Treating cracking catalyst fines containing a passivating material

• US 4,348,273 A
• Filed: 06/25/1980
• Issued: 09/07/1982
• Est. Priority Date: 06/25/1980
• Status: Expired due to Term

• Current Assignee: Phillips Petroleum Company (ConocoPhillips)
• Original Assignee: Phillips Petroleum Company (ConocoPhillips)
• Inventors: Nielsen, Richard H.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): Schmitkons, G. E.
• Application Number:
  US06/163,004
• Time in Patent Office: 804 Days
• Field of Search: 208/113, 208/127, 208/120, 208/52 CT, 208/152, 405/128, 405/129, 252/411 R
• US Class Current: 208/113
• CPC Class Codes: C10G 11/02 characterised by the catalyst used
• CPC Class Codes: C10G 11/18 according to the "fluidised-bed" technique

Abstract

In a hydrocarbon conversion operation employing a fluidized cracking catalyst wherein the cracking catalyst has been passivated to render contaminating metals thereon substantially inactive thus to avoid undesired reactions and wherein the used catalyst is regenerated and the regeneration step yields catalyst fines and a flue gas and the flue gas and fines are separated in at least two stages a first stage yielding coarse fines and a later stage yielding finer fines the step of treating finer fines to render metals thereon non-leachable or having substantially reduced leachability to render the finer fines usable as land fill which comprises treating the finer fines with a tin and/or indium and/or a compound of tin and/or a compound of indium.

Claims

1. A process comprising:

(a) cracking a hydrocarbon oil in a cracking zone in the presence of a cracking catalyst;

wherein said catalyst becomes contaminated with a contaminant that is a member of the group consisting of vanadium, chromium, iron, cobalt, copper, arsenic, antimony, platinum, bismuth and compounds thereof;

(b) regenerating, in a regeneration zone, said cracking catalyst;

(c) passing from said regeneration zone gas and fines of said catalyst to a first separation zone.

(d) separating, in said first separation zone, coarser fines of said catalyst from finer fines of said catalyst;

wherein said finer fines are contaminated with more, on a weight percent basis, of said contaminant than are said coarser fines;

(e) recycling said coarser fines to said cracking zone;

(f) separating, in a second separation zone, said gas from said finer fines; and

(g) treating said finer fines with a stabilizing agent in an amount sufficient to improve the stability of said contaminant against leaching by water;

wherein said stabilizing agent is a member of the group consisting of indium, tin and compounds thereof.

2. A process in accordance with claim 1 wherein said contaminant is a member of the group consisting of antimony and compounds thereof.

3. A process in accordance with claim 1 or 2 wherein said stabilizing agent is a member of the group consisting of a water insoluble oxide of indium and a water insoluble sulfide of indium.

5. A process in accordance with claim 1 or 2 wherein said stabilizing agent is a member of the group consisting of a water insoluble oxide of tin and a water insoluble sulfide of tin.

6. A process in accordance with claim 1 or 2 wherein said stabilizing agent is a tin compound selected from the group consisting of stannous oxide, stannic oxide, stannous sulfide, stannic sulfide, a tin salt of a carboxylic acid, a tin thiocarboxylate, a dihydrocarbyltin bis(hydrocarbyl mercaptoalkanoate), a tin thiocarbamate and a dihydrocarbyltin bis(0,0-dihydrocarbyl thiophosphate).

7. A process in accordance with claim 1 or 2 wherein an aqueous solution of said stabilizing agent is used to treat said finer fines.

4. A process in accordance with claim 16 or 17 wherein said stabilizing agent is an indium compound selected from the group consisting of indium oxide, indium sulfide, indium tris (0,0-dihydrocarbyl phosphite), indium tallate, indium dialkyldithiocarbamate and indium salt of the organic phosphate