Method for extracting bitumen from an oil sand stream
Abstract
The present invention provides a method for extracting bitumen from an oil sand stream that includes the steps of: providing an oil sand stream; contacting the oil sand stream with a liquid comprising a solvent thereby obtaining a solvent-diluted oil sand slurry; separating the solvent-diluted oil sand slurry, thereby obtaining a solids-depleted stream and a solids-enriched stream; increasing the S/B weight ratio of the solids-enriched stream thereby obtaining a solids-enriched stream having an increased S/B weight ratio and a liquid stream; filtering the solids-enriched stream having an increased S/B weight ratio, thereby obtaining bitumen-depleted sand. In another embodiment, the invention is a system for practicing this method.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A method for extracting bitumen from an oil sand stream, the method comprising at least the steps of:
providing an oil sand stream; contacting the oil sand stream with a liquid comprising a solvent thereby obtaining a solvent-diluted oil sand slurry; separating the solvent-diluted oil sand slurry, thereby obtaining a solids-depleted stream and a solids-enriched stream; increasing the solvent-to-bitumen (S/B) weight ratio of the solids-enriched stream thereby obtaining a solids-enriched stream having an increased S/B weight ratio and a liquid stream; and filtering the solids-enriched stream having an increased S/B weight ratio, thereby obtaining bitumen-depleted sand.
2 . The method of claim 1 , wherein the solvent comprises an aliphatic hydrocarbon, preferably having from 3 to 9 carbon atoms per molecule.
3 . The method of claim 2 , wherein the solvent comprises from 4 to 7 carbons per molecule, or a combination thereof.
4 . The method of claim 1 wherein the solvent-diluted oil sand slurry has a solvent-to-bitumen (S/B) weight ratio of from 0.5 to 4.0.
5 . The method of claim 4 wherein the solvent-diluted oil sand slurry has a solvent-to-bitumen (S/B) weight ration of from 0.7 to 3.0
6 . The method of claim 5 wherein the solvent-diluted oil sand slurry has a solvent-to-bitumen (S/B) weight ration of from 0.9 to 2.5.
7 . The method of claim 1 wherein the solvent-diluted oil sand slurry comprises from 10 to 60 vol. % of solids.
8 . The method of claim 7 wherein the solvent-diluted oil sand slurry comprises from 20 to 40 vol. % of solids.
9 . The method of claim 8 wherein the solvent-diluted oil sand slurry comprises from 25 to 35 vol. % of solids.
10 . The method of claim 1 wherein the solvent is removed from the solids-depleted stream thereby obtaining a bitumen-enriched stream.
11 . The method of claim 1 wherein the solids-enriched stream comprises from 30 to 65 vol. % of solids.
12 . The method of claim 11 wherein the solids-enriched stream comprises from 40 to 55 vol. % of solids.
13 . The method of claim 12 wherein the solids-enriched stream comprises from 45 to 55 vol. % of solids.
14 . The method of claim 1 wherein at least part of the liquid stream is used in the step of contacting the oil sand stream with a liquid comprising a solvent.
15 . The method claim 1 wherein the solids-enriched stream having an increased S/B weight ratio has an S/B weight ratio of from 1.5 to 8.0.
16 . The method claim 15 wherein the solids-enriched stream having an increased S/B weight ratio has an S/B weight ratio of from 2.0 to 7.0.
17 . The method claim 16 wherein the solids-enriched stream having an increased S/B weight ratio has an S/B weight ratio of from 2.2 to 6.0.
18 . The method of claim 1 wherein in the step of filtering the solids-enriched stream, a (“first”) bitumen-enriched filtrate is obtained, which is at least partly reused in the step of contacting the oil sand stream with a liquid comprising a solvent.
19 . The method of claim 18 wherein the bitumen-enriched filtrate has an S/B weight ratio of from 1.2 to 8.0.
20 . The method of claim 19 wherein the bitumen-enriched filtrate has an S/B weight ratio of from 2.0 to 7.0.
21 . The method of claim 20 wherein the bitumen-enriched filtrate has an S/B weight ratio of from 2.2 to 6.0.
22 . The method of claim 1 wherein in the step of filtering the solids-enriched stream having an increased S/B weight ratio, a (“second”) bitumen-depleted filtrate is obtained, and the (“second”) bitumen-depleted filtrate is at least partly reused in the step of increasing the solvent-to-bitumen (S/B) weight ratio of the solids-enriched stream.
23 . The method of claim 22 , wherein the bitumen-depleted filtrate has an S/B weight ratio of above 3.0.
24 . The method of claim 23 , wherein the bitumen-depleted filtrate has an S/B weight ratio of above 5.0.
25 . A system for performing a method for extracting bitumen from an oil sand stream, the system comprising:
a mixer for contacting an oil sand stream with a liquid, the liquid comprising a solvent, the mixer having an inlet for the oil sand stream and an outlet for a solvent-diluted oil sand slurry; a solid/liquid separator for separating the solvent-diluted oil sand slurry, the separator having a first outlet for a solids-depleted stream and a second outlet for a solids-enriched stream; a washer for increasing the S/B weight ratio of the solids-enriched stream, the washer having a first outlet for a solids-enriched stream having an increased S/B weight ratio and a second outlet for a liquid stream; and a filter for filtering the solids-enriched stream having an increased S/B weight ratio, the filter having an outlet for a bitumen-depleted sand.Cited by (0)
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