U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Zeolite aggregates and catalysts

Patent 5348924 Issued on September 20, 1994. Estimated Expiration Date: Icon_subject February 23, 2013. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

2865866

3216789

3326818

3557024

Method of manufacturing an extruded catalyst composition
Patent #: 4046713
Issued on: 09/06/1977
Inventor: Mitsche ,   et al.

Method of dehydrocyclizing aliphatic hydrocarbons
Patent #: 4104320
Issued on: 08/01/1978
Inventor: Bernard ,   et al.

Stabilized reforming catalyst
Patent #: 4305811
Issued on: 12/15/1981
Inventor: Johnson

Solvent deasphalting by polarity gradient extraction
Patent #: 4305812
Issued on: 12/15/1981
Inventor: Shih ,   et al.

Stabilized reforming catalyst
Patent #: 4306963
Issued on: 12/22/1981
Inventor: Johnson

Stabilized reforming catalyst
Patent #: 4311582
Issued on: 01/19/1982
Inventor: Johnson ,   et al.

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Inventors

Assignee

Application

No. 023733 filed on 02/23/1993

US Classes:

502/66, And Group VIII (Iron Group or Platinum Group) metal containing502/10, Treating preformed sphere only502/64, Zeolite502/69Heterogeneous arrangement

Examiners

Primary: Dees, Carl F.

Attorney, Agent or Firm

Foreign Patent References

  • 0220616 EP. 05/20/1987
  • 0314336 EP. 05/20/1989
  • 2106413 GB. 04/20/1983

International Classes

B01J 029/04
B01J 020/18
B01J 037/00

Abstract

A process for producing zeolite aggregates involves providing a formable paste composed of zeolite, a binder composed of an organic/metal oxide containing aluminum, a peptizing agent and water; forming the paste into an aggregate, preferably by extruding into an extrudate; curing the aggregate; hydro-thermally calcining the aggregate; and washing the hydro-thermally calcined aggregate with a washing medium, preferably followed by rinsing with a rinsing medium to remove residual washing medium from the aggregate. The washed and rinsed aggregate may then be permitted to equilibrate or is subjected to a drying procedure. Preferably, the washed and rinsed aggregate is again subjected to curing/hydro-thermal calcining. The resultant aggregates, such as extrudates, have an exterior surface with openings and interstitial spaces between particles of binder and zeolite which communicate by such openings between the exterior surface of the aggregate and micropores of the zeolite; the aggregates also exhibit characteristics of crush strength greater than about 0.9 pounds per millimeter and a loss by attrition of less than about 3.0%. Regenerable catalysts, such as reforming catalysts, based on such aggregate also exhibit a catalyst activity pass through to the zeolite bound in the aggregate of at least 70% of the initial catalyst activity of freshly prepared zeolite, as well as exhibiting more than about 70% of the reforming benzene yield that the reforming catalyst exhibited when similarly tested prior to being exposed to a hydrocarbon stream under specified reforming conditions of the catalyst activity test procedures.

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