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.

1. Support preparation
<ol>
	<li>Pretreatment of support
	<ol>
		<li>Cut out a 3 cm long tubular porous &#945;-Al2O3 support (see Table of Materials).</li>
		<li>Wash the support with distilled water for 10 min. After that, wash the support with acetone for 10 min. Repeat this washing process 2x. 
		NOTE: Do not touch the outer surface of a support after the washing step. No other treatment was carried out (e.g., sonication, and rubbing by sandpaper, etc.)</li>
		<li>Dry the ...

<ol>
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J. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Matrimid&#174;+derived+carbon+molecular+sieve+hollow+fiber+membranes+for+ethylene/ethane+separation.">Matrimid&#174; derived carbon molecular sieve hollow fiber membranes for ethylene/ethane separation.</a> Journal of Membrane Science. 380, 138-147 (2011).</li><li>Morigami, Y., Kondo, M., Abe, J., Kita, H., Okamoto, K. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=The+first+large-scale+pervaporation+plant+using+tubular-type+module+with+zeolite+NaA+membrane.">The first large-scale pervaporation plant using tubular-type module with zeolite NaA membrane.</a> Separation and Purification Technology. 25, 251-260 (2001).</li><li>Kondo, M., Komori, M., Kita, H., Okamoto, K. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Tubular-type+pervaporation+module+with+zeolite+NaA+membrane.">Tubular-type pervaporation module with zeolite NaA membrane.</a> Journal of Membrane Science. 133, 133-141 (1997).</li><li>Hoof, V. V., Dotremont, C., Buekenhoudt, A. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Performance+of+Mitsui+NaA+type+zeolite+membranes+for+the+dehydration+of+organic+solvents+in+comparison+with+commercial+polymeric+pervaporation+membranes.">Performance of Mitsui NaA type zeolite membranes for the dehydration of organic solvents in comparison with commercial polymeric pervaporation membranes.</a> Separation and Purification Technology. 48, 304-309 (2006).</li><li>Kamimura, Y., Chaikittisilp, W., Itabashi, K., Shimojima, A., Okubo, T. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Critical+Factors+in+the+Seed-Assisted+Synthesis+of+Zeolite+Beta+and+"Green+Beta"+from+OSDA-Free+Na+-Aluminosilicate+Gels.">Critical Factors in the Seed-Assisted Synthesis of Zeolite Beta and "Green Beta" from OSDA-Free Na+-Aluminosilicate Gels.</a> Chemistry An Asian Journal. 5, 2182-2191 (2010).</li><li>Majano, G., Delmotte, L., Valtchev, V., Mintova, S. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Al-Rich+Zeolite+Beta+by+Seeding+in+the+Absence+of+Organic+Template.">Al-Rich Zeolite Beta by Seeding in the Absence of Organic Template.</a> Chemistry of Materials. 21, 4184-4191 (2009).</li><li>Sakai, M., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Formation+process+of+*BEA-type+zeolite+membrane+under+OSDA-free+conditions+and+its+separation+property.">Formation process of *BEA-type zeolite membrane under OSDA-free conditions and its separation property.</a> Microporous and Mesoporous Materials. 284, 360-365 (2019).</li><li>Choi, J., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Grain+Boundary+Defect+Elimination+in+a+Zeolite+Membrane+by+Rapid+Thermal+Processing.">Grain Boundary Defect Elimination in a Zeolite Membrane by Rapid Thermal Processing.</a> Science. 325, 590-593 (2009).</li><li>Dong, J., Lin, Y. S., Hu, M. Z. -. C., Peascoe, R. A., Payzant, E. A. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Template-removal-associated+microstructural+development+of+porous-ceramic-supported+MFI+zeolite+membranes.">Template-removal-associated microstructural development of porous-ceramic-supported MFI zeolite membranes.</a> Microporous and Mesoporous Materials. 34, 241-253 (2000).</li><li>Schoeman, B. J., Babouchkina, E., Mintova, S., Valtchev, V. 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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...

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&#39;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, &#34;*&#34; 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.

<table border="1" fo:keep-together.within-page="1" fo:keep-with-next.within-page="always">
	<tbody>
		<tr>
			<td>a-Al2O3 support</td>
			<td>Noritake Co. Ltd.</td>
			<td>NS-1</td>
			<td>Average pore size, 150 nm; Outer diameter, 10 mm; Innar diameter, 7 mm</td>
		</tr>
		<tr>
			<td>Colloidal silica</td>
			<td>Nissan Chemical</td>
			<td>ST-S</td>
			<td>SiO2 30.5%, Na2O 0.44%, H2O 69.1%</td>
		</tr>
		<tr>
			<td>Mesh filter (PTFE membrane)</td>
			<td>Omnipore</td>
			<td>JGWP04700</td>
			<td>Pore size, 200 nm</td>
		</tr>
		<tr>
			<td>NaAl2O</td>
			<td>Kanto Chemical</td>
			<td>34095-01</td>
			<td>Na2O 31.0-35.0%; Al2O3 34.0-39.0%</td>
		</tr>
		<tr>
			<td>NaOH</td>
			<td>Kanto Chemical</td>
			<td>37184-00</td>
			<td>97%</td>
		</tr>
		<tr>
			<td>Tetraethylammonium hydroxide</td>
			<td>Sigma-Aldrich</td>
			<td>302929-500ML</td>
			<td>35 wt% solution</td>
		</tr>
	</tbody>
</table>

organic structure-directing agent-free synthesis for *bea-type zeolite membrane

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 &#945;-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.

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&#176; 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...

Watch this Scientific Journal Video about Organic Structure-directing Agent-free Synthesis for *BEA-type Zeolite Membrane at JoVE.com

Organic Structure-directing Agent-free Synthesis for *BEA-type Zeolite Membrane

A *BEA seed crystal was loaded on a porous &#945;-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 ...

The preparation of zeolite membrane is based on knowhow and experience accumulated in the laboratory. We would like to share this protocol as a reference for everyone who wants to start membrane synthesis. This method enables us to obtain a BEA membrane, having a good separation performance without using organic structure-directing-agent.Operationally, equipment for zeolite membrane preparation are quite unique. This video can help you to run how to prepare zeolite membranes. Demonstrating the procedure will be Yuto Tsuzuki, a graduate student from our laboratory.To begin, cut out a three centimeter long tubular porous alpha aluminum oxide support. Wash the support with distilled water for 10 minutes. After that, wash the support with acetone for 10 minutes.Repeat this washing process twice. Use a beaker to transfer the washed support into an incubator to dry at 110 degrees Celsius overnight. In the morning, measure the weight of the support piece.First, add 26.2 grams of colloidal silica and 8.39 grams of tetraethylammonium hydroxide into a 250ml bottle made of polypropylene. Stir the mixture using a magnetic stirrer for 20 minutes in a 50 degrees Celsius water bath. After that, stir the mixture using a magnetic stirrer for 20 minutes at room temperature.Then, add 8.39 grams of tetraethylammonium hydroxide, 5.79 grams of distilled water, 1.08 grams of sodium hydroxide, and 0.186 grams of sodium aluminate into a Teflon beaker. Stir the mixture, by using a magnetic stirrer for 20 minutes at room temperature. Next, add solution B to solution A in a 250ml bottle.The mixture of solution A and B becomes milky. Cap the bottle, and shake it vigorously by hand for 5 minutes. After that, stir the mixture, using a magnetic stirrer, for 24 hours at room temperature.The next day, the gel obtained is the synthesis gel, with the final composition of 24 sodium oxide to one aluminum oxide to 200 silicon dioxide to 69 tetraethylammonium hydroxide to 2905 water. To perform crystallization, pour the synthesis gel into a Teflon-lined autoclave. Place the autoclave in an air oven at 100 degrees Celsius for seven days.Then, quench the autoclave with flowing water for 30 minutes. Remove the white sediment in the autoclave by a vacuum filtration apparatus with a 200 nanometer mesh filter. Wash the white sediment with 200ml of boiling water to remove amorphous and uncrystallized materials.Dry the washed sediment in a dish at 110 degrees Celsius overnight. The dried sediment is the seed crystal. To prepare BEA seed slurry, add 0.5g of the seed crystals into 100ml of distilled water in a bottle.Carry out sonication of the seed slurry for one hour to disperse the seed crystals. Then, fix a tubular support with a stainless steel rod, using Teflon tape, to plug the inside of the support. Pour the seed slurry into a glass tube, with a 19ml diameter.Immerse the fixed support into the poured seed slurry and wait for one minute. After that, withdraw the seed slurry vertically at approximately 3 centimeters per second through the silicon cap. Repeat the dip-coating process one more time.After dip-coating, dry the support at 70 degrees Celsius for two hours. Next, calsign the dip-coated support at 538 degrees Celsius for six hours with the increase and decrease temperature rates at 50 degrees Celsius per minute. This removes OSDA and chemically binds the seeds onto the support surface.After calcination, measure the weight of the support. Calculate the amount of seed crystal loaded, as the difference in the support weight, before and after dip-coating. Add 92.9 grams of distilled water, 9.39 grams of sodium hydroxide, and 1.15 grams of sodium aluminate into a 250ml polypropylene bottle.Stir the mixture using a magnetic stirrer for 30 minutes at 60 degrees Celsius in a water bath. After that, add 81.6 grams of colloidal silica in a step-wise manner of 1 drop per second into the mixture. Stir the mixture for another four hours at 60 degrees Celsius in a water bath.The gel obtained is the synthesis gel, having a final composition of 30 sodium oxide to one aluminum oxide to 100 silicon oxide to 2000 water. Then, pour the synthesis gel into a Teflon-lined autoclave in which the seeded support is placed vertically. Place the autoclave in an air oven at 120 degrees Celsius for seven days for crystallization.After crystallization, quench the autoclave with flowing water for 30 minutes. Wash the support with the membrane in boiling water for eight hours and dry overnight. This is the BEA membrane.After drying, measure the weight of the prepared support with membrane. Calculate the weight of the membrane by the difference in support weight before and after crystallization. The X-ray defraction pattern of synthesized BEA seed crystal, shows typical strong reflection peaks, around two theta, equaling 7.7 and 22.1 degrees.In addition, no obvious reflection peaks, other than the BEA type zeolite, were observed. Spherical seed crystals were observed through the FE-SEM image of the synthesized seed crystal and their size was uniformly approximately 200 nanometers. The X-ray defraction pattern of synthesized BEA membrane shows the same peaks observed in the seed crystals.In addition, reflection peaks of alpha aluminum oxide with two theta equaling 26, 35.5 and 38 degrees were observed. FE-SEM image of the synthesized membrane reveals that the crystals had truncated octohedral morphology, uniformly covering the support surface. There are many kinds of zircon and aluminum sources for zeolite synthesis.However, please do not change your materials for preparation of this BEA-type membrane.

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14.1K vistas.  Waseda University. La preparación de la membrana de zeolita se basa en el knowhow y la experiencia acumulada en el laboratorio. Nos gustaría compartir este protocolo como referencia para todos los que quieren iniciar la síntesis de membranas. Este método nos permite obtener una membrana BEA, teniendo un buen rendimiento de separación sin utilizar estructura orgánica-dirección-agente.Operativamente, los equipos para la preparación de la membrana de zeolita son bastante únicos. Este video puede ay...