← Back to Patent Explorer
US5508019A Expired / Lapsed US ⏱️ 0.0 years remaining

Dealumination of aluminosilicates

Assignee: Lyondell Chemical Technology LP
•
Filing: 1994-06-30
•
Granted: 1996-04-16
•
Expires: 2014-06-30
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Crystalline aluminosilicates such as zeolite beta may be readily dealuminated using organic sulfonic acids such as methanesulfonic acid to provide useful catalysts or catalyst precursors. A high degree of aluminum removal with minimal loss of crystallinity is possible even when an organic template is not present in the starting aluminosilicate.

Inventors

  • 👤 Robert J. Saxton
  • 👤 Guy L. Crocco
  • 👤 John G. Zajacek

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 19:27
CPC Classifications
C; C01; C01B; C01B37/00; C01B37/02; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/70; B01J29/7007; C01B39/00; C01B39/02; C01B39/026; B01J2229/00; B01J2229/10; B01J2229/16; B01J2229/30; B01J2229/34; B01J2229/37; Y; Y10; Y10S; Y10S423/00; Y10S423/27

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 87 words
A method of removing framework aluminum from a zeolite beta, said method comprising contacting the zeolite beta with a water-soluble organic sulfonic acid, wherein the water-soluble organic sulfonic acid is present at a concentration of at least 2N in an aqueous medium, at a temperature of from 20° C. to 200° C. to form a dealuminated zeolite beta having a framework Si/Al ratio of at least 800 and a crystallinity of at least 90% relative to the crystallinity of the zeolite beta prior to said acid treatment.
Claim 2
Independent Claim 87 words
A method of removing framework aluminum from a zeolite beta, said method comprising contacting the zeolite beta with a water-soluble organic sulfonic acid, wherein the water-soluble organic sulfonic acid is present at a concentration of at least 2N in an aqueous medium, at a temperature of from 20° C. to 200° C. to form a dealuminated zeolite beta having a framework Si/Al ratio of at least 800 and a crystallinity of at least 90% relative to the crystallinity of the zeolite beta prior to said acid treatment.
Claim 3
Dependent Claim 14 words
The method of claim 1 wherein the water-soluble organic sulfonic acid is methanesulfonic acid.
Claim 4
Dependent Claim 20 words
The method of claim 1 wherein the water-soluble organic sulfonic acid is present at a concentration of at least 5N.
Claim 5
Dependent Claim 26 words
The method of claim 1 comprising an additional step of contacting the dealuminated zeolite beta with a titanium compound to form a titanium substituted zeolite beta.
Claim 6
Dependent Claim 16 words
The method of claim 1 wherein the zeolite beta is essentially free of a structuring agent.
Claim 7
Dependent Claim 19 words
The method of claim 1 wherein the water-soluble organic sulfonic acid has a pk a of less than 1.
Claim 8
Dependent Claim 42 words
The method of claim 1 wherein the water soluble organic sulfonic acid is selected from the group consisting of benzenesulfonic acid, methanesulfonic acid, p-toluenesulfonic acid, ethanesulfonic acid, trifluoromethane sulfonic acid, propanesulfonic acid, butanesulfonic acid, xylenesulfonic acid, trichloromethane sulfonic acid, and mixtures thereof.
Claim 9
Dependent Claim 19 words
The method of claim 1 comprising an additional step of separating the dealuminated zeolite beta from the aqueous medium.
Claim 10
Dependent Claim 17 words
The method of claim 8 comprising an additional step of washing the dealuminated zeolite beta with water.
Claim 11
Dependent Claim 17 words
The method of claim 9 comprising an additional step of drying the dealuminated zeolite beta after washing.
Claim 12
Dependent Claim 12 words
The method of claim 8 wherein the separated aqueous medium is recycled.
Claim 13
Dependent Claim 15 words
The method of claim 1 wherein said temperature is from 40° C. to 120° C.
Claim 14
Dependent Claim 13 words
The method of claim 1 wherein said contacting is performed in multiple stages.
Claim 15
Dependent Claim 14 words
The method of claim 1 wherein said contacting is performed in a single stage.
Claim 16
Independent Claim 107 words
A method of removing framework aluminum from a zeolite beta, said method comprising contacting the zeolite beta with a water-soluble organic sulfonic acid having the structure RSO 3 H wherein R is C 1 -C 20 alkyl or C 6 -C 20 aryl, wherein the water soluble organic sulfonic acid is present at a concentration of at least 5N in an aqueous medium, at a temperature of 40° C. to 120° C. to form a dealuminated zeolite beta having a framework Si/Al ratio of at least 800 and a crystallinity of at least 90% relative to the crystallinity of the zeolite beta prior to said acid treatment.
Claim 17
Independent Claim 107 words
A method of removing framework aluminum from a zeolite beta, said method comprising contacting the zeolite beta with a water-soluble organic sulfonic acid having the structure RSO 3 H wherein R is C 1 -C 20 alkyl or C 6 -C 20 aryl, wherein the water soluble organic sulfonic acid is present at a concentration of at least 5N in an aqueous medium, at a temperature of 40° C. to 120° C. to form a dealuminated zeolite beta having a framework Si/Al ratio of at least 800 and a crystallinity of at least 90% relative to the crystallinity of the zeolite beta prior to said acid treatment.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1999-04-16 1999-10-16 2000-04-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2003-04-16 2003-10-16 2004-04-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2007-04-16 2007-10-16 2008-04-16 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag