Process to upgrade and desulfurize crude oil by supercritical water

Patent metadata

Field	Value
Publication number	US-9914885-B2
Application number	US-201313785437-A
Country	US
Kind code	B2
Filing date	Mar 5, 2013
Priority date	Mar 5, 2013
Publication date	Mar 13, 2018
Grant date	Mar 13, 2018

Abstract

This present invention generally relates to a process for upgrading and desulfurizing crude oil using supercritical water. In general, the invention provides a process for removal of contaminants from a crude oil stream by mixing the crude oil stream with supercritical water and then filtering out the precipitated solid compounds that result from mixing the crude oil stream with supercritical water.

First claim

The invention claimed is:

1. A process for removal of contaminants from a crude oil stream, the process comprising the steps of:
feeding a crude oil stream to a mixing apparatus, wherein the mixing apparatus is selected from a static mixer, an in-line mixer, agitator, in-line parts that can enhance mixing, and an impeller embedded device;
feeding a supercritical water stream to the mixing apparatus;
mixing the crude oil stream and the supercritical water stream in the mixing apparatus to produce a mixed crude oil and supercritical water stream, wherein mixing the crude oil stream and the supercritical water stream in the mixing apparatus causes solid compounds to precipitate;
feeding the mixed crude oil and supercritical water stream to a physical filter to remove the solid compounds from the mixed crude oil and supercritical water stream and to produce a filtered mixed crude oil and supercritical water stream;
feeding the filtered mixed crude oil and supercritical water stream to a unit for further processing, wherein the filtered mixed crude oil and supercritical water stream are subjected to upgrading reactions that occur in the unit for further processing.

2. The process of claim 1 wherein the unit is a desulfurization unit.

3. The process of claim 1 wherein the solid compounds are alkaline compounds.

4. The process of claim 1 further comprising the step of:
feeding the supercritical water stream to a water filter to produce a filtered supercritical water stream before feeding the supercritical water stream to the mixing apparatus.

5. The process of claim 1 wherein the physical filter comprises two or more filters arranged in series.

6. The process of claim 1 wherein the physical filter comprises two or more physical filters arranged in parallel.

7. The process of claim 1 wherein the temperature of the mixed crude oil and supercritical water stream as it is fed to the physical filter is maintained at a temperature of over 400° C.

8. The process of claim 1 wherein the physical filter is a cup-type filter, a membrane-type filter, or a depth-type filter.

9. The process of claim 1 further comprising the step of:
feeding the mixed crude oil and supercritical water stream to an apparatus for creating turbulent flow of the mixed crude oil and supercritical water stream to produce a turbulent flow mixed crude oil and supercritical water stream before feeding the mixed crude oil and supercritical water stream to the filter.

10. The process of claim 9 wherein the apparatus for creating turbulent flow is a continuous stirred tank reactor.

11. The process of claim 1 wherein the unit is selected from the group consisting of a desulfurization unit, a supercritical water reactor unit, a hydrotreating unit, and a hydrocracking unit.

12. A process for removal of contaminants from a crude oil stream, the process comprising the steps of:
feeding a water stream below supercritical conditions to a water filter to remove solid compounds to produce a filtered water stream;
heating the filtered water stream to supercritical conditions using a heating apparatus to produce a filtered supercritical water stream;
feeding the filtered supercritical water stream to a mixing apparatus, wherein the mixing apparatus is selected from a static mixer, an in-line mixer, agitator, in-line parts that can enhance mixing, and an impeller embedded device;
feeding a crude oil stream to the mixing apparatus;
mixing the crude oil stream and the filtered supercritical water stream in the mixing apparatus to produce a mixed crude oil and supercritical water stream;
feeding the mixed crude oil and supercritical water stream to a physical filter to remove second solid compounds from the mixed crude oil and supercritical water stream and to produce a filtered mixed crude oil and supercritical water stream;
feeding the filtered mixed crude oil and supercritical water stream to a unit for further processing, wherein the filtered mixed crude oil and supercritical water stream are subjected to upgrading reactions that occur in the unit for further processing.

13. The process of claim 12 wherein the physical filter comprises two or more filters arranged in series.

14. The process of claim 12 wherein the physical filter comprises two or more filters arranged in parallel.

15. The process of claim 12 wherein the temperature of the mixed crude oil and supercritical water stream as it is fed to the physical filter is maintained at a temperature of over 400° C.

16. The process of claim 12 wherein the physical filter is a cup-type filter, a membrane-type filter, or a depth-type filter.

17. The process of claim 12 wherein the solid compounds are alkaline compounds in the water stream.

18. The process of claim 12 wherein the second solid compounds are alkaline compounds that precipitate as a result of the crude oil stream mixing with the supercritical water stream in the mixing apparatus.

19. The process of claim 12 further comprising the step of:
feeding the mixed crude oil and supercritical water stream to an apparatus for creating turbulent flow of the mixed crude oil and supercritical water stream to produce a turbulent flow mixed crude oil and supercritical water stream before feeding the mixed crude oil and supercritical water stream to the filter.

20. The process of claim 19 wherein the apparatus for creating turbulent flow is a continuous stirred tank reactor.

Assignees

• Saudi Arabian Oil Co

Inventors

• Choi Ki-Hyouk
• Lee Joo-Hyeong
• Garhoush Mohammad S

Classifications

• C10G2300/42

  Hydrogen of special source or of special composition · CPC title

• C10G2300/4012

  Pressure · CPC title

• C10G2300/4006

  Temperature · CPC title

• C10G2300/208

  Sediments, e.g. bottom sediment and water or BSW · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title