Faujasite (FAU-type zeolite) is a mineral group in the zeolite family of silicate minerals. The group consists of faujasite-Na, faujasite-Mg and faujasite-Ca. They all share the same basic formula (Na2,Ca,Mg)3.5[Al7Si17O48]·32(H2O) by varying the amounts of sodium, magnesium and calcium.[1] Faujasite occurs as a rare mineral in several locations worldwide.
| Faujasite | |
|---|---|
 | |
| General | |
| Category | Zeolite |
| Formula (repeating unit) | (Na2,Ca,Mg)3.5[Al7Si17O48]·32(H2O)[1] |
| IMA symbol | Fau[2] |
| Strunz classification | 9.GD.30 |
| Crystal system | Cubic |
| Crystal class | Hexoctahedral (m3m) H–M Symbol (4/m 3 2/m) |
| Space group | Fd3m |
| Unit cell | a = 24.638–24.65 Å, Z = 32 |
| Identification | |
| Color | Colorless, white |
| Crystal habit | Octahedral or rarely trisoctahedral crystals up to 4 mm in size |
| Twinning | on {111}, contact and penetration twins |
| Cleavage | {111}, perfect |
| Fracture | Uneven to conchoidal |
| Tenacity | Brittle |
| Mohs scale hardness | 4.5-5 |
| Luster | Vitreous to adamantine |
| Streak | White |
| Diaphaneity | Transparent |
| Specific gravity | 1.92–1.93 |
| Optical properties | Isotropic |
| Refractive index | n = 1.466–1.480 |
| Pleochroism | None |
| References | [3][4][5] |
Faujasite materials are widely synthesized industrially. The relatively low-silica (Si/Al<2) synthetic faujasite is called Zeolite X and the high-silica (Si/Al>2) one is called Zeolite Y. In addition, the aluminum component in zeolite Y can be removed by acid-treatment and/or steam-treatment, and the resulting faujasite is called USY (Ultrastable zeolite Y). USY is used in fluid catalytic cracking process as a catalyst.
Discovery and occurrence
editFaujasite was first described in 1842 from an occurrence in the Limberg Quarries, Sasbach, Kaiserstuhl, Baden-Württemberg, Germany. The sodium modifier faujasite-Na was added following the discovery of the magnesium and calcium rich phases in the 1990s. It was named for Barthélemy Faujas de Saint-Fond (1741–1819), French geologist and volcanologist.[4][5]
Faujasite occurs in vesicles within basalt and phonolite lava and tuff as an alteration or authigenic mineral. It occurs with other zeolites, olivine, augite and nepheline.[3]
Structure
edit.svg)
The faujasite framework has been attributed the code FAU by the International Zeolite Association.[6] It consists of sodalite cages which are connected through hexagonal prisms. The pore, which is formed by a 12-membered ring, has a relatively large diameter of 7.4 Å. The inner cavity has a diameter of 12 Å and is surrounded by 10 sodalite cages. The unit cell is cubic; Pearson symbol cF576, symmetry Fd3m, No. 227,[7] lattice constant 24.7 Å. Of the two types (X and Y) of zeolites coded with FAU, zeolite Y, which is the one with the higher range of silica-to-alumina content, has a void fraction of 48% and a Si/Al ratio of 2.43.[citation needed] It thermally decomposes at 793 °C.[8]
Synthesis
editFaujasite is synthesized, as are other zeolites, from alumina sources such as sodium aluminate and silica sources such as sodium silicate. Other aluminosilicates such as kaolin are used as well. The ingredients are dissolved in a basic environment such as sodium hydroxide aqueous solution and crystallized at 70 to 300 °C (usually at 100 °C). After crystallization the faujasite is in its sodium form and must be ion exchanged with ammonium to improve stability. The ammonium ion is removed later by calcination which renders the zeolite in its acid form. Depending on the silica-to-alumina ratio of their framework, synthetic faujasite zeolites are divided into X and Y zeolites. In X zeolites that ratio is between 2 and 3, while in Y zeolites it is 3 or higher. The negative charges of the framework are balanced by the positive charges of cations (usually either sodium from the NaOH solution, or ammonium or H+ after exchanges) in non-framework positions. Such zeolites have ion-exchange, catalytic and adsorptive properties. The stability of the zeolite increases with the silica-to-alumina ratio of the framework (Lowenstein's rule). It is also affected by the type and amount of cations located in non-framework positions. For catalytic cracking, the Y zeolite is often used in a rare earth-hydrogen exchanged form.[9]
By using thermal, hydrothermal or chemical methods, some of the alumina can be removed from the Y zeolite framework, resulting in high-silica Y zeolites. Such zeolites are used in cracking and hydrocracking catalysts. Complete dealumination results in faujasite-silica.[9]
Use
editFaujasite is used above all as a catalyst in fluid catalytic cracking to convert high-boiling fractions of petroleum crude to more valuable gasoline, diesel and other products. Zeolite Y has superseded zeolite X in this use because it is both more active and more stable at high temperatures due to the higher Si/Al ratio. It is also used in the hydrocracking units as a platinum/palladium support to increase aromatic content of reformulated refinery products.[10]
Type X zeolite can be used to selectively adsorb CO2 from gas streams[11] and is used in the prepurification of air for industrial air separation.
Due to its widely known structure, behaviour and properties, Faujasite is often used as a standard in catalytic and (ad/de)sorption studies on zeolites, along with MFI, FER and CHA[12][13][14][15]
See also
edit- Cu Y Zeolite, copper-containing high-silica derivatives of the faujasite mineral group
References
edit- ^ a b The Faujasite group on Mindat
- ^ Warr, L.N. (2021). "IMA–CNMNC approved mineral symbols". Mineralogical Magazine. 85 (3): 291–320. Bibcode:2021MinM...85..291W. doi:10.1180/mgm.2021.43. S2CID 235729616.
- ^ a b Faujasite. Handbook of Mineralogy.
- ^ a b Faujasite. Mindat.
- ^ a b Faujasite Mineral Data. Webmineral.
- ^ "FAU: Framework Type". asia.iza-structure.org. Retrieved 2020-05-01.
- ^ Hriljac J.A.; Eddy M.M.; Cheetham A.K.; Donohue J.A.; Ray G.J. (1993). "Powder Neutron Diffraction and 29Si MAS NMR Studies of Siliceous Zeolite-Y". Journal of Solid State Chemistry. 106 (1): 66–72. Bibcode:1993JSSCh.106...66H. doi:10.1006/jssc.1993.1265.
- ^ "The Chemical Engineering Zeolite Page". Archived from the original on 2008-09-15. Retrieved 2008-08-03.
- ^ a b Scherzer, Julius (1989). "Octane-Enhancing, Zeolitic FCC Catalysts: Scientific and Technical Aspects". Catalysis Reviews. 31 (3): 215–354. doi:10.1080/01614948909349934.
- ^ Broach, Robert W.; Jan, Deng-Yang; Lesch, David A.; Kulprathipanja, Santi; Roland, Eckehart; Kleinschmit, Peter (2012-04-15). "Zeolites". Ullmann's Encyclopedia of Industrial Chemistry. doi:10.1002/14356007.a28_475.pub2. ISBN 978-3-527-30385-4.
- ^ A1 USA US20020178914 A1, Timothy Golden, "Process for reducing the level of carbon dioxide in a gaseous mixture", published Dec 5, 2002
- ^ Verboekend, D.; Nuttens, N.; Locus, R.; Aelst, J. Van; Verolme, P.; Groen, J. C.; Pérez-Ramírez, J.; Sels, B. F. (2016-06-13). "Synthesis, characterisation, and catalytic evaluation of hierarchical faujasite zeolites: milestones, challenges, and future directions". Chemical Society Reviews. 45 (12): 3331–3352. doi:10.1039/C5CS00520E. hdl:20.500.11850/125146. ISSN 1460-4744. PMID 26313001.
- ^ "FER: Framework Type". europe.iza-structure.org. Retrieved 2023-12-07.
- ^ "CHA: Framework Type". europe.iza-structure.org. Retrieved 2023-12-07.
- ^ "MFI: Framework Type". europe.iza-structure.org. Retrieved 2023-12-07.
Literature
edit- Subhash Bhatia, Zeolite Catalysis: Principles and Applications, CRC Press, Inc., Boca Raton, Florida, 1990.
- Ribeiro, F. R., et al., ed., Zeolites: Science and Technology, Martinus Nijhoff Publishers, The Hague, 1984.