Method for catalytically cracking hydrocarbons

• US 4,026,789 A
• Filed: 02/13/1976
• Issued: 05/31/1977
• Est. Priority Date: 01/17/1975
• Status: Expired due to Term

• Current Assignee: Phillips Petroleum Company (ConocoPhillips)
• Original Assignee: Phillips Petroleum Company (ConocoPhillips)
• Inventors: James, John Preston
• Primary Examiner(s): Levine, Herbert
• Application Number:
  US05/657,818
• Time in Patent Office: 473 Days
• Field of Search: 23/288 S, 23/288 B, 23/288 E, 208/74, 208/75, 208/155, 208/156, 208/DIG.1, 208/164
• US Class Current: 208/74
• CPC Class Codes: B01J 8/24 according to "fluidised-bed" technique B01J8/20 takes precedence
• CPC Class Codes: C10G 11/18 according to the "fluidised-bed" technique
• CPC Class Codes: C10G 11/187 Controlling or regulating
• CPC Class Codes: Y10S 208/01 Automatic control

Abstract

An apparatus for catalytically cracking hydrocarbons comprising a riser reactor having a plurality of catalyst injectors positioned along the length thereof. Adjacent to and upstream of certain of the catalyst injectors, cyclone separators are connected to the reactor so that fluid which contains a partially converted or cracked hydrocarbon and catalyst pass therethrough for separating the catalyst from the fluid with the fluid being returned to the reactor. Fresh catalyst is introduced into the fluid after same exits the separator to continue the cracking process. Steam can also be introduced into the reactor adjacent the catalyst injectors.

Claims

1. A method for catalytically cracking hydrocarbons in a riser reactor comprising:

(a) introducing a hydrocarbon material and steam into a first zone of a riser reactor having a plurality of zones;

(b) introducing fresh catalyst into said reactor first zone adjacent the point of introduction of said hydrocarbon and steam;

(c) diverting at least a portion of the mixture of hydrocarbon, steam and catalyst from a downstream end of the reactor first zone into a separating means;

(d) separating said catalyst from the mixture of same with hydrocarbon and steam;

(e) reintroducing the hydrocarbon and steam into said reactor into an upstream end of a second zone;

(f) introducing fresh catalyst into said reactor adjacent the upstream end of the second zone to form a mixture of same with the hydrocarbon and steam from said separating means; and

(g) separating said catalyst from said mixture of catalyst, hydrocarbon and steam from a downstream end of the reactor second zone and conducting said steam and hydrocarbon to equipment for processing same.

2. The method as set forth in claim 1 including:

(a) collecting said separated catalyst from the first and second zones;

(b) conducting said separated catalyst to a regenerator; and

(c) regenerating said separated catalyst to make fresh catalyst.

3. The method as set forth in claim 2 including:

(a) returning at least a portion of said regenerated fresh catalyst to said reactor for mixing same with the mixture of hydrocarbon and steam, said regenerated fresh catalyst being at least a portion of the fresh catalyst introduced into said mixture of hydrocarbon and steam in the first and second zones of said reactor.

4. The method as set forth in claim 1 including:

(a) controlling the introduction of fresh catalyst into said reactor in response to the temperature therein.

5. A method for catalytically cracking hydrocarbons in a riser reactor comprising:

(a) introducing a hydrocarbon material and steam into an upstream end of a reactor having a plurality of reaction zones connected in series relation;

(b) introducing fresh catalyst into the upstream end of the reactor adjacent the point of introduction of the hydrocarbon and steam and into the upstream end of each of the remaining zones;

(c) diverting at least a portion of the mixture of hydrocarbon, steam and catalyst from a downstream end of each zone into a separating means;

(e) separating in the separating means said catalyst from the mixture of same with hydrocarbon and steam;

(f) introducing the separated hydrocarbon and steam from one zone and fresh catalyst into an upstream end of the next downstream zone of the reactor;

(g) separating catalyst from a mixture of same with hydrocarbon and steam from the last downstream zone and recovering the last mentioned catalyst and hydrocarbon;

(h) collecting the separated catalyst;

(i) conducting the collected catalyst to a regenerator;

(j) regenerating the collected catalyst to make fresh catalyst; and

(k) returning at least a portion of said regenerated fresh catalyst to said reactor and introducing the regenerated fresh catalyst as at least a portion of the fresh catalyst introduced into the mixture of hydrocarbon and steam in the zones.

6. The method as set forth in claim 5 including:

(a) controlling separately the temperature in each of said zones by controlling the rate of introduction of fresh catalyst into the respective zone.

7. The method as set forth in claim 6 including:

(a) maintaining a positive catalyst head in the separating means as measured by a pressure controller by controlling the rate of discharge of catalyst from the separating means.