Category Zeolite Crystal system Cubic | Strunz classification 9.GD.30 Space group Fd3m | |
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Formula
(repeating unit) (Na2,Ca,Mg)3.5[Al7Si17O48]·32(H2O) Crystal class Hexoctahedral (m3m)
H–M Symbol (4/m 3 2/m) | ||
Faujasite 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. It occurs as a rare mineral in several locations worldwide and is also synthesized industrially.
Contents
Discovery and occurrence
Faujasite was first described in 1842 for 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.
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.
Structure
The faujasite framework consists of sodalite cages which are connected through hexagonal prisms. The pores are arranged perpendicular to each other. 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, lattice constant 24.7 Å. Zeolite Y has a void fraction of 48% and a Si/Al ratio of 2.43. It thermally decomposes at 793 °C.
Synthesis
Faujasite is synthesized, as are other zeolites, from alumina sources such as sodium aluminate and silica sources such as sodium silicate. Other alumosilicates 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 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. 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.
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.
Use
Faujasite 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.
Type X zeolite can be used to selectively adsorb CO2 from gas streams and is used in the prepurification of air for industrial air separation.