Solvent and water/surfactant process for removal of bitumen from tar sands contaminated with clay

• US 4,968,412 A
• Filed: 03/07/1990
• Issued: 11/06/1990
• Est. Priority Date: 01/17/1989
• Status: Expired due to Fees

• Current Assignee: Guymon E. Park
• Original Assignee: Guymon E. Park
• Inventors: Guymon, E. Park
• Primary Examiner(s): Pal, Asok
• Application Number:
  US07/490,089
• Time in Patent Office: 244 Days
• Field of Search: 208/390, 208/391
• US Class Current: 208/390
• CPC Class Codes: C10G 1/04 by extraction

Abstract

This invention involves the separation of clay-contaminated bitumen from sand with a solvent. The bitumen is dissolved with an organic solvent such as condensate from a natural gas well. The clay is separated from the dissolved bitumen and the solvent is recoverd and recycled. The sand is washed with water containing a carefully selected, nonanionic surface active agent to remove residual bitumen and solvent. Prior removal of the clay precludes it from unduly contaminating the water.

Claims

1. A process for removing bitumen from a tar sand contaminated with clay comprising:

obtaining a tar sand consisting of bitumen and clay mixed with sand;

introducing said tar sand into a stripper vessel;

dissolving said bitumen with a solvent, said solvent also removing said clay from said sand into a liquid medium formed with said solvent and bitumen;

removing said liquid medium from said sand; and

washing said sand with water to which a nonionic surface active agent has been added to remove residual bitumen from said sand, said surfactive agent comprising a linear alcohol having carbon atoms within the range on the order of about eight to fifteen carbon atoms and ethoxylate units on the carbon atoms within the range on the order of about two to eight ethoxylate units, said surfactant being present in said water in an effective amount less than about 0.5 percent, by volume.

2. The process defined in claim 1 wherein said dissolving step comprises obtaining said solvent from a condensate from a natural gas source.

3. The process defined in claim 1 wherein said dissolving step comprises obtaining said solvent from a group consisting of organic solvents.

4. The process defined in claim 1 wherein said removing step includes separating said clay from said liquid medium.

5. The process defined in claim 4 wherein said separating step includes recovering said solvent from said liquid medium by evaporating said solvent from said bitumen thereby recovering said solvent and producing bitumen.

6. The process defined in claim 5 wherein the recovering step includes recycling said solvent to said stripper vessel and amending said solvent with additional solvent.

7. The process defined in claim 4 wherein said separating step includes removing said clay from said liquid medium by centrifugation of said liquid medium.

8. The process defined in claim 1 wherein said adding step includes agitating said sand in said water by passing a gas upwardly through said sand.

9. The process defined in claim 1 wherein said agitating step is followed by removing said residual bitumen from said water by passing said water and residual bitumen into an oil/water separator, said residual bitumen floating to the surface of said oil/water separator.

10. A process for recovering bitumen from a tar sand having a bitumen, clay, and sand content comprising:

obtaining a tar sand having a bitumen, clay, and sand content;

sizing said tar sand and introducing said sized tar sand into a stripper vessel;

stripping said clay and said bitumen from said sand by dissolving said bitumen with a solvent, said clay, bitumen and solvent forming a liquid medium, and leaving a sand residue;

removing said liquid medium from said sand residue;

separating said clay from said liquid medium;

recovering said bitumen from said liquid medium by evaporating said solvent from said bitumen; and

washing said sand residue with water to which a carefully selected nonanionic surfactant has been added in an effective amount less than about 0.5 percent, by volume, said surfactant comprising a linear alcohol having carbon atoms within the range on the order of about eight to fifteen carbon atoms and ethoxylate groups within the range on the order of about two to eight ethoxylate groups.

11. The process defined in claim 10 wherein said stripping step includes obtaining said solvent as a condensate from a natural gas well head.

12. The process defined in claim 10 wherein said separating step includes removing said clay from said liquid medium by centrifugation of said liquid medium.

13. The process defined in claim 10 wherein the recovering step includes recycling said solvent to said stripper vessel and amending said solvent with additional solvent.

14. The process defined in claim 10 wherein said adding step includes agitating said sand in said water by passing a gas upwardly through said sand.

15. The process defined in claim 10 wherein said agitating step is followed by removing said residual bitumen from said water by passing said water and residual bitumen into an oil/water separator, said residual bitumen floating to the surface of said oil/water separator.

16. A process for recovering bitumen from a tar sand having a clay contaminant in the bitumen comprising:

mining a tar sand having a sand bonded by a bitumen and clay matrix;

screening said tar sand to remove large pieces of tar sand while introducing the tar sand into a stripper;

obtaining a solvent from a wellhead of a natural gas well, the solvent comprising a hydrocarbon condensate;

dissolving said bitumen by introducing said solvent into said stripper, the solvent releasing said sand from said bitumen and said clay and forming a liquid medium with said bitumen and said clay;

removing said clay from said liquid medium by processing said liquid medium in a centrifuge;

separating said solvent from said bitumen by evaporating said solvent in a distillation column;

recycling said solvent to said stripper;

washing said sand in a washer by passing water and a gas upwardly through said sand in said washer, said water including a carefully selected, nonanionic surface active agent, said surface active agent being present in an effective amount less than about 0.5%, by volume, and comprising a linear alcohol having carbon atoms within the range on the order of about eight to fifteen carbon atoms and ethoxylate groups within the range on the order of about two to eight ethoxylate groups, said water removing residual bitumen from said sand;

floating said bitumen from said water by passing said water into an oil/water separator;

recycling said water back to said washer; and

discharging sand from which bitumen has been removed from said washer.