Bitumen extraction process

Patent metadata

Field	Value
Publication number	US-10519381-B2
Application number	US-201314648734-A
Country	US
Kind code	B2
Filing date	Dec 10, 2013
Priority date	Dec 19, 2012
Publication date	Dec 31, 2019
Grant date	Dec 31, 2019

Abstract

A process for the extraction and recovery of bitumen from oil sands using deionized silicate solutions. Bitumen is recovered in a process comprising contacting a deionized silicate solution with an ore sand oil to produce a froth comprising bitumen and a tailings stream comprising water, sand and clay fines and optionally unrecovered bitumen. Preferably the tailings stream is dewatered and recovered water may be recycled to the extraction process.

First claim

What is claimed is:

1. A process for extracting bitumen from an oil sands ore, comprising (a) providing an aqueous slurry of an oil sands ore, and (b) contacting the slurry with a deionized silicate solution and optionally a caustic, to extract bitumen from the ore to produce i) a froth comprising bitumen, and ii) an aqueous tailings stream comprising sand and clay fines;
wherein the deionized silicate solution has a molar ratio of Si:M of at least 2.6, wherein M is an alkali metal and the deionized silicate solution has a S-value of 50% or greater.

2. A process according to claim 1 further comprising (c) dewatering the aqueous tailings stream.

3. A process of claim 2 further comprising adding an anionic polyacrylamide or an anionic polyacrylamide and a low molecular weight cationic organic polymer after step (b) and before step (c) to flocculate the aqueous tailings stream.

4. A process of claim 1 wherein air is added during the contacting step (b).

5. A process according to claim 1 wherein the temperature in step (b) is 25 to 90° C.

6. A process according to claim 1 wherein the deionized silicate solution is a deionized colloidal silica.

7. A process according to claim 1 further comprising, after step (b) a step (d) permitting separation of the aqueous tailings stream into a middlings and a coarse tailings.

8. A process according to claim 7 further comprising removing the froth from the aqueous tailings and contacting the froth with solvent to extract bitumen from the froth and to produce a froth treatment tailings.

9. A process according to claim 8 wherein the solvent is selected from the group consisting of paraffinic C 5 to C 8 n-alkanes, and naphthenic solvents.

10. A process according to claim 7 further comprising contacting the middlings with air to produce a second froth, a second middlings and a fine tailings, and permitting separation of the second froth and the fine tailings.

11. A process according to claim 10 further comprising contacting the second middlings with air to produce a third froth and a second fine tailings.

12. A process of claim 1 wherein the aqueous tailings stream comprises 1) a middlings stream of unrecovered bitumen and clay fines; and 2) a coarse tailings stream comprising sand and clay fines.

13. A process according to claim 1 further comprising, after step (b) and before step (c), step (d) permitting separation of the aqueous tailings stream into a middlings and a coarse tailings wherein step (c) comprises dewatering the middlings and coarse tailings separately.

14. A process according to claim 13 further comprising removing the froth from the aqueous tailings and contacting the froth with solvent to extract bitumen from the froth and to produce a froth treatment tailings.

15. A process according to claim 14 wherein the solvent is selected from the group consisting of paraffinic C 5 to C 8 n-alkanes, and naphthenic solvents.

16. A process according to claim 10 further comprising contacting the second middlings with air to produce a third froth and a second fine tailings.

17. A process according to claim 1 wherein the deionized silicate solution is prepared by contacting a solution of sodium silicate with a strong cation exchange resin.

18. A process according to claim 1 wherein the deionized silicate solution is prepared by contacting a solution of sodium silicate with a weak cation exchange resin.

19. A process according to claim 1 wherein the deionized silicate solution is prepared by removing alkali metal from a solution of alkali metal silicate using bipolar electrolysis.

Assignees

• Chemours Co Fc Llc

Inventors

• Moffett Robert Harvey

Classifications

• C04B18/049

  Wastes from oil or other wells, e.g. drilling mud · CPC title

• C10G21/14

  Hydrocarbons · CPC title

• C10G21/26

  Silicon-containing compounds · CPC title

• C10G1/047

  Hot water or cold water extraction processes · CPC title

• C10G1/045 Primary

  Separation of insoluble materials · CPC title