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US4388218A Expired / Lapsed US ⏱️ 0.0 years remaining

Regeneration of cracking catalyst in two successive zones

Assignee: Imperial Chemical Industries Ltd
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Filing: 1981-09-22
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Granted: 1983-06-14
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Expires: 2001-09-22
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Abstract

Abstract Process and apparatus suitable for the regeneration of catalytic cracking catalyst particles and for the heating and partial conversion of coke particles from a coking process are described. The particles are heated in two successive zones, for example formed by two fluidized beds, conditions being controlled so that (1) only partial regeneration of catalyst particles or conversion of coke particles occurs in the first zone, and (2) there is no major evolution of heat from either zone.

Inventors

  • 👤 Frederick Rowe

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 18:25
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/26; B01J8/28; B01J23/00; B01J23/90; C; C10; C10G; C10G11/00; C10G11/14; C10G11/16; C10G11/18; C10G9/00; C10G9/28; C10G9/32

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 227 words
A process for treating solid particles of partially or completely deactivated cracking catalyst which process comprises: (1) passing said solid particles into a first fluidized bed reactor and therein contacting the solid particles at elevated temperatures with a first gas stream consisting essentially of (a) oxygen plus steam, (b) oxygen plus carbon dioxide, or (c) oxygen plus steam plus carbon dioxide and adjusting the ratio of oxygen to steam and/or carbon dioxide so that some carbon is removed form the solid particles without major net evolution of heat in the first reactor, thereby partially regenerating the said cracking catalyst particles to produce synthesis gas containing a mixture of steam, carbon monoxide, carbon dioxide and hydrogen, and thereafter (2) passing the thus-treated solid particles from the base of said first fluidized bed reactor downwardly by gravity to the top of a second fluidized bed reactor and therein contacting the solid particles at elevated temperature wih a second gas stream comprising oxygen thereby substantially completely regenerating the said cracking catalyst particles and removing the regenerated catalyst from the base of the second fluidized bed reactor, provided that the first fluidized bed reactor is disposed substantially vertically above the second fluidized bed reactor located within one vessel, the contacting and the reactions occurring in both reactors being controlled so that there is no major evolution of heat from either reactor.
Claim 2
Dependent Claim 227 words
A process for treating solid particles of partially or completely deactivated cracking catalyst which process comprises: (1) passing said solid particles into a first fluidized bed reactor and therein contacting the solid particles at elevated temperatures with a first gas stream consisting essentially of (a) oxygen plus steam, (b) oxygen plus carbon dioxide, or (c) oxygen plus steam plus carbon dioxide and adjusting the ratio of oxygen to steam and/or carbon dioxide so that some carbon is removed form the solid particles without major net evolution of heat in the first reactor, thereby partially regenerating the said cracking catalyst particles to produce synthesis gas containing a mixture of steam, carbon monoxide, carbon dioxide and hydrogen, and thereafter (2) passing the thus-treated solid particles from the base of said first fluidized bed reactor downwardly by gravity to the top of a second fluidized bed reactor and therein contacting the solid particles at elevated temperature wih a second gas stream comprising oxygen thereby substantially completely regenerating the said cracking catalyst particles and removing the regenerated catalyst from the base of the second fluidized bed reactor, provided that the first fluidized bed reactor is disposed substantially vertically above the second fluidized bed reactor located within one vessel, the contacting and the reactions occurring in both reactors being controlled so that there is no major evolution of heat from either reactor.
Claim 3
Dependent Claim 34 words
A process as claimed in claim 1 in which the solid particles are discharged from the second zone at a temperature which is substantially the same as that used in a catalytic cracking process.
Claim 4
Dependent Claim 19 words
A process as claimed in claim 1 in which the second gas stream comprising oxygen is an air stream.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-06-13 1986-12-13 1987-06-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-06-13 1990-12-13 1991-06-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-06-13 1994-12-13 1995-06-14 $7700.00 Window Closed / Lapsed

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