Slurry hydrocarbon synthesis with downcomer fed product filtration (LAW552)

• US 5,811,469 A
• Filed: 05/06/1997
• Issued: 09/22/1998
• Est. Priority Date: 05/06/1997
• Status: Expired due to Term

• Current Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Original Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Inventors: Mart, Charles J., Leviness, Stephen C.
• Primary Examiner(s): Geist, Gary
• Assistant Examiner(s): PARSA, JAFAR F
• Application Number:
  US08/851,866
• Time in Patent Office: 504 Days
• Field of Search: 518/700, 502/21, 502/22, 502/53, 422/230, 422/231
• US Class Current: 518/700
• CPC Class Codes: B01J 8/006 by filtration
• CPC Class Codes: B01J 8/22 gas being introduced into the liquid
• CPC Class Codes: B01J 8/226 internally, i.e. the particles rotate within the vessel
• CPC Class Codes: B01J 8/228 externally, i.e. the particles leaving the vessel and subsequently re-entering it
• CPC Class Codes: C07C 1/0485 Set-up of reactors or accessories; Multi-step processes
• CPC Class Codes: C07C 1/066 used for dissolving, suspending or transporting the catalyst

Abstract

Hydrocarbon liquid products are filtered and removed from a three phase hydrocarbon synthesis slurry comprising gas bubbles and particulate catalyst solids in a hydrocarbon liquid, by circulating the slurry through a gas disengaging downcomer immersed in the slurry to a filtration zone external or internal of the reactor, and then back into the slurry in the reactor. The gas disengagement densifies the slurry which is passed across the filtration surface under high flow conditions, to reduce solids build up on the filter as filter cake. Circulation through the filtration zone occurs by gravity and hydrostatics due to slurry density differences. The downcomer may also be a gas and solids reducing downcomer.

Claims

1. A slurry hydrocarbon synthesis process for forming hydrocarbons comprising:

(a) reacting a synthesis gas comprising a mixture of H₂ and CO, in the presence of a solid, particulate hydrocarbon synthesis catalyst in a slurry body comprising said catalyst and gas bubbles in a hydrocarbon slurry liquid under reaction conditions effective to form hydrocarbons, at least a portion of which are liquid at said reaction conditions, wherein said slurry hydrocarbon liquid comprises said liquid hydrocarbons;

(b) passing a portion of said slurry from said slurry body through a gas disengaging zone immersed in said slurry body to form a gas reduced slurry;

(c) passing said gas reduced slurry from said gas disengaging zone through a downcomer and into a filtration zone under conditions of high flow;

(d) contacting said gas reduced slurry with filtration means in said filtration zone under said high flow conditions to separate a portion of said hydrocarbon liquid from said slurry as a filtrate and produce a hydrocarbon reduced slurry, and

(e) passing hydrocarbon reduced slurry back into said slurry body.

2. A process according to claim 1 wherein said slurry body is in a hydrocarbon synthesis reactor.

3. A process according to claim 2 wherein said gas reduced slurry in produced in a gas disengaging downcomer.

4. A process according to claim 2 wherein a portion of said slurry body is passed out of said reactor and wherein said gas reduced slurry is formed external of said reactor.

5. A process according to claim 1, wherein in step (b) said slurry is also passed through a solids reducing zone to produce a gas and solids reduced slurry which is passed through said filtration zone under said high liquid shear flow conditions and back into said slurry body.

6. A process according to claim 5 wherein said gas and solids reduced slurry is produced in a gas and solids reducing downcomer.

7. A process according to claim 2 wherein said filtration zone is external of said reactor.

8. A process according to claim 3 wherein said filtration means is vertically upwardly removable from said filtration zone.

9. A process according to claim 8 wherein said filtration zone is within said slurry body.

10. A process according to claim 9 wherein said filtration zone is within said downcomer immersed in said slurry body.

11. A process according to claim 1 wherein at least a portion of said filtrate is subjected to conversion.

12. A process according to claim 11 wherein the conversion is non-catalytic.

13. A process according to claim 11 wherein the conversion is catalytic.

14. A process according to claim 13 wherein hydrogen is present in the catalytic conversion.

15. A process according to claim 14 wherein the catalytic conversion is hydroisomerization.