Method for the pyrolytic extraction of hydrocarbon from oil shale

• US 8,435,404 B2
• Filed: 10/22/2009
• Issued: 05/07/2013
• Est. Priority Date: 10/22/2009
• Status: Active Grant

• Current Assignee: Komline-Sanderson Corp.
• Original Assignee: Wyssmont Company, Inc.
• Inventors: Weisselberg, Edward
• Primary Examiner(s): MCCAIG, BRIAN A
• Application Number:
  US12/589,394
• Publication Number:
  US 20110094940A1
• Time in Patent Office: 1,293 Days
• Field of Search: 208/390, 208/400, 208407-408, 34 64- 65, 34218-219, 342/26, 345/05, 202/109, 202117-118
• US Class Current: 208/400
• CPC Class Codes: C10G 1/00 Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal mechanical winning of oil from oil-shales, oil-sand, or the like B03B
• CPC Class Codes: C10G 1/02 by distillation

Abstract

A method for the pyrolytic extraction of hydrocarbons such as shale oil from kerogen. Oil shale containing kerogen which has been ground into particulate form, is cascaded downwardly between a plurality of rotating trays within a heated processing chamber. As the hydrocarbons are volatized within the chamber, the volatiles are collected and condensed within a condenser or other suitable recovery apparatus.

Claims

1. A method for extracting shale oil from oil shale containing kerogen, said method comprising:

cascading oil shale in particulate form between a plurality of trays vertically stacked within at least one heated processing zone provided within a material processing chamber,

heating said oil shale within at least one heated processing zone to volatize said shale oil from said kerogen,

maintaining said material processing chamber at a pressure of about ±

0.05-±

0.10 inches water;

condensing the volatized shale oil, and discharging the residual of said oil shale from said material processing chamber.

2. The method of claim 1, further including supplying said oil shale in particulate form in the range of about 15 to 325 mesh size.

3. The method of claim 1, wherein the residual of said oil shale discharged from said chamber is substantially free of organic contaminants.

4. The method of claim 1, wherein heating said oil shale comprises heating said material processing chamber to a temperature in the range of 480°

F. to 1200°

F.

5. The method of claim 1, further including condensing at least one organic hydrocarbon volatized from said oil shale in addition to said volatized shale oil.

6. The method of claim 5, wherein condensing the volatized organic hydrocarbon is independent from condensing said volatized shale oil.

7. The method of claim 1, wherein said volatized shale oil is condensed within said material processing chamber.

8. The method of claim 1, wherein said heating comprises supplying heated inert gas to said material processing chamber.

9. The method of claim 8, further including distributing said heated inert gas within said material processing chamber by at least one or a plurality of fans.

10. The method of claim 1, further including providing at least one stationary wiper arm overlying each of said trays, and rotating said plurality of trays.

11. The method of claim 1, further including providing at least one wiper arm overlying each of said plurality of trays, and rotating the wiper arms while said plurality of trays remain stationary.

12. A method for extracting shale oil from oil shale containing kerogen, said method comprising:

passing oil shale in particulate form downwardly between a plurality of horizontal material supports within a material processing chamber,

heating said oil shale within said material processing chamber to a sufficient temperature to volatize said shale oil from said kerogen,

maintaining said material processing chamber at a pressure of about ±

0.05-±

0.10 inches water;

discharging the volatized shale oil from said material processing chamber,

condensing the volatized shale oil, and

discharging the residual oil shale from said material processing chamber.

13. The method of claim 12, wherein said material supports comprise a plurality of vertically stacked trays.

14. The method of claim 12, further including supplying said oil shale in particulate form in the range of about 15 to 325 mesh size.

15. The method of claim 12, wherein the residual of said oil shale discharged from said chamber is substantially free of organic contaminants.

16. The method of claim 12, wherein heating said oil shale comprises heating said material processing chamber to a temperature in the range of 480°

F. to 1200°

F.

17. The method of claim 12, further including condensing at least one organic hydrocarbon volatized from said oil shale in addition to said volatized shale oil.

18. The method of claim 17, wherein condensing the volatized organic hydrocarbon is independent from condensing said volatized shale oil.

19. The method of claim 12, wherein said volatized shale oil is condensed inside or outside said material processing chamber.

20. The method of claim 12, wherein said heating comprises supplying heated inert gas to said material processing chamber.

21. The method of claim 20, further including distributing said heated inert gas within said material processing chamber by at least one or a plurality of fans.

22. The method of claim 12, further including providing at least one stationary wiper arm overlying each of said supports, and rotating said plurality of supports.

23. The method of claim 12, further including providing at least one wiper arm overlying each of said plurality of supports, and rotating the wiper arms while said plurality of supports remain stationary.

24. A method for extracting hydrocarbons from oil shale containing kerogen, said method comprising:

supplying oil shale in particulate form to a material processing chamber having an upper processing zone and a lower processing zone, said material processing chamber including a plurality of vertically displaced material supports extending through said upper processing zone and said lower processing zone;

passing said oil shale downwardly within said material processing chamber from one material support to another underlying material support;

maintaining said material processing chamber at a pressure of about ±

0.05-±

0.10 inches water;

applying heat within said upper and lower processing zones within said material processing chamber for volatizing said hydrocarbons from said kerogen;

discharging a first volatized oil shale component from said upper processing zone within said material processing chamber;

discharging a second volatized oil shale component from said lower processing zone within said material processing chamber;

condensing at least one of the volatized oil shale components, and

discharging the residual oil shale from said material processing chamber.

25. The method of claim 24, further including supplying said oil shale in particulate form in the range of about 15 to 325 mesh size.

26. The method of claim 24, wherein the residual of said oil shale discharged from said chamber is substantially free of organic contaminants.

27. The method of claim 24, wherein said lower processing zone is heated to a temperature in the range of 480°

F. to 1200°

F.

28. The method of claim 24, further including condensing each of the volatized oil shale components.

29. The method of claim 24, wherein said upper processing zone is heated to a temperature in the range of 480°

F. to 1200°

F.

30. The method of claim 24, wherein said applying heat comprises supplying heated inert gas.

31. The method of claim 30, further including distributing said heated inert gas within said material processing chamber by at least one or a plurality of fans.

32. The method of claim 24, further including providing at least one stationary wiper arm overlying each of said supports, and rotating said plurality of supports.

33. The method of claim 24, further including providing at least one wiper arm overlying each of said plurality of supports, and rotating the wiper arms while said plurality of supports remain stationary.

34. A method for extracting shale oil from oil shale, said method comprising:

transferring oil shale through a heated processing chamber between a plurality of material supports arranged in a vertical stack within said processing chamber,

maintaining said processing chamber at a pressure of about ±

0.05-±

0.10 inches water;

heating said oil shale within said plurality of material supports, said heating of said oil shale volatizing shale oil contained in said oil shale, and

condensing the volatized shale oil.

35. The method of claim 34, further including supplying said oil shale in particulate form in the range of about 15 to 325 mesh size.

36. The method of claim 34, discharging the residual of the oil shale from said processing chamber, wherein the residual oil shale is substantially free of organic contaminants.

37. The method of claim 34, wherein said processing chamber is heated to a temperature in the range of 480°

F. to 1200°

F.

38. The method of claim 34, wherein said material supports comprise horizontally arranged trays.

39. The method of claim 38, further including rotating said trays containing said oil shale.

40. The method of claim 34, wherein said volatized shale oil is condensed inside or outside said material processing chamber.

41. The method of claim 34, wherein said heating comprises supplying heated inert gas to said material processing chamber.

42. The method of claim 41, further including distributing said heated inert gas within said material processing chamber by at least one or a plurality of fans.

43. The method of claim 34, further including providing at least one stationary wiper arm overlying each of said supports, and rotating said plurality of supports.

44. The method of claim 34, further including providing at least one wiper arm overlying each of said plurality of supports, and rotating the wiper arms while said plurality of supports remain stationary.