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Shape selective catalyst from zeolite alpha and use thereof

Assignee: Mobil Oil AS
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Filing: 1979-09-12
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Granted: 1981-11-10
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Expires: 1999-09-12
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Abstract

Abstract A method is provided for preparing a synthetic crystalline aluminosilicate zeolite Alpha containing platinum-group metal within the zeolite pores as synthesized, thereby providing shape-selective hydrogenation activity. The method comprises synthesizing the zeolite from a reaction mixture of controlled composition including a source of a cationic platinum-group metal complex. Catalysts made with the zeolite synthesized in accordance hereto are stable, both thermally and in the presence of steam, and exhibit beneficial shape-selectivity in catalysis and absorption.

Inventors

  • 👤 Guenter H. Kuehl

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 15:22
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/58; C10G45/60; C10G45/64; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/70; B01J29/72; B01J29/74; B01J31/00; B01J31/02; B01J31/0234; B01J31/0235; B01J31/0254; B01J2229/00; B01J2229/30; B01J2229/40; B01J31/0239; Y; Y10; Y10S; Y10S423/00; Y10S423/24

Claims Analysis

Total Claims: 21
Claim 1
Independent Claim 229 words
A catalyst produced by a method for synthesizing crystalline alumino-silicate zeolite Alpha containing platinum-group metal within the zeolite pores which comprises the steps of preparing a reaction mixture containing sources of sodium oxide, tetramethylammonium oxide, aluminum oxide, silicon dioxide, a cationic platinum-group metal complex and water and having a composition, in terms of mole ratios of oxides, falling within the following ranges: SiO 2 /Al 2 O 3 =4.0-12.0 H 2 O/(Na 2 O+R 2 O)=15.0-40.0 (Na 2 O+R 2 O)/Al 2 O 3 =2.0-7.0 Na 2 O/(Na 2 O+R 2 O)=0.2-0.75 M/Al 2 O 3 =10 -6 -0.06 wherein R is a tetramethylammonium cation and M is a platinum-group metal, aging said mixture for from about 2 hours to about 100 hours at a temperature of from about 10° C. to about 70° C., and then heating said mixture at a temperature of from about 80° C. to about 150° C. until crystals of said zeolite are formed, and which comprises the further step of replacing, at least in part, the original sodium cations of said zeolite by ion exchange with a cation or a mixture of cations selected from the group consisting of hydrogen and metals from Groups IIA, IVA, IB, IIB, IIIB, VIB, and VIIB of the Periodic Table of Elements, and then heating said zeolite at a temperature from 480° C. to about 820° C.
Claim 2
Dependent Claim 229 words
A catalyst produced by a method for synthesizing crystalline alumino-silicate zeolite Alpha containing platinum-group metal within the zeolite pores which comprises the steps of preparing a reaction mixture containing sources of sodium oxide, tetramethylammonium oxide, aluminum oxide, silicon dioxide, a cationic platinum-group metal complex and water and having a composition, in terms of mole ratios of oxides, falling within the following ranges: SiO 2 /Al 2 O 3 =4.0-12.0 H 2 O/(Na 2 O+R 2 O)=15.0-40.0 (Na 2 O+R 2 O)/Al 2 O 3 =2.0-7.0 Na 2 O/(Na 2 O+R 2 O)=0.2-0.75 M/Al 2 O 3 =10 -6 -0.06 wherein R is a tetramethylammonium cation and M is a platinum-group metal, aging said mixture for from about 2 hours to about 100 hours at a temperature of from about 10° C. to about 70° C., and then heating said mixture at a temperature of from about 80° C. to about 150° C. until crystals of said zeolite are formed, and which comprises the further step of replacing, at least in part, the original sodium cations of said zeolite by ion exchange with a cation or a mixture of cations selected from the group consisting of hydrogen and metals from Groups IIA, IVA, IB, IIB, IIIB, VIB, and VIIB of the Periodic Table of Elements, and then heating said zeolite at a temperature from 480° C. to about 820° C.
Claim 3
Dependent Claim 19 words
A catalyst according to claim 1 wherein the heating step is maintained between about 90° C. and 120° C.
Claim 4
Dependent Claim 25 words
A catalyst according to claim 1 wherein the silicon dioxide comprises a finely dispersed silica obtained by precipitation from an aqueous solution of a silicate.
Claim 5
Dependent Claim 24 words
A catalyst according to claim 1 wherein the silicon dioxide comprises a finely dispersed silica obtained by vapor phase hydrolysis of a silicon halide.
Claim 6
Dependent Claim 15 words
A catalyst according to claim 1 wherein the silicon dioxide comprises a colloidal silica sol.
Claim 7
Dependent Claim 17 words
A catalyst according to claim 1 wherein the temperature of said further step is approximately 550° C.
Claim 8
Dependent Claim 17 words
A catalyst according to claim 2 wherein the temperature of said further step is approximately 550° C.
Claim 9
Dependent Claim 17 words
A catalyst according to claim 3 wherein the temperature of said further step is approximately 550° C.
Claim 10
Dependent Claim 17 words
A catalyst according to claim 4 wherein the temperature of said further step is approximately 550° C.
Claim 11
Dependent Claim 17 words
A catalyst according to claim 5 wherein the temperature of said further step is approximately 550° C.
Claim 12
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 1.
Claim 13
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 2.
Claim 14
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 3.
Claim 15
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 4.
Claim 16
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 5.
Claim 17
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 6.
Claim 18
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 7.
Claim 19
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 8.
Claim 20
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 9.
Claim 21
Dependent Claim 30 words
The process of catalytically converting an organic compound charge which comprises contacting said charge under organic compound conversion conditions with a catalyst comprising a zeolite synthesized as in claim 10.

References Cited (Backward Citations)

US2882243A Cited
US3314752A Cited
US3375205A Cited
US3373109A Cited
US4191663A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-11-09 1985-05-11 1985-11-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-11-09 1989-05-11 1989-11-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-11-09 1993-05-11 1993-11-10 $7700.00 Window Closed / Lapsed

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