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

Catalytic cracking with reduced emission of noxious gases

Patent 4153535 Issued on May 8, 1979. Estimated Expiration Date: Icon_subject December 8, 1996. 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

931515

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Inventors

Assignee

Application

No. 05/748555 filed on 12/08/1976

US Classes:

208/120.05, With group VII metal or metal oxide (i.e., Mn, Tc, Re, or oxide thereof)208/120.1, With group IV metal or metal oxide (i.e., Ti, Zr, Hf, Ge, Sn, Pb, or oxide thereof)208/120.15, With group I metal or metal oxide (i.e., alkali metal, Ag, Au, Cu, or oxide thereof)208/120.25, With group II metal or metal oxide (i.e., alkaline earth metal, Be, Mg, Zn, Cd, Hg, or oxide thereof)208/164, Solids transferring423/244.1, Transition metal or compound thereof catalyst502/42And substantially complete oxidation of carbon monoxide to carbon dioxide within regeneration zone

Examiners

Primary: Vertiz, O. R.
Assistant: Straub, Gary P.

Attorney, Agent or Firm

International Classes

C10G 11/00 (20060101)
C10G 11/18 (20060101)
C10G 11/05 (20060101)
B01J 8/24 (20060101)
B01J 8/28 (20060101)
B01J 29/06 (20060101)
B01J 29/00 (20060101)

Abstract

A cyclic, fluidized catalytic cracking process providing reduced emissions of noxious effluents in regeneration zone flue gases is operated with homogeneous or non-homogeneous, regenerable, fluidized, solid particles which are circulated throughout the catalytic cracking process cycle and which comprise (1) a molecular sieve-type cracking catalyst, comprising a cracking catalyst matrix containing crystalline aluminosilicate distributed throughout said matrix and (2) a metallic reactant which reacts with a sulfur oxide to form a metal- and sulfur-containing compound in the solid particles. The method involves regeneration of the cracking catalyst in the presence of a metallic oxidation promoter which can also be a component of the solid particles.

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