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.