Additives for improving hydrocarbon recovery
View Patent ↗A hydrocarbon from a subterranean formation can be recovered by contacting the hydrocarbon with water or steam and one or more additives. The hydrocarbon can be selected from heavy or light crude oil, bitumen, an oil sand ore, a tar sand ore, and combinations thereof. The additive can be, for example, an aromatic hydrocarbon. The water or steam and the additive can be injected into the subterranean formation. Compositions or mixtures include hydrocarbons, water or steam, and additives.
1. A process for recovering a hydrocarbon from a subterranean formation comprising the steps of: (i) contacting a hydrocarbon from a subterranean formation with steam or water; (ii) contacting the hydrocarbon from the subterranean formation with one or more aromatic hydrocarbons, wherein the hydrocarbon from the subterranean formation is contacted with the steam or water and the one or more aromatic hydrocarbons inside of the subterranean formation, wherein the one or more aromatic hydrocarbons have atmospheric boiling points of less than or equal to about 300° C. and/or the one or more aromatic hydrocarbons comprise a functional group selected from: an alcohol, ether, aldehyde, ketone, carboxylic acid, ester, and combinations thereof, and wherein the one or more aromatic hydrocarbons are added at a concentration from about 250 to about 50,000 ppm by weight of the aromatic hydrocarbon in the steam; and (iii) recovering the hydrocarbon from the subterranean formation.
2. The process of claim 1 , wherein the hydrocarbon from the subterranean formation is selected from: heavy or light crude oil, bitumen, an oil sand ore, a tar sand ore, and combinations thereof.
3. The process of claim 1 , wherein contacting the hydrocarbon from the subterranean formation with the water or steam and/or the one or more aromatic hydrocarbons occurs at any time during recovery of the hydrocarbon from the subterranean formation.
4. The process of claim 1 , wherein the one or more aromatic hydrocarbons are selected from: methyl salicylate, methylsalicylic acid (3,4,5, or 6-methyl substituted), salicylic acid, phenyl acetate, benzoic acid, methyl 4-hydroxybenzoate, benzyl acetate, benzaldehyde, and acetophenone, and any combination or mixture thereof.
5. The process of claim 1 , wherein the one or more aromatic hydrocarbons are added at a concentration from about 1000 to about 50,000 ppm by weight of the aromatic hydrocarbon in the steam.
6. The process of claim 1 , wherein contacting the hydrocarbon with the steam and the aromatic hydrocarbons comprises injecting the steam and the aromatic hydrocarbons into the subterranean formation independently or injecting the steam and the aromatic hydrocarbons into the subterranean formation as a mixture.
7. The process of claim 1 , wherein the subterranean formation comprises any number of wells.
8. The process of claim 1 , wherein the subterranean formation comprises two wells.
9. A process for the recovery of bitumen from a subterranean formation comprising the steps of: (i) contacting the bitumen with steam or water; (ii) contacting the bitumen with one or more aromatic hydrocarbons, wherein the bitumen is contacted with the steam or water and the one or more aromatic hydrocarbons inside of the subterranean formation, wherein the one or more aromatic hydrocarbons have atmospheric boiling points of less than or equal to about 300° C. and/or the one or more aromatic hydrocarbons comprise a functional group selected from: an alcohol, ether, aldehyde, ketone, and ester, and combinations thereof; and (iii) recovering the bitumen.
10. The process of claim 9 , wherein contacting the bitumen with the steam or water and/or the one or more aromatic hydrocarbons occurs at any time during recovery of the bitumen.
11. The process of claim 9 , wherein the one or more aromatic hydrocarbons are selected from: methyl salicylate, phenyl acetate, methyl 4-hydroxybenzoate, benzyl acetate, benzaldehyde, and acetophenone, and any combination or mixture thereof.
12. The process of claim 9 , wherein the one or more aromatic hydrocarbons are added at a concentration from about 25 to about 50,000 ppm by weight of the aromatic hydrocarbon in the steam.
13. The process of claim 9 , wherein contacting the bitumen with the steam and the aromatic hydrocarbons comprises injecting the steam and the aromatic hydrocarbons into the subterranean formation independently or injecting the steam and the aromatic hydrocarbons into the subterranean formation as a mixture.
14. The process of claim 9 , wherein the subterranean formation comprises any number of wells.
15. The process of claim 9 , wherein the subterranean formation comprises two wells.