Method for permeability correction by in situ genesis of macroemulsions in hard brine

Claim 2

A process for recovering oil from a subterranean oil-bearing reservoir having zones of varying permeability and containing connate water having divalent ions comprising the steps of: (a) injecting into said reservoir through at least one injection well a surfactant system, thereby selectively plugging high permeability zones, said surfactant system comprising: water; 0.5 to 12 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight within the range of 375 to 500; 250 to 17,000 parts per million by weight of a predominantly sodium chloride electrolyte based on the weight of said water; and 1 to 12 weight percent based on the weight of said water of a cosurfactant selected from the group consisting of amides, amines, esters, aldehydes and ketones containing 1 to 20 carbon atoms and alcohols containing 4 to 7 carbon atoms, which cosurfactant has a solubility in water within the range of 0.5 to 20 grams per 100 grams of water, said surfactant system having less than 1 weight percent oil; (b) thereafter injecting a secondary or tertiary oil recovery system through at least one injection well so as to displace oil toward at least one recovery well; and (c) recovering oil from said at least one production well.

Claim 3

A method according to claim 1 wherein said connate water has a concentration of divalent ions within the range of 300 to 10,000 ppm.

Claim 4

A method according to claim 2 wherein said divalent ions are predominantly calcium and magnesium.

Claim 5

A method according to claim 3 wherein said surfactant system of (a) is injected in an amount within the range of 0.01 to 0.05 pore volume of said reservoir.

Claim 6

A method according to claim 3 wherein the cosurfactant of step (a) is selected from the group consisting of amides, amines, esters, aldehydes and ketones having a solubility in water within the range of 2 to 10 grams per 100 grams of water.

Claim 7

A method according to claim 1 wherein said petroleum sulfonate has an equivalent weight of about 420, said cosurfactant is isobutyl alcohol and said electrolyte is present in an amount of about 15,000 parts per million.

Claim 8

A method according to claim 1 wherein the secondary or tertiary oil recovery system of step (b) comprises a surfactant system capable of forming a microemulsion in situ.

Claim 9

A method according to claim 7 wherein the surfactant system is followed by a mobility buffer and drive fluid.

Claim 10

A method according to claim 7 or claim 10 wherein the surfactant system of (b) comprises: water; 1 to 7 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight within the range of 375 to 500; 250 to 100,000 parts by million by weight of an electrolyte based on said water; and 1 to 12 weight percent based on the weight of said water of a cosurfactant, which cosurfactant has a solubility in water within the range of 5 to 20 grams per 100 grams of water, which surfactant system is thereafter followed by an injection of a mobility buffer and finally by the injection of a drive fluid.

Claim 11

A method according to claim 9 in which step (b) is preceded by a preflush to lower the concentration of divalent ions.

Claim 12

A method according to claim 1 or claim 9 wherein the cosurfactant of step (a) is at least one alcohol containing 4 to 7 carbon atoms.

Claim 13

A method according to claim 11 wherein the cosurfactant is selected from the group consisting of isobutyl alcohol, secondary butyl alcohol, n-butyl alcohol, n-amyl alcohol and isoamyl alcohol.

Claim 14

A method according to claim 12 wherein the cosurfactant is isobutyl alcohol.

Claim 15

A method according to claim 13 wherein the electrolyte is present in an amount within the range of 2,000 to 17,000 parts per million total dissolved solids and the petroleum sulfonate has an average equivalent weight within the range of 400 to 425.

Claim 16

A process for recovering oil from a subterranean oil-bearing reservoir having zones of varying permeability and containing connate water having divalent ions comprising the steps of: (a) injecting into said reservoir through at least one injection well a surfactant system comprising: water; 0.5 to 12 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight of about 420; 15,000 parts per million by weight of a predominantly sodium chloride electrolyte based on the weight of said water; and 1 to 12 weight percent based on the weight of said water of a cosurfactant, which cosurfactant is isobutyl alcohol, said surfactant system having less than 1 weight percent oil; (b) thereafter injecting a secondary or tertiary oil recovery system through at least one injection well so as to displace oil toward at least one recovery well, wherein said secondary or tertiary oil recovery system is a surfactant system comprising: water; 1 to 7 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight within the range of 375 to 500; 250 to 100,000 parts per million by weight of an electrolyte based on said water; and 1 to 12 weight percent based on the weight of said water of a cosurfactant, which cosurfactant has a solubility in water within the range of 0.5 to 20 grams per 100 grams of water, which surfactant system is thereafter followed by an injection of a mobility buffer and finally by the injection of a drive fluid.

Claim 17

A process for recovering oil from a subterranean oil-bearing reservoir having zones of varying permeability and containing connate water having divalent ions comprising the steps of: (a) injecting into said reservoir through at least one injection well a surfactant system comprising: water; 0.5 to 12 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight of about 420; 15,000 parts per million by weight of a predominantly sodium chloride electrolyte based on the weight of said water; and 1 to 12 weight percent based on the weight of said water of a cosurfactant, which cosurfactant is isobutyl alcohol, said surfactant system having less than 1 weight percent oil; (b) thereafter injecting a secondary or tertiary oil recovery system through at least one injection well so as to displace oil toward at least one recovery well, wherein said secondary or tertiary oil recovery system is a surfactant system comprising: water; 1 to 7 weight percent based on the weight of said water of a petroleum sulfonate surfactant having an average equivalent weight within the range of 375 to 500; 250 to 100,000 parts per million by weight of an electrolyte based on said water; and 1 to 12 weight percent based on the weight of said water of a cosurfactant, which cosurfactant has a solubility in water within the range of 0.5 to 20 grams per 100 grams of water, which surfactant system is thereafter followed by an injection of a mobility buffer and finally by the injection of a drive fluid.

Claim 18

A method according to claim 15 wherein said injection of (b) is preceded by a preflush to lower the concentration of divalent ions.

Claim 19

A method according to claim 16 wherein said electrolyte of (b) is present in an amount within the range of 2,000 to 50,000 ppm.