US2009145809A1PendingUtilityA1
Compositions for oil recovery and methods of using same
Assignee: CHEVRON PHILLIPS CHEMICAL COPriority: Dec 10, 2007Filed: Dec 10, 2007Published: Jun 11, 2009
Est. expiryDec 10, 2027(~1.4 yrs left)· nominal 20-yr term from priority
C10G 2300/44C10G 2300/4081C10G 2300/302C10G 2300/308C10G 2300/1055C10G 1/04
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Claims
Abstract
A method of removing bitumen from tar sands comprising contacting the tar sands with a first mixture comprising a petroleum distillate and an oxygenated solvent, and recovering a second mixture comprising (a) at least a portion of the petroleum distillate and oxygenated solvent from the first mixture, (b) bitumen and (c) sand having a reduced amount of bitumen.
Claims
exact text as granted — not AI-modified1 . A method of removing bitumen from tar sands comprising:
contacting the tar sands with a first mixture comprising a petroleum distillate and an oxygenated solvent, and recovering a second mixture comprising (a) at least a portion of the petroleum distillate and oxygenated solvent from the first mixture, (b) bitumen and (c) sand having a reduced amount of bitumen.
2 . The method of claim 1 wherein the bitumen has an API gravity of equal to or less than about 10°.
3 . The method of claim 1 wherein the bitumen has a viscosity of equal to or greater than about 0.2 Pa·S.
4 . The method of claim 1 wherein the petroleum distillate comprises diesel.
5 . The method of claim 1 wherein the petroleum distillate is present in the first mixture in an amount of from about 2% to about 90%.
6 . The method of claim 1 wherein the oxygenated solvent comprises a glycol ether.
7 . The method of claim 6 wherein the glycol ether comprises ethylene glycol monoalkyl ether, ethylene glycol dialkyl ether, diethylene glycol butyl ether, diethylene glycol ethyl ether, ethylene glycol monobutyl ether, combinations thereof.
8 . The method of claim 1 wherein the oxygenated solvent is present in the first mixture in an amount of from about 10% to about 98%.
9 . The method of claim 1 wherein the first mixture further comprises a surfactant.
10 . The method of claim 9 wherein the surfactant comprises an alkyl polyglycoside.
11 . The method of claim 9 wherein the surfactant is present in the first mixture in an amount of from about 0.01% to about 1%.
12 . The method of claim 1 wherein the percent recovery of the bitumen from the tar sands is equal to or greater than about 50% by weight.
13 . The method of claim 1 wherein the contacting occurs via a counter current flow of the tar sands and the first mixture.
14 . The method of claim 1 wherein the contacting occurs via filtration of the first mixture through the tar sands.
15 . The method of claim 14 wherein the filtration further comprises passing the second mixture through a membrane.
16 . The method of claim 1 further comprising separating the bitumen from the petroleum distillate and the oxygenated solvent in the second mixture.
17 . The method of claim 16 further comprising converting at least a portion of the bitumen to a lighter petroleum product.
18 . The method of claim 17 further comprising recycling all or a portion of the lighter petroleum product to the first mixture.
19 . The method of claim 16 further comprising recycling all or a portion of the petroleum distillate and oxygenated solvent to the first mixture.
20 . The method of claim 1 further comprising scrubbing the recovered sand.
21 . The method of claim 20 further comprising contacting the scrubbed sand with additional solvent.Join the waitlist — get patent alerts
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