Selectively controlling fluid flow through the higher permeability zones of subterranean reservoirs

Claim 3

The method defined in claim 1 wherein said water-soluble relatively high molecular weight polymer is employed at a concentration of about 0.001 to 1 percent by weight of the aqueous solution.

Claim 4

The method defined in claim 1 wherein said water-soluble relatively high molecular weight polymer is employed at a concentration of about 0.05 to 0.15 percent by weight of the aqueous solution.

Claim 5

The method defined in claim 1 wherein said alkali metal silicate is employed at a concentration of about 0.05 to about 5 percent by weight of the aqueous solution.

Claim 6

The method defined in claim 1 wherein said alkali metal silicate is employed at a concentration of about 0.1 to 1.5 percent by weight of the aqueous solution.

Claim 7

The method defined in claim 1 wherein said alkali metal silicate is sodium silicate.

Claim 8

The method defined in claim 1 wherein the aqueous solutions are admixed at the surface prior to injection into the well.

Claim 9

The method defined in claim 1 wherein the aqueous solutions are injected sequentially into the well.

Claim 10

The method defined in claim 1 wherein the aqueous solutions are injected simultaneously into the well.

Claim 11

The method defined in claim 1 wherein the aqueous solution of an alkali metal silicate additionally contains an effective amount of a cellulose ether thickener.

Claim 12

The method defined in claim 10 wherein the cellulose ether is hydroxyethylcellulose.

Claim 13

The method defined in claim 1 wherein the high to medium permeability strata have a permeability of about 50 to 1,000 milldarcys.

Claim 14

The method defined in claim 1 wherein the said aqueous solution or dispersion of a water-soluble relatively high molecular weight polymer and the said aqueous solution or dispersion of an alkali metal silicate are substantially free of a cross-linking agent and a gelling agent.

Claim 15

The method defined in claim 1 wherein the reduction in permeability takes place at a distance of about 35 to 100 feet or more from the well.

Claim 16

The method defined in claim 1 wherein the reduction in permeability becomes effective from about two weeks in two months or longer after injection into the reservoir.

Claim 17

In a method for enhanced oil recovery wherein a drive fluid is injected into a reservoir having heterogeneous permeability via one or more injection wells to displace oil toward one or more production wells, the improvement which comprises reducing the permeability of the medium to high permeability strata or channels of said reservoir by interrupting the injection of the drive fluid to inject into the said injection well and into the said reservoir a slug of about 1 to 100 barrels per vertical foot of strata to be treated of a first composition consisting essentially of an aqueous solution or dispersion of a water-soluble relatively high molecular weight polymer selected from the group consisting of acrylic acid-acrylamide copolymers, terpolymers of acrylamides and substituted acrylamides, polyacrylamides, partially hydrolyzed polyacrylamides, polyalkyleneoxides and heteropolysaccharides obtained by by the fermentation of starch-derived sugar, and about 1 to 100 barrels per vertical foot of a second composition consisting essentially of an aqueous solution on dispersion of an alkali metal silicate, which solutions are substantially free of a cross-linking agent and a gelling agent, which solutions mix and pass through the reservoir to form at a substantial distance from the injection well a fluid flow restricting composition which remains capable of at least limited fluid flow through the reservoir.

Claim 18

In a method for enhanced oil recovery wherein a drive fluid is injected into a reservoir having heterogeneous permeability via one or more injection wells to displace oil toward one or more production wells, the improvement which comprises reducing the permeability of the medium to high permeability strata or channels of said reservoir by interrupting the injection of the drive fluid to inject into the said injection well and into the said reservoir a slug of about 1 to 100 barrels per vertical foot of strata to be treated of a first composition consisting essentially of an aqueous solution or dispersion of a water-soluble relatively high molecular weight polymer selected from the group consisting of acrylic acid-acrylamide copolymers, terpolymers of acrylamides and substituted acrylamides, polyacrylamides, partially hydrolyzed polyacrylamides, polyalkyleneoxides and heteropolysaccharides obtained by by the fermentation of starch-derived sugar, and about 1 to 100 barrels per vertical foot of a second composition consisting essentially of an aqueous solution on dispersion of an alkali metal silicate, which solutions are substantially free of a cross-linking agent and a gelling agent, which solutions mix and pass through the reservoir to form at a substantial distance from the injection well a fluid flow restricting composition which remains capable of at least limited fluid flow through the reservoir.

Claim 19

The method defined in claim 16 wherein said water-soluble relatively high molecular weight polymer is employed at a concentration of about 0.001 to 1 percent by weight of the aqueous solution.

Claim 20

The method defined in claim 16 wherein said water-soluble relatively high molecular weight polymer is employed at a concentration of about 0.05 to 0.15 percent by weight of the aqueous solution.

Claim 21

The method defined in claim 16 wherein said alkali metal silicate is employed at a concentration of about 0.05 to about 5 percent by weight of the aqueous solution.

Claim 22

The method defined in claim 16 wherein said alkali metal silicate is employed at a concentration of about 0.1 to 1.5 percent by weight of the aqueous solution.

Claim 23

The method defined in claim 16 wherein said alkali metal silicate is sodium silicate.

Claim 24

The method defined in claim 16 wherein the aqueous solutions are admixed at the surface prior to injection into the well.

Claim 25

The method defined in claim 16 wherein the aqueous solutions are injected sequentially into the well.

Claim 26

The method defined in claim 16 wherein the aqueous solutions are injected simultaneously into the well.

Claim 27

The method defined in claim 16 wherein the aqueous solution of an alkali metal silicate additionally contains an effective amount of a cellulose ether thickener.

Claim 28

The method defined in claim 25 wherein the cellulose ether is hydroxyethylcellulose.

Claim 29

The method defined in claim 16 wherein the high to medium permeability strata have a permeability of about 50 to 1,000 darcys.

Claim 30

The method defined in claim 16 wherein the reduction is permeability takes place at a distance of about 35 to 100 feet or more from the well.

Claim 31

The method defined in claim 16 wherein the reduction in permeability becomes effective from about two weeks to two months or longer after injection into the reservoir.