IP Library › Granted Patent US 10,543,468
Granted Patent B2
US 10,543,468 · App. 15/448,961 · Granted Jan 28, 2020

Supercritical reactor systems and processes for petroleum upgrading

Inventors: Ki-Hyouk Choi (Dhahran, SA); Abdullah T. Alabdulhadi (Dhahran, SA); Mohammad A. Al-Abdullah (Dhahran, SA)
Assignee: Saudi Arabian Oil Company
B01J3/008B01J3/02C10G11/10C10G31/08C10G49/18C10G51/026C10G65/02C10G65/10C10G65/12C10G75/00C10G75/04C10G2300/70C10G2300/703C10G2300/805C10G2300/807Y02P20/544
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Quick Facts
Patent No.
US 10,543,468
App. No.
15/448,961
Granted
Jan 28, 2020
Kind
B2
Abstract

Provided herein are supercritical upgrading reactors and reactor systems for upgrading a petroleum-based composition by using one or more supercritical upgrading reactors and one or more supercritical standby reactors that alternate functions such that the supercritical upgrading reactor is converted to a supercritical standby reactor and the supercritical standby reactor is converted to a supercritical upgrading reactor. The supercritical upgrading reactor upgrades a combined feed stream while a supercritical standby reactor delivers a cleaning fluid into the supercritical standby reactor. The supercritical reactors may have one or more catalyst layers and one or more purging fluid inlets, and the catalyst layers may have differing void volume ratios.

Claims (18)

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 one or more supercritical upgrading reactors and one or more supercritical standby reactors,

where the supercritical upgrading reactor and the supercritical standby reactor both operate at a temperature greater than a critical temperature of water and a pressure greater than a critical pressure of water,

where the supercritical upgrading reactor and the supercritical standby reactor both comprise at least one catalyst layer,

where the supercritical upgrading reactor, the supercritical standby reactor, or both comprise a first catalyst layer and a second catalyst layer, where the first catalyst layer comprises a heterogeneous porous metal containing catalyst having a first void volume ratio and the second catalyst layer comprises a heterogeneous porous metal containing catalyst having a second void volume ratio, where the second void volume ratio is less than the first void volume ratio, and

upgrading the combined feed stream in the supercritical upgrading reactor to produce an upgraded product;

cleaning the supercritical standby reactor by passing a cleaning fluid into the supercritical standby reactor, while the upgrading step is being performed in the supercritical upgrading reactor; and

alternating functions of the supercritical upgrading reactor and the supercritical standby reactor, such that the supercritical upgrading reactor is converted to a supercritical standby reactor undergoing a cleaning operation by the delivery of the cleaning fluid, while the supercritical standby reactor is converted to a supercritical upgrading reactor that upgrades the combined feed stream.

2. The process of claim 1 , where the at least one catalyst layer comprises a heterogeneous porous metal containing catalyst.

3. The process of claim 2 , where the heterogeneous porous metal containing catalyst includes one or more components selected from the group consisting of transition metals and precious metals.

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

5. The process of claim 4 , where the one or more pressure sensors trigger shutting down the combined feed stream from the supercritical upgrading reactor and commencing a cleaning operation.

6. The process of claim 4 , where the one or more pressure sensors trigger an alert when the pressure of at least one supercritical upgrading reactor or supercritical standby reactor has deviated from an operating pressure by from 1% to 10%.

7. The process of claim 1 , where the cleaning fluid comprises supercritical water, oil, or both.

8. The process of claim 1 , where the cleaning fluid comprises between 0.1 weight percent (wt %) and 2.0 wt % O 2 .

9. The process of claim 1 , where the supercritical upgrading reactor, the supercritical standby reactor, or both comprise one or more purging fluid inlets.

10. The process of claim 9 , where the one or more purging fluid inlets inject a purging fluid into the supercritical upgrading reactor, supercritical standby reactor, or both, in response to one or more pressure sensors.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 3, 2017
From: CHOI, KI-HYOUK; ALABDULHADI, ABDULLAH T.; AL-ABDULLAH, MOHAMMAD A.
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 041459/0644 →
Continuity (3)
Division 15377351 · Dec 13, 2016
Provisional Application 62267406 · Dec 15, 2015
Related Publication 20170175006A1 · Jun 22, 2017