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US5019543A Expired / Lapsed US ⏱️ 0.0 years remaining

High silica crystalline zeolites and process for their preparation

Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1989-07-05
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Granted: 1991-05-28
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Expires: 2009-07-05
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Abstract

Abstract Crystalline aluminosilicate zeolites having increased silica to alumina mole ratios are prepared by a process wherein a conventional crystalline aluminosilicate zeolite is treated to remove alumina from the crystal lattice. By-product non-framework amorphous alumina is then selectively removed from the zeolite either by using a blocking agent, to prevent removal of framework aluminum during a subsequent acid treatment, or by using a selective organic acid extracting agent. The invention is also directed to high silica crystalline zeolites prepared by the present process.

Inventors

  • 👤 Stephen M. Davis
  • 👤 W. Scott Varnado

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 12:15
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/18; B01J29/08; B01J29/70; B01J37/00; B01J37/08; B01J37/10; B01J2229/00; B01J2229/10; B01J2229/16; B01J2229/26; B01J2229/30; B01J2229/42

Claims Analysis

Total Claims: 30
Claim 1
Independent Claim 252 words
A process for increasing the silica to aluminum (Si/Al) mole ratio in the crystal lattice of a crystalline aluminosilicate zeolite, said process comprising: (1) hydrothermally treating said zeilite for a period of time sufficient to effect removal of alumina from said crystal lattice, thereby increasing the Si/Al ratio of the zeilite and forming a non-framework amorphous phase alumina by-product on said zeolite; and (2) extracting the amorphous phase alumina selectively with respect to the alumina in said crystal lattice of said zeolite to produce a zeolite product substantially retaining its degree of framework crystallinity with respect to the dealuminized zeolite produced in step (1), said extracting step being carried out by one of the following processes: a) contacting the treated zeolite of step (1) with a solution of an organic acid selected from the group consisting of Cl x F 3-x COOH, RCF 2 COOH or RCCl 2 COOH, wherein x is 1, 2 or 3 and R is phenyl or an alkyl group having from 1 to 10 carbon atoms, for a sufficient time and under process conditions suitable to remove a substantial portion of the amorphous phase alumina from said zeolite; or alternatively b) loading the treated zeolite of step (1) with an organic blocking agent to block access to the framework aluminum centers of the zeolite, and contacting said blocked zeolite with a solution of an extracting agent for sufficient time and under process conditions suitable to remove a substantial portion of the amorphous phase alumina from said zeolite.
Claim 2
Dependent Claim 252 words
A process for increasing the silica to aluminum (Si/Al) mole ratio in the crystal lattice of a crystalline aluminosilicate zeolite, said process comprising: (1) hydrothermally treating said zeilite for a period of time sufficient to effect removal of alumina from said crystal lattice, thereby increasing the Si/Al ratio of the zeilite and forming a non-framework amorphous phase alumina by-product on said zeolite; and (2) extracting the amorphous phase alumina selectively with respect to the alumina in said crystal lattice of said zeolite to produce a zeolite product substantially retaining its degree of framework crystallinity with respect to the dealuminized zeolite produced in step (1), said extracting step being carried out by one of the following processes: a) contacting the treated zeolite of step (1) with a solution of an organic acid selected from the group consisting of Cl x F 3-x COOH, RCF 2 COOH or RCCl 2 COOH, wherein x is 1, 2 or 3 and R is phenyl or an alkyl group having from 1 to 10 carbon atoms, for a sufficient time and under process conditions suitable to remove a substantial portion of the amorphous phase alumina from said zeolite; or alternatively b) loading the treated zeolite of step (1) with an organic blocking agent to block access to the framework aluminum centers of the zeolite, and contacting said blocked zeolite with a solution of an extracting agent for sufficient time and under process conditions suitable to remove a substantial portion of the amorphous phase alumina from said zeolite.
Claim 3
Dependent Claim 17 words
The process of claim 1, wherein the unit cell size of the zeolite product is below 24.5.
Claim 4
Dependent Claim 18 words
The process of claim 1, wherein the unit cell size of the zeolite product is 24.5 to 24.2.
Claim 5
Dependent Claim 31 words
The process of claim 1, wherein said hydrothermal treating is performed at a temperature within the range of about 800° to 1500° F. in an atmosphere containing at least 2% water.
Claim 6
Dependent Claim 28 words
The process of claim 1, wherein the temperature, time, and water content is such to obtain a Si/Al ratio of the zeolite product of at least about 8.
Claim 7
Dependent Claim 17 words
The process of claim 1 wherein the zeolite treated in step (1) is a faujasite type zeolite.
Claim 8
Dependent Claim 24 words
The process of claim 1 wherein said zeolite treated in step (1) has an initial silica to alumina ratio of about 2.0 to 8.
Claim 9
Dependent Claim 20 words
The process of claim 7, wherein said zeolite has an initial silica to alumina ratio of about 2.5 to 5.
Claim 10
Dependent Claim 19 words
The process of claim 1 wherein the selectivity for removing non-framework alumina over framework alumina is at least 3:1.
Claim 11
Dependent Claim 19 words
The process of claim 9, wherein the selectivity for removing non-framework alumina over framework alumina is at least 5:1.
Claim 12
Dependent Claim 20 words
The process of claim 1, wherein less than about 5 percent by weight of the zeolite product is non-framework alumina.
Claim 13
Dependent Claim 20 words
The process of claim 1, wherein less than about 2 percent by weight of the zeolite product is non-framework alumina.
Claim 14
Dependent Claim 17 words
The process of claim 1, wherein the amorphous alumina is selectively extracted in accordance with process (a).
Claim 15
Dependent Claim 12 words
The process of claim 13, wherein the organic acid is trichloroacetic acid.
Claim 16
Dependent Claim 25 words
The process of claim 1, wherein the selective extraction is accomplished by using an organic blocking agent prior to extraction in accordance with process (b).
Claim 17
Dependent Claim 21 words
The process of claim 15, wherein the blocking agent comprises a hydrocarbon having 10 to 20 carbon atoms or mixtures thereof.
Claim 18
Dependent Claim 15 words
The process of claim 16, wherein the blocking agent comprises paraffins, olefins, or mixtures thereof.
Claim 19
Dependent Claim 25 words
The process of claim 15, wherein the blocking agent comprises a hydrocarbonaceous coke deposit produced by heating the zeolite in the presence of a hydrocarbon.
Claim 20
Dependent Claim 23 words
The process of claim 1, wherein the sodium content of the zeolite product is less than or equal to about 0.3 weight percent.
Claim 21
Dependent Claim 20 words
The process of claim 1 where said zeolite product has a final Si/Al mole ratio of about 8 to 50.
Claim 22
Dependent Claim 20 words
The process of claim 1, wherein the zeolite product of step (2) is subsequently ionexchanged or treated with an additive.
Claim 23
Dependent Claim 18 words
The process of claim 21, wherein the additive is a catalytic metal employed in hydrocracking, reforming, or hydrotreating.
Claim 24
Dependent Claim 18 words
The process of claim 21, wherein the additive is an aluminosilicate additive used to make a composite catalyst.
Claim 25
Dependent Claim 16 words
The process of claim 1, wherein the zeolite treated in step (1) is a Y-type zeolite.
Claim 26
Dependent Claim 26 words
The process of claim 14 wherein the concentration of said acid in solution is within the range of from about 0.1 up to about 0.4 M.
Claim 27
Dependent Claim 12 words
The process of claim 15 wherein said extracting agent is hydrochloric acid.
Claim 28
Dependent Claim 24 words
The process of claim 15 wherein said zeolite treated in step (1) has an initial silica to alumina ratio of about 2.0 to 8.
Claim 29
Dependent Claim 18 words
The process of claim 15 wherein said blocking agent is removed from said zeolite after said extraction step.
Claim 30
Dependent Claim 23 words
The process of claim 28 wherein said blocking agent is removed by heating the zeolite at high temperatures in the presence of oxygen.

References Cited (Backward Citations)

US4093560A Cited
US4840930A Cited
US4533533A Cited
US4512961A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-05-27 1994-11-26 1995-05-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-05-27 1998-11-26 1999-05-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-05-27 2002-11-26 2003-05-28 $7700.00 Window Closed / Lapsed

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