A *BEA seed crystal was loaded on a porous α-Al2O3 support by the dip-coating method, and hydrothermally grown without using an organic structure-directing agent. A *BEA-type zeolite membrane having very few defects was successfully prepared by the secondary growth method.
Membrane separation has drawn attention as a novel-energy saving separation process. Zeolite membranes have great potential for hydrocarbon separation in petroleum and petrochemical fields because of their high thermal, chemical, and mechanical strength. A *BEA-type zeolite is an interesting membrane material because of its large pore size and wide Si/Al range. This manuscript presents a protocol for *BEA membrane preparation by a secondary growth method that does not use an organic structure-directing agent (OSDA). The preparation protocol consists of four steps: pretreatment of support, seed preparation, dip-coating, and membrane crystallization. First, the *BEA seed crystal is prepared by conventional hydrothermal synthesis using OSDA. The synthesized seed crystal is loaded on the outer surface of a 3 cm long tubular α-Al2O3 support by a dip-coating method. The loaded seed layer is prepared with the secondary growth method using a hydrothermal treatment at 393 K for 7 days without using OSDA. A *BEA membrane having very few defects is successfully obtained. The seed preparation and dip-coating steps strongly affect the membrane quality.
Membrane separation has drawn attention as novel-energy saving separation process. Many types of membranes have been developed for the past decades. Polymeric membranes have been widely used for gas separation, creating drinkable water from sea water1, and wastewater treatment2.
Inorganic membrane materials like silica3, carbon molecular sieve4, and zeolite have advantages for thermal, chemical, and mechanical strength compared with polymeric membranes. Therefore, inorganic membranes tend to be used under more severe conditions, such as hydrocarbon separation in petroleum and petrochemical fields.
Zeolite has unique adsorption and molecular sieving properties due to its micropores. In addition, zeolite has a cation exchange ability that contributes to control zeolite's adsorption and molecular sieving properties. The number of cations in zeolite is determined by the Si/Al ratio of the zeolite structure. Therefore, the size of the micropores and Si/Al ratio are key characteristics that determine the permeation and separation properties of zeolite membranes. For these reasons, zeolite is a promising type of inorganic membrane material. Some zeolite membranes have already been commercialized for dehydration of organic solvents due to their hydrophilicity and molecular sieving properties5,6,7,8.
*BEA-type zeolite is an interesting membrane material because of its large pore size and wide Si/Al range. *BEA has generally been prepared by hydrothermal treatment using tetraethylammonium hydroxide as organic structure-directing agent (OSDA). However, the synthesis method using OSDA has economic and environmental disadvantages. Recently, a seed-assisted method for *BEA synthesis without using OSDA was reported9,10.
*BEA is an intergrowth crystal of polymorph A and polymorph B. Thereby, "*" represents an intergrowth material. At present, no bulk materials consisting only of polymorph A or B is known.
We have successfully prepared *BEA membranes without using OSDA by a modified seed-assisted method11. The *BEA membrane had very few defects and exhibited high separation performance for hydrocarbons due to its molecular sieving effect. It is well known that calcination to remove OSDA after synthesis is one of the most common causes of defect formation in zeolite membranes12,13. Our *BEA membrane prepared without using OSDA showed good separation performance possibly because this calcination step was skipped.
The preparation of zeolite membranes is based on know-how and experience accumulated in the laboratory. Consequently, it is difficult for a beginner to synthesize zeolite membranes alone. Here, we would like to share a protocol for *BEA membrane preparation as a reference for everyone who wants to start membrane synthesis.
1. Support preparation
2. *BEA seed crystal synthesis
3. Seeding on support by dip-coating
4. *BEA membrane preparation by a secondary growth method
Figure 1 shows the preparation procedure of the *BEA seed crystal. Figure 2 shows the X-ray diffraction (XRD) pattern of synthesized *BEA seed crystal. Typical strong reflection peaks of (101) and (302) around 2q = 7.7 and 22.1° appeared. In addition, no obvious reflection peaks other than the *BEA-type zeolite were observed. These results showed that the pure phase of *BEA zeolite was successfully synthesized.
A typical FE-SEM image of the synthesized seed crystal is shown in Figure 3. Spherical seed crystals were observed and their size was uniformly ~200 nm. The Si/Al ratio of the obtained crystals was ~19 when analyzed by EDX.
Figure 4 and Figure 5 show the procedures of dip-coating and membrane preparation, respectively. Figure 6 shows the XRD pattern of synthesized *BEA membrane. As in the case of the seed crystals, typical strong reflection peaks of (101) and (302) around 2q = 7.7 and 22.1° appeared. In addition, reflection peaks of α-Al2O3 as support around 2q = 26, 35.5, and 38° were observed. As a result, we were able to confirm that the pure phase of *BEA was obtained as a membrane.
A typical field emission scanning electron microscope (FE-SEM) image of the synthesized membrane is shown in Figure 7. Crystals having truncated octahedral morphology uniformly covered the support surface. The distinct morphology seems to be very similar to typical *BEA crystals synthesized by the OSDA-free method previously reported9,10,15. The Si/Al ratio of the obtained membrane was ~5.1 analyzed by EDX.
Figure 1: Preparation procedure of *BEA seed crystal. *BEA seed crystal was synthesized by typical hydrothermal treatment using OSDA. Please click here to view a larger version of this figure.
Figure 2: XRD pattern of *BEA seed crystals. The crystal phase of the sediment obtained was confirmed with the XRD pattern. Please click here to view a larger version of this figure.
Figure 3: Typical FE-SEM image of seed crystals. Microscopic analysis was carried out to estimate the size of the seed crystals. Please click here to view a larger version of this figure.
Figure 4: Dip-coating procedure. Seed crystals were loaded by the dip-coating method using the seed slurry. Please click here to view a larger version of this figure.
Figure 5: Preparation procedure of the *BEA membrane. The *BEA membrane was synthesized by the secondary growth method without using OSDA. Please click here to view a larger version of this figure.
Figure 6: XRD pattern of the *BEA membrane. The crystal phase of the membrane obtained was confirmed from the XRD pattern. Please click here to view a larger version of this figure.
Figure 7: Typical FE-SEM image of the *BEA membrane. Microscopic analysis was carried out to investigate the membrane thickness and crystal morphology. Please click here to view a larger version of this figure.
There are many kinds of Si and Al sources for zeolite synthesis. However, we cannot change raw materials for preparation of this *BEA-type membrane. If raw materials are changed, the phase of zeolite crystallized and/or growth rate may be changed.
Glass beakers cannot be used for synthesis gel preparation because the synthesis gel has high alkalinity. Bottles and beakers made of polyethylene, polypropylene, and Teflon can be used instead.
To prepare a higher quality *BEA membrane, uniform seed layer on the outer surface of tubular support is essential. The size of the seed crystals and their distribution are quite important to form a uniform seed layer by dip-coating. The required seed size is larger than that of the pore size of the support (150 nm) to stop the seed crystal from spreading into the support. In addition, a narrow distribution of the seed size is also required to prepare a uniform seed layer.
Crystallization conditions for membrane preparation such as temperatures and time periods are quite important. Changing the crystallization conditions easily shifts the phase of zeolite crystalized. Higher temperatures and longer time periods lead to crystallization of the MOR-type zeolite. If the MOR-type zeolite co-crystallizes in the *BEA membrane, large spherical crystal can be observed on the surface by microscopic observation.
Successfully synthesized *BEA membrane has very few defects and can be used for hydrocarbon separation11.
The authors have nothing to disclose.
This work was partially supported by JST CREST (Japan Science and Technology agency, Create REvolutionary technological seeds for Science and Technology innovation program), Grant Number JPMJCR1324, Japan.
a-Al2O3 support | Noritake Co. Ltd. | NS-1 | Average pore size, 150 nm; Outer diameter, 10 mm; Innar diameter, 7 mm |
Colloidal silica | Nissan Chemical | ST-S | SiO2 30.5%, Na2O 0.44%, H2O 69.1% |
Mesh filter (PTFE membrane) | Omnipore | JGWP04700 | Pore size, 200 nm |
NaAl2O | Kanto Chemical | 34095-01 | Na2O 31.0-35.0%; Al2O3 34.0-39.0% |
NaOH | Kanto Chemical | 37184-00 | 97% |
Tetraethylammonium hydroxide | Sigma-Aldrich | 302929-500ML | 35 wt% solution |