Supercritical reactor systems and processes for petroleum upgrading

Patent metadata

Field	Value
Publication number	US-10384179-B2
Application number	US-201715448913-A
Country	US
Kind code	B2
Filing date	Mar 3, 2017
Priority date	Dec 15, 2015
Publication date	Aug 20, 2019
Grant date	Aug 20, 2019

Abstract

Supercritical upgrading reactors and reactor systems are provided for upgrading a petroleum-based composition using one or more purging fluid inlets to prevent plugging of the catalyst layer in the reactor. Processes for upgrading petroleum-based compositions by utilizing a reactor having at least one purging fluid inlet are also provided.

First claim

What is claimed is:

1. A reactor for upgrading a petroleum-based composition comprising:
a first catalyst layer disposed in a central region of the reactor,
a second catalyst layer disposed vertically below the first catalyst layer in the reactor,
an insert coaxially disposed inside a metal tubular wall of the reactor, and
a plurality of purging fluid inlets disposed proximate to the first catalyst layer, the second catalyst layer, or both, where
the purging fluid inlets comprise one or more linear pipes extending horizontally within the reactor;
the purging fluid inlets penetrate the insert; and
the reactor operates at a temperature greater than a critical temperature of water and a pressure greater than a critical pressure of water.

2. The reactor of claim 1 , where at least one of the first catalyst layer, the second catalyst layer, or the purging fluid inlets are supported by the insert.

3. The reactor of claim 1 , where the purging fluid inlets further comprise one or more angled linear pipes, the angle being relative to a horizontal plane defined by the first catalyst layer, the second catalyst layer, or both.

4. The reactor of claim 1 , where the purging fluid inlets further comprise one or more non-linear pipes, the non-linear pipes including at least one bend or curvature relative to a straight section of the non-linear pipe.

5. The reactor of claim 4 , where the bend is oriented at an angle θ relative to a plane defined by a straight section of the non-linear pipe.

6. The reactor of claim 1 , where at least one of the purging fluid inlets further comprises an annular ring having one or more openings, multiple pipes having one or more openings, or both.

7. A process for upgrading a petroleum-based composition comprising:
combining a supercritical water stream with a pressurized, heated petroleum-based composition in a mixing device to create a combined feed stream;
introducing the combined feed stream into an upgrading reactor system comprising at least one downflow supercritical upgrading reactor operating at a temperature greater than a critical temperature of water and a pressure greater than a critical pressure of water,
where the downflow supercritical upgrading reactor comprises
a first catalyst layer disposed in a central region of the reactor,
a second catalyst layer disposed vertically below the first catalyst layer in the downflow supercritical upgrading reactor,
an insert coaxially disposed inside a metal tubular wall of the reactor, and a plurality of purging fluid inlets disposed proximate to the first catalyst layer, the second catalyst layer, or both, where
the purging fluid inlets comprise one or more linear pipes extending horizontally within the reactor, and
the purging fluid inlets penetrate the insert;

passing the combined feed stream through the first catalyst layer, the second catalyst layer, or both to at least partially convert the combined feed stream to an upgraded product comprising light hydrocarbons;
injecting purging fluid through the purging fluid inlets to contact the first catalyst layer, the second catalyst layer, or both to reduce plugging; and
passing upgraded product out of the downflow supercritical upgrading reactor.

8. The process of claim 7 , where the purging fluid inlets are vertically disposed above the catalyst layers.

9. The process of claim 7 , wherein the purging fluid inlets are vertically disposed between the first catalyst layer and the second catalyst layer.

10. The process of claim 7 , where the purging fluid inlets further comprise one or more angled linear pipes, the angle being relative to a horizontal plane defined by the first catalyst layer, the second catalyst layer, or both.

11. The process of claim 7 , where the purging fluid inlets further comprise one or more non-linear pipes, the non-linear pipes including at least one bend or curvature relative to a straight section of the non-linear pipe.

12. The process of claim 11 , in which the bend is oriented at an angle θ relative to a plane defined by a straight section of the non-linear pipe.

13. The process of claim 7 , where at least one of the purging fluid inlets further comprises an annular ring having one or more openings.

14. The process of claim 7 , where the purging fluid inlets further comprise multiple pipes spaced apart or interconnected with one or more openings.

15. The process of claim 7 , where the purging fluid comprises aromatic hydrocarbons selected from the group consisting of benzene, toluene, xylene, and combinations thereof.

16. The process of claim 7 , further comprising one or more pressure sensors upstream, downstream, or both upstream and downstream of the downflow supercritical upgrading reactor.

17. The process of claim 16 , where the pressure sensors trigger one or more of the purging fluid inlets to deliver purging fluid when the pressure of the downflow supercritical upgrading reactor deviates from 1% to 10% of operating pressure.

Assignees

• Saudi Arabian Oil Co

Inventors

• Choi Ki-Hyouk
• Alabdulhadi Abdullah T
• Al-Abdullah Mohammad A

Classifications

• C10G31/08 Primary

  by treating with water · CPC title

• B01J3/008 Primary

  Processes carried out under supercritical conditions · CPC title

• C10G11/10

  with stationary catalyst bed · CPC title

• C10G75/04 Primary

  by addition of antifouling agents · CPC title

• C10G51/026

  only catalytic cracking steps · CPC title