDA molecules inserted into cages . It means that if there are an additional content of silicon integrating within the structure of SAPO-34 materials, they could exist as amorphous phase in extra-framework [15, 26].
FT-IR spectroscopy is a well-known technique for identifying zeolite materials’ framework structures and their acidity due to the appearance of some typical vibrations in IR spectra, which could come from the charge-balancing cations, the framework, or the relatively isolated groups . Figure 3 shows the IR spectra of SAPO-34 with differing OSDA type of the samples, and the transmission bands of the as-synthesized samples are in good agreement with the published data [28–30]. In the fingerprint region (400–1150 cm−1), the bands collected around 500 cm−1 and 620 cm−1 are mainly referred to the T-O tetrahedra bending bands of SiO4 and double-6 rings. The double-6 ring is a basic structural unit of CHA framework; hence, an appearance of this peak corresponds to the successful synthesis of SAPO-34. The vibration band at 850 cm−1 is assigned to the symmetric stretching vibration of P-O (or Al-O), while that at 1150 cm−1 is credited for the asymmetric stretching vibration of O-P-O. The band at 1600 cm−1 corresponds to the vibrational bending mode of H-O-H weakly adsorbed in the SAPO-34 channels and assigned to CH3 bending vibrational frequencies of the template molecule [31, 32]. The asymmetric stretching vibration of physically adsorbed CO2 from the environment shows weak absorbance at 2360 cm−1 [27, 28]. All spectra of as-synthesized samples show a broad adsorption band between 3400 cm−1 and 3600 cm−1, which could be allocated to the hydroxyl groups from the Si-OH-Al bond. This hydroxyl bonding evidences that the production of Brønsted acidity of SAPO-34 improves . The intensity of this peak was almost similar for samples M3, M4, M5, and M8, except for M6 sample, which is lower. It could be assumed that the OH peak in FT-IR spectra of M6 sample is assigned for the formation of hydroxyl groups in the defect structure.
The nitrogen adsorption-desorption isotherms of the as-synthesized SAPO-34 samples are displayed in Figure 4, and Table 3 shows the crystal size and surface area of these samples. As seen in Figure 4, M3, M4, M5, and M8 samples displayed the curve at low relative pressures which referred to type I isotherm microporous solids. And, absorption near the saturation pressure in the isotherm lines of the as-synthesized samples can be detected due to the intercrystalline porosity, which is common in the nanostructures and microporosity of SAPO-34 . As illustrated in this table, the average sizes of these samples vary from 3 µm to 38 µm depending on the type of templates. It is significant that the surface area of SAPO-5 material was smaller than that of the SAPO-34 molecular sieve. The surface area of pure SAPO-34 reached up to 650 m2/g in several previous reports [34–36]. Our prepared SAPO-34 samples also have a high surface area in the range from 440 m2/g to 725 m2/g depending on the type of templates. The highest surface area belonged to the sample prepared by using TEA/TEAOH as OSDAs, which is even higher than that of pure reported SAPO-34. The differences in the surface area are attributable to specific changes in channel dimensions and crystal network caused by each OSDAs.
NH3-TPD descriptions exhibited two desorption profiles of ammonia peaks corresponding to the weak and strong acid sites of as-synthesized SAPO-34 materials (Figure 5). The desorption of NH3 molecules on weak acidic centers, which are mostly Lewis acid sites and/or the Brønsted acid sites produced by either P-OH hydroxyl groups not sufficiently linked to the [AlO4] tetrahedra or Al-OH and Si-OH groups or other zeolitic defects, causes the appearance of the first peak at a low temperature of 150–250°F . The desorption peak shown at a higher temperature of 350–450°C is ascribed to the stronger acid sites, formed by the substitution of P by Si atoms in the framework of the SAPO-34. These sites are related to Si-OH-Al hydroxyl groups as strong Brønsted acid sites, which should be operated for MTO or deNOx reaction [37, 38].
The amount of NH3 desorption of four samples is different, which depends on the amount of Si contents. The M3 sample with the highest Si content has the highest Brønsted acid sites since these sites (Si-OH-Al) are generated by the proton produced by the template(s) for balancing the negative charges which originated from the incorporation of Si into the neutral AlPOs framework. The origin of the formation of the acid centers of SAPO-34 molecular sieves is consistent with the previous report , in which acid sites were produced by the incorporation of Si into the aluminophosphate channel. Although Si content of M8 was lower than that of the M4 sample (Table 2), the M8 sample exhibited higher total acid sites due to a higher concentration of hydroxyl groups, indicating that the formation of Si islands in M4 samples might decrease its acid content. Moreover, the combination of TEA/Mor and TEAOH benefits for the Si incorporation into the SAPO-34 framework, leading to an increase in strong acid amounts of the M8 sample. There is an agreement between the ammoniac adsorption-desorption curve with the FT-IR spectrum of the samples in terms of band region of the OH vibration. The replacement of Si for other atoms (Si and P) in the AlPO framework plays an essential role in acid site production .
Figure 6 depicts the TG/DTA curves of the prepared samples under different templating agents burning in the air. Three weight losses (I, II, and III) in the range of 25–800°C are observed in the TG analysis. The first weight loss (I) occurring from 25 to 200°C is assigned to the desorption progress of physically adsorbed water from the as-synthesized samples. A strongly exothermic process arising between 200°C and 450°C caused the second weight loss (II) which represented combustion decomposition of the templates. The third weight loss (III) with an exothermic process at a temperature greater than 450°C is likely due to the removal of the residual templating agents in the channel molecular sieve of SAPO-34 . The TGA results show that there was a competition among the decomposition of templates at temperatures higher than 500°C. Three absorption peaks were observed in all differently templating samples. Water decomposition occurred at a low temperature (70°C) with a weak signal, demonstrating the modest capacity in the molecule and the weak interactions between water molecules and the molecular sieve. The second absorption peak represents the intensity of the removal of the templates. In particular, sample M8, obtained with the tri-template TEA/Mor/TEAOH, had a sharp and strong removal peak while double-template with several structure-directing agents, namely, TEA/TEAOH and Mor/TEAOH, had different elevation peaks at this point. The results show that the interaction between the TEAOH agent and the framework of SAPO-34 was the most powerful.
The TGA results of M4, M5, and M8 samples are shown in Table 4. According to the molecular weight loss research, the reduced weight of water was quite small, and the primary reason for weight loss was caused by the removal of the templates. Besides, the weight loss of the different samples was distinct. The moles of templates located in the molecular sieves prepared with the different templates were directly calculated by using the thermogravimetric analysis results. The average number of templating agents per cage in the sample molecular sieve was 1.48, 1.25, and 1.36 with M4, M5, and M8, respectively. For sample M5, which used the dual template of Mor and TEAOH, more favorably entered the cage structure due to the presence of negative charges of morpholine in the SAPO-34 framework. Marchese et al.  reported that on average, 1.5 molecules of morpholine present within the chabazite channels of SAPO-34. Meanwhile, the molecular volume of cyclic morpholine is significantly lower than that of TEA, which contains three ethyl branches . In the case of Mor/TEA/TEAOH mixture, because the material framework and TEAOH templating agent had the most potent force and easily linked with the aluminum atoms, silicon atoms, and phosphorus atoms at the precursor process of crystallization, adding TEAOH enhances the medium number of OSDAs in the material cage.
The silicon situation in the framework of SAPO-34 was analyzed by 29Si MAS NMR. In Figure 7, several peaks exhibited in the spectrum of samples M4, M5, and M8 are shown According to , the strong peak at δ = −90.3 ppm should be due to Si(4Al) species; the small peaks formants shown at δ = −93.2 ppm and −98.9 ppm were attributed to Si(3Al) and Si(2Al) species, respectively, and the peak appeared at δ = −108.9 ppm resulting from the Si(0Al) environment. The presence of different silicon situations is suitable for the silicone replacement theory , in which SM2 (the substitution of P atoms by Si atoms alone) and SM3 (a pair Si atoms substituted by a pair of Al + P). A silicon-island region surrounded by the SM2 method was created, and the center was substituted by SM3. Compared to the dual template of Mor/TEAOH and TEA/TEAOH, increasing the relative contents of Si(3Al), Si(2Al), Si(1Al), and Si(0Al) structures is the result of using a combination of three templates. Based on Table 5 which shows the distribution of the acid properties of as-synthesized catalysts with different template agents, it can be concluded that the creation of silicon islands enhances the acidity of the silicoaluminophosphate zeolite SAPO-34 synonymous with the acid strength of the molecular sieves SAPO-34 which gradually grew up by increasing the size of the silicon islands . The strongest acid sites were located on the borders of the silicon islands.
By using the hydrothermal method, SAPO-34 molecular sieves were prepared with various combinations of Mor/TEA/TEAOH as organic structure-directing agents showed different physicochemical characteristics. The single-template TEA was preferable to synthesize SAPO-5 molecular sieves, while TEAOH and Mor favored SAPO-34 formation. The morphology of all samples was the same to the uniform cube-shaped particles of the standard SAPO-34 material, except as-synthesized samples using Mor/TEA as OSDAs, which additionally includes sphere-shaped particles consisting of cubic agglomerates. Combination of tri-templates in the initial gel led to decrease in the particle size of the samples. The morphology of spherical particles can be created by a coherence of nanosized crystals, and the crystal size will be reduced to submicrometer size. The catalyst with molar ratios of Mor : TEA : TEAOH = 3 : 3 : 1 increased the surface area, decreased the crystal size of the samples to nanosize, improved the crystallinity, and enhanced the acid content. The preparation of SAPO-34 catalysts with mixture template synthesis was proven to be effective and has economic advantages.
The X-ray diffraction, field emission scanning electron microscope, Fourier-transform infrared method, N2 adsorption-desorption, magic-angle spinning nuclear magnetic resonance, thermogravimetric analysis, differential scanning calorimeter/thermal analysis, and temperature-programmed desorption of ammonia data used to support the findings of this study are included within the article. The field emission scanning electron microscope data used to support the findings of this study are included within the supplementary information file for more details with images of increased resolution.
Conflicts of Interest
The authors declare that they have no conflicts of interest.
This work was supported by the RoHan Project funded by the German Academic Exchange Service (DAAD, no. 57315854) and the Federal Ministry for Economic Cooperation and Development (BMZ) inside the framework SDG Bilateral Graduate School Programme. And, this research was also funded by the Vietnam National Foundation for Science and Technology Development (NAFOSTED) under grant no. 104.05-2018.306.
Supplementary Figure S1. field emission scanning electron microscope images of as-synthesized SAPO-34 from different organic structure-directing agents. FE-SEM images clearly show different morphologies and crystal sizes of these samples on a larger scale. (Supplementary Materials)
B. M. Lok, C. A. Messina, R. L. Patton, R. T. Gajek, T. R. Cannan, and E. M. Flanigen, “Silicoaluminophosphate molecular sieves: another new class of microporous crystalline inorganic solids,” Journal of the American Chemical Society, vol. 106, no. 20, pp. 6092-6093, 1984.View at: Publisher Site | Google Scholar
Ø. B. Vistad, D. E. Akporiaye, and K. P. Lillerud, “Identification of a key precursor phase for synthesis of SAPO-34 and kinetics of formation investigated by in situ X-ray diffraction,” Journal of Physical Chemistry B, vol. 105, no. 50, pp. 12437–12447, 2001.View at: Publisher Site | Google Scholar
M. Hunger, M. Seiler, and A. Buchholz, “In situ MAS NMR spectroscopic investigation of the conversion of methanol to olefins on silicoaluminophosphates SAPO-34 and SAPO-18 under continuous flow conditions,” Catalysis Letters, vol. 74, pp. 61–68, 2001.View at: Google Scholar
M. Salmasi, S. Fatemi, and A. Taheri Najafabadi, “Improvement of light olefins selectivity and catalyst lifetime in MTO reaction; using Ni and Mg-modified SAPO-34 synthesized by combination of two templates,” Journal of Industrial and Engineering Chemistry, vol. 17, no. 4, pp. 755–761, 2011.View at: Publisher Site | Google Scholar
S. M. Auerbach, K. A. Carrado, and P. K. Dutta, Handbook of Zeolites Science and Technology, Marcel Dekker, Inc., New York, NY, USA, 2003.
E. Aghaei and M. Haghighi, “High temperature synthesis of nanostructured Ce-SAPO-34 catalyst used in conversion of methanol to light olefins: effect of temperature on physicochemical properties and catalytic performance,” Journal of Porous Materials, vol. 22, no. 1, pp. 187–200, 2015.View at: Publisher Site | Google Scholar
Z. Li, J. Martínez-Triguero, P. Concepción, J. Yu, and A. Corma, “Methanol to olefins: activity and stability of nanosized SAPO-34 molecular sieves and control of selectivity by silicon distribution,” Physical Chemistry Chemical Physics, vol. 15, no. 35, pp. 14670–14680, 2013.View at: Publisher Site | Google Scholar
L. Marchese, A. Frache, E. Gianotti, G. Martra, M. Causà, and S. Coluccia, “ALPO-34 and SAPO-34 synthesized by using morpholine as templating agent. FTIR and FT-Raman studies of the host-guest and guest-guest interactions within the zeolitic framework,” Microporous and Mesoporous Materials, vol. 30, no. 1, pp. 145–153, 1999.View at: Publisher Site | Google Scholar