US5013699A
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US
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Novel zeolite compositions derived from zeolite Y
Assignee: Honeywell UOP LLC
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Filing: 1989-10-05
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Granted: 1991-05-07
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Expires: 2009-10-05
Abstract
Abstract Novel catalyst bases are described which are prepared by hydrothermally treating an ammonium ion exchanged sodium Y zeolite followed by low pH ammonium ion exchange to produce highly crystalline zeolite catalyst base. Catalysts incorporating such novel zeolite catalyst bases, as well as hydrocracking and fluid catalytic cracking processes for the production of gasoline products utilizing catalysts incorporating such novel catalyst bases, are also described.
Inventors
- 👤 James G. Vassilakis
- 👤 Donald F. Best
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 07:42
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/08; B01J29/084; B01J29/80; C; C10; C10G; C10G11/00; C10G11/02; C10G11/04; C10G11/05; C10G47/00; C10G47/02; C10G47/10; C10G47/12; C10G47/16; B01J2229/00; B01J2229/10; B01J2229/16; B01J2229/30; B01J2229/36; B01J2229/38; B01J29/70
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
152 words
A zeolite composition prepared by the process comprising the steps of: (a) providing a crystalline sodium zeolite Y starting composition and contacting said starting composition with ammonium cations under cation exchange conditions to reduce the Na 2 O content of the starting composition to less than 3.0 weight percent; (b) hydrothermally steaming the ammonium exchanged zeolite Y of step (a) at a temperature of from 550° C. to about 850° C. to reduce the unit cell dimension of the crystal lattice; (c) contacting the steamed product of step (b) with a sufficient amount of an aqueous solution of ammonium ions having a pH of less than about 4.0 and for a sufficient time to exchange at least some of the residual sodium cations and to increase the bulk Si/Al 2 ratio of the composition to the range of 6.5 to 20; and (d) recovering the ion-exchanged and extracted product of step (c).
Claim 2
Dependent Claim
152 words
A zeolite composition prepared by the process comprising the steps of: (a) providing a crystalline sodium zeolite Y starting composition and contacting said starting composition with ammonium cations under cation exchange conditions to reduce the Na 2 O content of the starting composition to less than 3.0 weight percent; (b) hydrothermally steaming the ammonium exchanged zeolite Y of step (a) at a temperature of from 550° C. to about 850° C. to reduce the unit cell dimension of the crystal lattice; (c) contacting the steamed product of step (b) with a sufficient amount of an aqueous solution of ammonium ions having a pH of less than about 4.0 and for a sufficient time to exchange at least some of the residual sodium cations and to increase the bulk Si/Al 2 ratio of the composition to the range of 6.5 to 20; and (d) recovering the ion-exchanged and extracted product of step (c).
Claim 3
Dependent Claim
49 words
Zeolite composition according to claim 1 wherein in the step (a) the Na 2 O content of the product of step (a) is less than 2.5 weight percent and wherein in step (b) the hydrothermal steaming is carried out using 100% steam for a period of about one hour.
Claim 4
Dependent Claim
28 words
Zeolite composition according to claim 2 wherein in step (b) the hydrothermal steaming is carried out at a temperature of from about 600° C. to about 725° C.
Claim 5
Dependent Claim
49 words
Zeolite composition according to claim 1 wherein the product recovered in step (d) has a unit cell dimension in the range of 24.34 to 24.58 Angstroms, a crystallinity of 85-100%, a bulk Si/Al 2 molar ratio of 8.0-18.0 and a surface area of greater than 735 m 2 /g.
Claim 6
Dependent Claim
27 words
Zeolite composition according to claim 1 which contains rare earth cations by virtue of contacting the product of step (a) with rare earth cations under ion-exchange conditions.
Claim 7
Dependent Claim
46 words
Zeolite composition according to claim 5 wherein the rare earth exchange step is carried out be contacting a mixed rare earth chloride containing approximately 60% La 2 O 3 with the NH 4 Y in an aqueous slurry which has been heated to about 85-90° C.
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