Advanced control of severe fluid catalytic cracking process for maximizing propylene production from petroleum feedstock

Patent metadata

Field	Value
Publication number	US-9701914-B2
Application number	US-98307807-A
Country	US
Kind code	B2
Filing date	Nov 7, 2007
Priority date	Nov 7, 2006
Publication date	Jul 11, 2017
Grant date	Jul 11, 2017

Abstract

With an aim to optimize propylene production, petroleum oil such as gas oil is catalytically cracked by contacting the oil with catalyst mixture consisting of a base cracking catalyst containing an stable Y-type zeolite and small amounts of rare-earth metal oxide, and an additive containing a shape-selective zeolite, in a down-flow type fluid catalytic cracking apparatus having a regeneration zone, a separation zone, and a stripping zone, wherein conversion of hydrocarbon occurs under relatively severe conditions. According to this fluid catalytic cracking process, the production of light-fraction olefins such as propylene is maximized by applying appropriate process control, monitoring, and optimizing systems. Process model and historical data to test a predictive system can provide early warning of potential performance degradation and equipment failure in the FCC unit.

First claim

What is claimed is:

1. A process for the production of propylene by the fluid catalytic cracking of petroleum oil feedstock, the process comprising the steps of:
contacting the oil feedstock with a cracking catalyst mixture, the cracking catalyst mixture comprising:
55 to 95 wt % of a base cracking catalyst comprising a stable Y-type zeolite and less than 0.6 wt % of rare-earth metal oxide,
5 to 45 wt % of an additive comprising a shape-selective zeolite, and
0.5 to 10% by weight of a phosphorus-containing compound;

reacting the cracking catalyst mixture and oil feedstock in a reaction zone of a down-flow type fluid catalytic cracking apparatus having a regeneration zone, a first separation zone, a stripping zone, and a catalyst injection system, said fluid catalytic cracking apparatus maintained at a temperature of between 500° C. and 650° C. and a contact time of approximately 0.05 to 3.0 seconds, to obtain a mixture of a propylene product stream, unreacted oil feedstock and spent catalyst, wherein the propylene product stream comprises an increased amount of propylene as compared to an amount of propylene in the feed stream;
wherein the catalyst/oil ratio in the fluid catalytic cracking apparatus is between 10 to 50 wt/wt;
wherein the catalyst injection system comprises at least one catalyst injection apparatus, at least one sensor adapted to determine the propylene product stream composition, and a controller coupled to the system, wherein the catalyst injection system controls catalyst injection in response to a signal from the at least sensor;
wherein the addition of oil feedstock and catalyst to the reaction zone is controlled by a process control; and
separating and collecting the propylene product stream from the spent catalyst and unreacted oil feedstock in the stripping zone;
regenerating spent catalyst in the regeneration zone;
withdrawing a stream comprising the propylene product stream and the unreacted oil feedstock from the stripping zone; and
recycling at least a portion of the propylene product stream from the stream withdrawn from the stripping zone, through a second separation zone before sending the recycled portion of the propylene product stream to the reaction zone,
wherein the process control comprises the steps of:
continuously monitoring feed data, products characterization data and operating conditions;
developing process models based on the feed data, products characterization data and operating conditions monitored;
comparing process performance with the process models; and
adjusting operating conditions to optimize propylene production.

2. The process of claim 1 wherein the separation zone comprises a cyclone separator and the fluid catalytic cracking apparatus further comprises a secondary separator coupled to the separation zone and a catalyst hopper for supplying fresh catalyst to the reaction zone.

3. The process of claim 1 wherein the reaction zone outlet temperature is greater than 500° C. and wherein the reaction of the cracking catalyst mixture and the oil feedstock is at a pressure of between 1 and 5 atmospheres.

4. The process of claim 1 wherein the feedstock composition, product composition and operating conditions can be monitored and utilized to a develop process model which is then used to maximize propylene yield.

5. The process of claim 1 wherein the rare-earth metal oxide content in the base cracking catalyst is less than 0.08 wt % and wherein the base cracking catalyst comprises between 0.1 to 10 weight percent of a promoter metal.

6. The process of claim 1 wherein the petroleum oil feedstock is selected from the group consisting of an oil selected from the group consisting of naphtha, crude oil, deasphalted oil, vacuum gas oil, gas oil, petroleum residua, hydrotreated petroleum oil products, and mixtures thereof.

7. A process for the production of propylene by the fluid catalytic cracking of a petroleum oil feedstock, comprising:
contacting the petroleum oil feedstock selected from the group consisting of straight-run gas oil, vacuum gas oil, atmospheric residue, vacuum residue, coker gas oil and petroleum oils obtained by hydrofining or hydrotreating said residues and gas oils, and mixtures thereof, with a cracking catalyst mixture, the cracking catalyst mixture comprising:
55 to 95 wt % of a base cracking catalyst comprising an ultra stable Y-type zeolite and less than 0.5 wt % of rare-earth metal oxide,
5 to 45 wt % of an additive comprising a shape-selective zeolite,
between 0.5 and 10% by weight of a phosphorus-containing compound; and
between about 0.1 and 10% by weight of a promoter metal selected from the group consisting of gallium, germanium, tin, and mixtures thereof;

reacting the cracking catalyst mixture and oil feedstock in a reaction zone of a down-flow type fluid catalytic cracking apparatus having a regeneration zone, a first separation zone, and a stripping zone maintained at a temperature of between 500° C. and 650° C. and a contact time of approximately 0.05 to 1.2 seconds, to obtain a mixture of a propylene product stream, unreacted petroleum oil feedstock, and spent catalyst, wherein the propylene product stream comprises an increased amount of propylene as compared to an amount of propylene in the feed stream;
wherein the addition of petroleum oil feedstock and fresh catalyst to the reaction zone is controlled by a process control;
separating and collecting the propylene product stream from the spent catalyst and unreacted petroleum oil feedstock in the stripping zone;
withdrawing a stream comprising the propylene product stream and the unreacted oil feedstock from the stripping zone; and
recycling at least a portion of the propylene product stream from the stream withdrawn from the stripping zone, through a second separation zone before sending the recycled portion of the propylene product stream to the reaction zone,
wherein the process control comprises the steps of:
continuously monitoring feed characterization data, propylene products characterization data, catalyst particle size, and operating conditions;
developing process models based on the feed characterization data, propylene products characterization data and operating conditions monitored;
comparing process performance with the process models; and
automatically adjusting operating conditions based upon the comparison of the process performance and the process models to optimize propylene production and minimize associated production costs.

8. The process of claim 7 , wherein the process control further comprises the step of sensing an output in the fluid catalytic cracking unit and adjusting the amount of catalyst dispensed in response thereto.

9. The process of claim 1 , wherein the process control further comprises the step of balancing energy requirements with available energy supply.

10. The process of claim 1 wherein the process control further comprises the step of real-time monitoring of the dollar cost per unit of products generated by the FCC unit.

11. The process of claim 1 wherein the process control is configured to communicate with sensors positioned throughout the FCC unit, wherein said sensors monitor feed and product characteristics and reaction conditions.

12. The process of claim 1 wherein sensors within the FCC unit communicate on-line measurement of the reaction temperature, reaction pressure, flow rates, catalyst particle size, chemical composition of fluid streams, regeneration zone temperatures and regeneration zone pressures to the process control, and wherein the process control optimizes the catalyst dosage and olefin production.

13. The process of cla

Assignees

• Khan M Rashid
• Taha Othman A
• Saudi Arabian Oil Co

Inventors

• Khan M Rashid
• Taha Othman A

Classifications

• C10G2300/1059

  Gasoil having a boiling range of about 330 - 427 °C · CPC title

• C10G2300/4081

  Recycling aspects · CPC title

• C10G2300/4006

  Temperature · CPC title

• C10G2300/1074

  Vacuum distillates · CPC title

• C10G2300/1044

  Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C · CPC title