IP Library Granted Patent US 9,242,190
Granted Patent B2
US 9,242,190 · App. 12/960,215 · Granted Jan 26, 2016

Methods and systems for removing fines from hydrocarbon-containing fluids

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Quick Facts
Patent No.
US 9,242,190
App. No.
12/960,215
Granted
Jan 26, 2016
Kind
B2
Abstract

A method of removing fines from a hydrocarbon-containing fluid can include preparing a bed media of particulate earthen material ( 12 ). The hydrocarbon-containing fluid having fines therein can be passed through the bed media ( 12 ) at a flow rate such that a portion of the fines are retained in the bed media ( 12 ) to form a filtered hydrocarbon-containing fluid. The flow rate is sufficient to maintain a wetting film of the hydrocarbon-containing fluid across at least a majority portion of the particulate earthen material which is contacted by the hydrocarbon-containing fluid. The filtered hydrocarbon-containing fluid can be recovered from the bed media ( 12 ) via a suitable outlet ( 16 ) having substantially reduced or eliminated fines content.

Claims (27)

1. A method of removing fines from a hydrocarbon-containing fluid, comprising:

a. preparing a bed media of particulate earthen material;

b. passing the hydrocarbon-containing fluid having fines therein through the bed media at a flow rate such that a portion of the fines are retained in the bed media to form a filtered hydrocarbon-containing fluid, said flow rate being sufficient to maintain a wetting film coated on individual particles of the particulate earthen material, the wetting film comprising a liquid of the hydrocarbon-containing fluid across at least a majority portion of the particulate earthen material which is contacted by the hydrocarbon-containing fluid; and

c. recovering the filtered hydrocarbon-containing fluid from the bed media.

2. The method of claim 1 , wherein the passing the hydrocarbon-containing fluid includes introducing the hydrocarbon-containing fluid into the bed media subsequent to production of the hydrocarbon-containing fluid from a hydrocarbonaceous material.

3. The method of claim 1 , wherein the hydrocarbon-containing fluid is produced from a hydro carbonaceous material and the particulate earthen material is of the same material type as the hydrocarbonaceous material.

4. The method of claim 1 , wherein the particulate earthen material is selected from the group consisting of oil shale, tar sands, coal, and combinations thereof.

5. The method of claim 1 , wherein the particulate earthen material is oil shale.

6. The method of claim 1 , wherein the particulate earthen material has an average particle diameter from about 0.06 mm to about 1 m.

7. The method of claim 6 , wherein the average size particle diameter is from about 2 cm to about 1 m.

8. The method of claim 6 , wherein the average size particle diameter is from about 0.06 mm to about 5 mm.

9. The method of claim 1 , wherein the hydrocarbon-containing fluid is selected from the group consisting of shale oil, tar sand tailings, coal liquefaction product, and combinations thereof.

10. The method of claim 1 , wherein the wetting film has a thickness less than about 1 mm.

11. The method of claim 1 , wherein the flow rate is sufficient to provide a residence time of the hydrocarbon-containing fluid from about 2 days to about 4 months.

12. The method of claim 1 , wherein at least a portion of the wetting film has a thickness which does not exceed an equilibrium film thickness.

13. The method of claim 12 , wherein the portion of the wetting film is at least 10% by volume of the particulate earthen material.

14. The method of claim 1 , wherein the bed media is substantially stationary during the passing the hydrocarbon-containing fluid through the bed media.

15. The method of claim 1 , wherein retention of the portion of fines in the bed media is primarily through adsorption rather than filtration.

16. The method of claim 1 , wherein the filtered hydrocarbon-containing fluid is substantially free of fines.

17. The method of claim 1 , wherein the fines have an average particle diameter of less than about 0.2 mm.

18. The method of claim 1 , wherein the fines have an average particle diameter of less than about 20 μm.

19. The method of claim 1 , wherein the bed media has a vertical depth from about 1 m to about 40 m.

20. The method of claim 1 , wherein void spaces are present between at least a majority of neighboring wetted particles.

21. A method of removing fines from a hydrocarbon-containing fluid, comprising:

a. preparing a bed media of particulate hydrocarbonaceous material;

b. producing a hydrocarbon-containing fluid having fines therein from the particulate hydrocarbonaceous material such that while the production is occurring the hydrocarbon-containing fluid passes through the bed media at a flow rate such that a portion of the fines are retained in the bed media to form a filtered hydrocarbon-containing fluid, said flow rate being sufficient to maintain a wetting film coated on individual particles of the particulate earthen material, the wetting film comprising a liquid of the hydrocarbon-containing fluid across at least a majority portion of the particulate hydrocarbonaceous material which is contacted by the hydrocarbon-containing fluid; and

c. recovering the filtered hydrocarbon-containing fluid from the bed media.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 22, 2011
From: PATTEN, JAMES W.
To: RED LEAF RESOURCES, INC.
Reel/Frame 025851/0752 →