Supercritical reactor systems and processes for petroleum upgrading

Patent metadata

Field	Value
Publication number	US-10640715-B2
Application number	US-201916451957-A
Country	US
Kind code	B2
Filing date	Jun 25, 2019
Priority date	Dec 15, 2015
Publication date	May 5, 2020
Grant date	May 5, 2020

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 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 at least one catalyst layer and one or more purging fluid inlets disposed on one or more side locations of the downflow supercritical upgrading reactor proximate the catalyst layer;

passing the combined feed stream through the at least one catalyst layer to at least partially convert the combined feed stream to an upgraded product comprising light hydrocarbons;
injecting purging fluid through the purging inlets to contact the at least one catalyst layer;
reducing plugging of the at least one catalyst layer by injecting the purging fluid, wherein the purging fluid comprises supercritical water, supercritical water comprising non-asphaltenic aromatic hydrocarbons, supercritical water comprising product oil, water saturated with molecular oxygen, water comprising hydrogen peroxide, water comprising organic peroxide, hydrocarbons comprising organic peroxide, or combinations thereof; and
passing upgraded product out of the downflow supercritical upgrading reactor.

2. The process of claim 1 , where the purging fluid inlets are vertically disposed above the at least one catalyst layer.

3. The process of claim 1 , wherein the supercritical upgrading reactor comprises at least a first catalyst layer and a second catalyst layer, and the purging fluid inlets are vertically disposed between the first catalyst layer and the second catalyst layer.

4. The process of claim 1 , where the purging fluid inlets comprise one or more angled linear pipes, the angle being relative to a horizontal plane defined by the at least one catalyst layer.

5. The process of claim 1 , where the purging fluid inlets comprise one or more linear pipes extending horizontally within the downflow supercritical upgrading reactor.

6. The process of claim 1 , where the purging fluid inlets 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.

7. The process of claim 6 , in which the bend is oriented at an angle θ relative to a plane defined by a straight section of the non-linear pipe.

8. The process of claim 1 , where the purging fluid inlets comprises an annular ring having one or more openings.

9. The process of claim 1 , where the purging fluid inlets comprise multiple pipes spaced apart or interconnected with one or more openings.

10. The process of claim 1 , where the aromatic hydrocarbons are selected from the group consisting of benzene, toluene, xylene, and combinations thereof.

11. The process of claim 1 , further comprising one or more pressure sensors upstream, downstream, or both upstream and downstream of the downflow supercritical upgrading reactor.

12. The process of claim 11 , 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

• C10G75/00

  Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general (C10G7/10, C10G9/16 take precedence) · CPC title

• C10G51/026

  only catalytic cracking steps · CPC title

• C10G11/10

  with stationary catalyst bed · CPC title

• C10G2300/70

  Catalyst aspects · CPC title

• B01J3/008 Primary

  Processes carried out under supercritical conditions · CPC title