Method for improved oil recovery

Claim 2

A non-thermal, single-well method for improved oil recovery from a hydrocarbon-bearing reservoir with essentially no natural drive in which: (a) a volume of a chemical surfactant/cosurfactant/brine mixture, greater than a volume required to fill the well bore and immediate vicinity thereo into a well penetrating the reservoir, which surfactant/cosurfactant/brine mixture is preformulated to produce a stable, low interfacial tension, three-phase, hydrocarbon-microemulsion-brine system with a sample of the hydrocarbon of the reservoir; (b) a subterranean, intra-reservoir, low interfacial tension, three-phase, hydrocarbon-microemulsion-brine system is formed; and (c) the low interfacial tension, three-phase, hydrocarbon-microemulsion-brine system is produced from the same well into which the surfactant/cosurfactant/brine mixture is injected.

Claim 3

The method according to claim 1 in which the hydrocarbon phase of the three-phase, hydrocarbon-microemulsion-brine system is subsequently separated from the microemulsion and brine phases and the microemulsion and brine phases are recovered and substituted for the chemical surfactant/corsurfactant/brine mixture in a subsequent performance of the method according to claim 1.

Claim 4

The method according to claim 1 in which the surfactant/cosurfactant/brine mixture comprises a surfactant package in water produced from the reservoir.

Claim 5

The method according to claim 1 in which the surfactant/cosurfactant/brine mixture comprises a surfactant package in a simulated brine formulated to have a salinity which is the same as the salinity of water naturally existing in the reservoir.

Claim 6

The method according to claim 1 in which the surfactant/cosurfactant/brine mixture comprises a surfactant package in a synthetic brine having a salinity differing from the salinity of water in the reservoir, so formulated to achieve a stable, three-phase, hydrocarbon-microemulsionbrine system.

Claim 7

The method according to claim 3, 4 or 5 in which the surfactant package comprises a nonionic surfactant and an alcohol cosurfactant.

Claim 8

The method according to claim 3, 4 or 5 in which the surfactant package comprises an anionic surfactant and an alcohol cosurfactant.

Claim 9

The method according to claim 7 in which the surfactant package further comprises a nonionic surfactant.

Claim 10

The method according to claim 8 wherein the anionic surfactant is a sulfonate and the nonionic surfactant is an alkylphenol.

Claim 11

The method according to claim 3, 4 or 5 in which the surfactant package comprises about 40% to about 70% by weight of an anionic surfactant, about 10% to about 40% by weight of a nonionic surfactant and about 5% to about 15% by weight of a cosurfactant.

Claim 12

The method according to claim 3, 4 or 5 in which the surfactant package comprises about 50% by weight of petroleum sulfonate, about 10% by weight of ethoxylated nonylphenol having about 7 ethoxy groups and about 40% by weight of n-propyl alcohol.

Claim 13

The method according to claim 1 in which the hydrocarbon in the reservoir has a viscosity from about 100 to about 1500 centipoise at ambient reservoir temperature.

Claim 14

The method according to claim 1 in which the hydrocarbon has a paraffinic content from about 42% to about 83% by weight and an aromatic content from about 15% to about 50% by weight.

Claim 15

The method according to claim 1 in which the hydrocarbon has a viscosity of about 1200 centipose at 26° C., a paraffinic content of about 54% by weight and an aromatic content of about 46% by weight.

Claim 16

The method according to claim 1 in which the hydrocarbon is selected from the group consisting of Gold Energy crude oil, Middendorf #3 crude oil, Harvey Meyer crude oil and Altamont crude oil.

Claim 17

The method according to claim 1 in which the reservoir is a subterranean shallow rock formation.

Claim 18

The method according to claim 1 in which the reservoir is a subterranean shallow sand formation.

Claim 19

The method according to claim 1 in which the reservoir has a high degree of natural fracturing such that there is substantially no fluid communication among wells drilled into the reservoir.

Claim 20

The method according to claim 1 in which the surfactant/cosurfactant/brine mixture is injected into the well at a pressure less than the fracture pressure of the reservoir.

Claim 21

The method according to claim 1 in which hydrocarbon is produced from the well at an average rate of about three times the original rate of hydrocarbon production during a period of about two weeks after injection of the surfactant/cosurfactant/brine mixture.

Claim 22

The method according to claim 2 in which the percent recovery of surfactant/cosurfactant in the brine after breaking the hydrocarbon-in-water emulsion is about 95% or greater.

Claim 23

A non-thermal, single-well method for improved recovery of a viscous hydrocarbon from a shallow subterranean resevoir with essentially no natural drive in which: (a) a volume of a mixture of a surfactant package comprising about 50% by weight of petroleum sulfonate, about 10% by weight of ethoxylated nonylphenol with about 7 ethoxy groups and about 40% by weight of n-propyl alcohol in produced water or a simulation thereof, such mixture being preformulated to produce a stable, low interfacial tension, three-phase, hydrocarbon-microemulsion-produced water system with a sample of the viscous hydrocarbon of the resevoir, such volume being greater than a volume required to fill the well bore and immediate vicinity thereof and sufficient to permeate into the reservoir, is injected into a well penetrating the resevoir; (b) a subterranean, intra-reservoir, low interfacial tension, three-phase, hydrocarbon-microemulsion-produced water system is formed; and (c) the low interfacial tension, three-phase, hydrocarbon-microemulsion-produced water system is produced from the same well into which the surfactant package/aqueous mixture is injected.

Claim 24

A non-thermal, single-well method for improved recovery of a viscous hydrocarbon from a shallow subterranean resevoir with essentially no natural drive in which: (a) a volume of a mixture of a surfactant package comprising about 50% by weight of petroleum sulfonate, about 10% by weight of ethoxylated nonylphenol with about 7 ethoxy groups and about 40% by weight of n-propyl alcohol in produced water or a simulation thereof, such mixture being preformulated to produce a stable, low interfacial tension, three-phase, hydrocarbon-microemulsion-produced water system with a sample of the viscous hydrocarbon of the resevoir, such volume being greater than a volume required to fill the well bore and immediate vicinity thereof and sufficient to permeate into the reservoir, is injected into a well penetrating the resevoir; (b) a subterranean, intra-reservoir, low interfacial tension, three-phase, hydrocarbon-microemulsion-produced water system is formed; and (c) the low interfacial tension, three-phase, hydrocarbon-microemulsion-produced water system is produced from the same well into which the surfactant package/aqueous mixture is injected.