Conformance control, sweep efficiency, deep diversion, and water shutoff method
US-2023184072-A1 · Jun 15, 2023 · US
US2025257640A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025257640-A1 |
| Application number | US-202418439583-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 12, 2024 |
| Priority date | Feb 12, 2024 |
| Publication date | Aug 14, 2025 |
| Grant date | — |
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The present disclosure relates to methods for enhanced oil recovery (EOR) from a subterranean formation by injecting a mixture including an anionic surfactant and an amine, followed by injecting CO2, to reduce CO2 mobility in a high-permeability zone of the formation.
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What is claimed is: 1 . A method of enhanced oil recovery (EOR) from a subterranean formation comprising a high-permeability zone and a low-permeability zone, the method comprising: injecting, through a wellbore into the high-permeability zone, a mixture comprising an anionic surfactant and an amine and having a viscosity of less than about 0.01 Pas at a shear rate from about 0.1 to about 1000 s −1 ; injecting CO 2 through the wellbore into the high-permeability zone to increase a viscosity of the mixture in the high-permeability zone, wherein increasing the viscosity of the mixture reduces a mobility of CO 2 in the high-permeability zone; and injecting CO 2 through the wellbore into the low-permeability zone to stimulate a flow of hydrocarbons from the low-permeability zone. 2 . The method of claim 1 , wherein the anionic surfactant comprises a carboxylate surfactant, a sulfonate surfactant, a sulfate surfactant, or any combination thereof. 3 . The method of claim 2 , wherein the anionic surfactant comprises an alkyl group, an alkenyl group, or an alkyl alcohol ether group. 4 . The method of claim 3 , wherein the alkyl group comprises a C 12-22 alkyl group. 5 . The method of claim 3 , wherein the alkyl group comprises a C 12-22 alkenyl group. 6 . The method of claim 3 , wherein the alkyl alcohol ether group comprises a C 12-22 alkyl alcohol polyoxyethylene group. 7 . The method of claim 2 , wherein the anionic surfactant comprises a compound of Formula I, Formula II, or Formula III: wherein: R 1 is the sum of m and q is an integer from 12 to 22; n is an integer from 0 to 10; p is 0 or 1; and X + is Li + , Na + , K + , Cs + , Ag + , or (R A ) 4 N + , wherein each occurrence of R A is selected from H, C 1-6 alkyl, C 3-6 cycloalkyl, 4- to 7-membered heterocycloalkyl, C 6-10 aryl, and 5- to 10-membered heteroaryl; each C 1-6 alkyl is optionally substituted with 1-3 R B independently selected from C 3-6 cycloalkyl, 4- to 7-membered heterocycloalkyl, C 6-10 aryl, and 5- to 10-membered heteroaryl; and optionally, one or more instances of R A are taken together with the nitrogen atom to which they are attached to form a 4- to 7-membered heterocycloalkyl. 8 . The method of claim 7 , wherein n is from 1 to 10; and p is 1. 9 . The method of claim 7 , wherein n, p, and q are each 0. 10 . The method of claim 2 , wherein the anionic surfactant comprises sodium dodecyl sulfate, sodium tetradecyl sulfate, sodium hexadecyl sulfate, sodium octadecyl sulfate, or any combination thereof. 11 . The method of claim 1 , wherein the amine comprises an alkylene diamine, alkylene triamine, alkanolamine, or any combination thereof. 12 . The method of claim 1 , wherein the amine comprises a compound of Formula IV: wherein R 2 is selected from C 1-6 alkyl, C 3-6 cycloalkyl, 4- to 7-membered heterocycloalkyl, C 6-10 aryl, and 5- to 10-membered heteroaryl; R 3 and R 4 are each independently selected from —H, C 1-6 alkyl, C 3-6 cycloalkyl, 4- to 7-membered heterocycloalkyl, C 6-10 aryl, and 5- to 10-membered heteroaryl; each C 1-6 alkyl and C 6-10 aryl is optionally substituted with 1-3 R C ; each R C is independently selected from —OH and —N(R D ) 2 ; and each R D is independently selected from —H and C 1-4 alkyl. 13 . The method of claim 12 , wherein R 2 is C 1-6 alkyl or phenyl; R 3 and R 4 are each independently selected from —H, C 1-6 alkyl, and phenyl; and each R C is independently selected from —OH and —NH 2 . 14 . The method of claim 1 , wherein the amine comprises diethylene triamine, bis(hexamethylene) triamine, 2-(dimethylamino) ethanol, or any combination thereof. 15 . The method of claim 1 , wherein the anionic surfactant and the amine are present in the mixture in a molar ratio of about 5:1 to about 1:5. 16 . The method of claim 1 , wherein the anionic surfactant and the amine are present in the mixture in a molar ratio of about 2:1 to about 1:2. 17 . The method of claim 1 , wherein a total concentration of the anionic surfactant and the amine in the high-permeability zone after injecting the mixture is about 0.01 mol/L to about 2 mol/L. 18 . The method of claim 1 , wherein a total concentration of the anionic surfactant and the amine in the high-permeability zone after injecting the mixture is about 0.1 mol/L to about 0.75 mol/L. 19 . The method of claim 1 , wherein the viscosity of the mixture before injecting CO 2 is less than about 0.005 Pa·s at a shear rate from about 0.1 to about 1000 s −1 . 20 . The method of claim 1 , wherein injecting CO 2 increases the viscosity of the mixture in the high-permeability zone to greater than about 0.01 Pa·s at a shear rate from about 0.1 to about 1000 s −1 . 21 . The method of claim 1 , wherein a depth of the low-permeability zone is greater than a depth of the high-permeability zone. 22 . A method of enhanced oil recovery (EOR) from a subterranean formation comprising a high-permeability zone and a low-permeability zone, the method comprising: expanding an upper seal of the straddle packer above the high-permeability zone and expanding a lower seal of the straddle packer below the high-permeability zone to mechanically isolate the high-permeability zone; injecting a mixture comprising an anionic surfactant and an amine through the straddle packer into the high-permeability zone; injecting CO 2 through the wellbore into the high-permeability zone to increase a viscosity of the mixture in the high-permeability zone, wherein increasing the viscosity of the mixture reduces a mobility of CO 2 in the high-permeability zone; removing the straddle packer from the wellbore after increasing the viscosity of the mixture; and injecting CO 2 through the wellbore into the low-permeability zone to stimulate a flow of hydrocarbons from the low-permeability zone.
Compositions used in combination with injected gas {, e.g. CO2 orcarbonated gas}(C09K8/592 takes precedence) · CPC title
characterised by the use of specific surfactants · CPC title
Injecting CO2 or carbonated water (in combination with organic material C09K8/594) · CPC title
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