Claims
- 1. An aluminum deficient crystalline aluminosilicate zeolite having the crystal structure of a faujasite and having a composition, in its anhydrous state, in terms of mole ratio of oxides, as represented by the following formula:
- (1-Z) (aM.sub.2 O+bR.sub.2 O+3wRE.sub.2 O.sub.3) . (1-Z)Al.sub.2 O.sub.3.XSiO.sub.2
- wherein RE represents a cation of a single rare earth metal or of a mixture of rare earth metals, wherein "w" ranges from a value of about 0.054 to about 0.217, said value w being the minimum amount of rare earth in said zeolite needed to stabilize said aluminum deficient zeolite; where R is an alkali metal cation; where M is selected from the group consisting of hydrogen ion, ammonium ion and mixtures thereof, wherein "a" ranges from zero to 1-3w; wherein "b" ranges from zero to 1-3w; wherein a+b+3w=1; wherein Z ranges from about 0.92 to 0.27, said value Z being the maximum fraction of alumina in the crystal structure that can be removed, and wherein X ranges from about 3.9 to about 54, said zeolite having a unit cell size ranging from about 24.25 to about 24.75 Angstroms, said zeolite having a unit cell size greater than the stoichiometric unit cell size when measured after heating for two hours at 1300.degree. F., said zeolite falling within the area of FIG. 1 designated "stabilized zone".
- 2. The zeolite of claim 1 wherein said zeolite is composited with catalytic metals of Group IB, IIA, IIB, IIIB, IVA, IVB, VB, VIB, VIIB, VIII and mixtures thereof of the Periodic Table of Elements.
- 3. The zeolite of claim 1 wherein X equals 3.9 and said unit cell size is 24.75 Angstroms.
- 4. The zeolite of claim 1 wherein X equals 54 and said cell size is 24.25 Angstroms.
- 5. The zeolite of claim 1 wherein said zeolite is represented by the formula:
- 0.20(NH.sub.4).sub.2 O.0.05Na.sub.2 O.0.25RE.sub.2 O.sub.3.Al.sub.2 O.sub.3.9SiO.sub.2.
- 6. The zeolite of claim 1 having been prepared by the steps which comprise:
- (a) contacting a Y-type zeolite with a dealuminating agent for a time sufficient to remove at least about 5% of the aluminum atoms from said zeolite;
- (b) contacting the resulting dealuminized zeolite with a fluid medium comprising rare earth metal cations to produce a rare earth metal exchanged zeolite; and
- (c) calcining the rare earth exchanged zeolite to produce said aluminum deficient rare earth stabilized zeolite.
- 7. A method for the preparation of an aluminum deficient rare earth stabilized crystalline aluminosilicate zeolite, which comprises the steps of:
- (a) treating an initial Y-type crystalline aluminosilicate zeolite with a dealuminizing agent, said initial zeolite having the crystal structure of faujasite and having a composition, in its anhydrous state, in terms of mole ratios of oxides, represented by the formula:
- (aM.sub.2 O+bR.sub.2 O) . Al.sub.2 O.sub.3.XSiO.sub.2
- wherein R represents an alkali metal cation; wherein M is a cation selected from the group consisting of hydrogen cation, ammonium cation, and mixtures thereof; wherein a+b =1; wherein "a" ranges from 0 to 1; wherein "b" ranges from 0 to 1; and wherein X ranges from 3.9 to 54; said zeolite having a unit cell size ranging from about 24.25 to about 24.75 Angstroms, said zeolite being treated at conditions and for a time sufficient to remove at least 5 percent of said aluminum from the structure of said zeolite;
- (b) contacting said zeolite during step (a) or after step (a) with an ion exchange medium comprising a rare earth metal cation to replace at least a portion of said M or R cation with a rare earth metal cation; and
- (c) recovering an aluminum deficient rare earth stabilized crystalline aluminosilicate represented by the formula of claim 1, and having a unit cell size greater than the stoichiometric unit cell size when measured after heating for two hours at 1300.degree. F., and falling within the area of FIG. 1 designated "stabilized zone".
- 8. The method of claim 7 wherein said dealuminating agent is selected from the groups consisting of organic acids, inorganic acids, chelating agents and mixtures thereof.
- 9. The method of claim 7 wherein step (a) is conducted at a temperature ranging from 150 to 220.degree. F. to remove at least about 5 percent of said aluminum from said crystal structure.
- 10. The method of claim 7 where said step (b) is conducted at a temperature ranging from about 60.degree. F. to about 220.degree. F.
- 11. The method of claim 7 wherein said initial zeolite has a silica to alumina mole ratio ranging from about 3.9 to about 54 and a unit cell size ranging from about 24.75 to about 24.25 Angstroms.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a continuation-in-part application of U.S. patent application Ser. No. 685,797 filed Dec. 24, 1984, and now abandoned which is a Rule 60 Divisional application of U.S. patent application Ser. No. 560,558 filed Dec. 12, 1983, and now abandoned the teachings of both of which are hereby incorporated by reference. Also related is U.S. patent application Ser. No. 715,601 filed Mar. 25, 1985 and now abandoned which is a continuation-in-part of U.S. patent application Ser. No. 560,558 now abandoned.
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Divisions (1)
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Number |
Date |
Country |
Parent |
560558 |
Dec 1983 |
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Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
685797 |
Dec 1984 |
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