Plugging high permeability zones of reservoirs having heterogeneous permeability

Claim 3

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

Claim 4

The method defined in claim 1 wherein said cross-linking agent is a mixture of a compound of a multivalent metal at a higher valence state and a reducing agent capable of reducing the multivalent metal to a lower valence state, and wherein the compound of the multivalent metal is employed at a concentration of from about 0.05 to 60 percent by weight of the polymer and the reducing agent is employed at a concentration of from about 0.1 to 150 percent by weight of the stoichiometric amount required to reduce the multivalent metal from said higher valence state to said lower valence state.

Claim 5

The method defined in claim 1 wherein said cross-linking agent is a low molecular weight water-soluble aldehyde employed at a concentration of from about 0.01 to 50 percent by weight of the polymer.

Claim 6

The method defined in claim 1 wherein said cross-linking agent is a water-soluble salt of a polyvalent cation which reacts in solution to form a colloidal hydroxide employed at a concentration of from about 0.005 to 5 percent by weight of the polymer.

Claim 7

The method defined in claim 1 wherein all of the said compositions are admixed at the surface before injection into the reservoir.

Claim 8

The method defined in claim 1 wherein any two or more of the said compositions are admixed at the surface and simultaneously injected into the reservoir along with the remaining compositions.

Claim 9

The method defined in claim 1 wherein each of the said compositions are injected separately and simultaneously.

Claim 10

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

Claim 11

The method defined in claim 1 wherein said aqueous solution of alkali metal silicate contains from about 1 to 30 weight percent of said alkali metal silicate.

Claim 12

The method defined in claim 1 wherein said gelling agent is ammonium sulfate or ammonium bicarbonate.

Claim 13

The method defined in claim 1 wherein said gelling agent is employed at a concentration of one part by weight gelling agent per each part by weight alkali metal silicate employed.

Claim 14

The method defined in claim 1 wherein the alkali metal silicate solution and the gelling agent solution are admixed at the surface before injection into the reservoir.

Claim 15

The method defined in claim 1 wherein the alkali metal silicate solution and the gelling agent solution are injected into the reservoir as separate slugs.

Claim 16

The method defined in claim 1 wherein the relatively high molecular weight polymer is selected from the class consisting of an at least partially cationic polyacrylamide, an at least partially anionic polyacrylamide which has been partially hydrolyzed, and mixtures thereof.

Claim 17

In a method for the recovery of oil from a subterranean oil reservoir having strata of heterogeneous permeability and which is in communication with at least one producing well and at least one injection well, which method includes injection into the reservoir of a secondary or a tertiary recovery fluid via an injection well and recovery of oil via a production well, the improvement which comprises, at some point during the injection of the secondary or tertiary recovery fluid, introducing into the heterogeneous reservoir from about 5 to about 500 barrels per vertical foot of strata to be treated of a mixture of: a. about 10 to 90 percent by volume of an aqueous solution of a relatively high molecular weight polymer selected from the class consisting of acrylic acidacrylamide copolymers, polyacrylamides, partially hydrolyzed polyacrylamides, polyalkyleneoxides, carboxyalkylcelluloses, hydroxyethylcelluloses and heteropolysaccharides obtained by the fermentation of starch-derived sugar, b. a cross-linking amount of an aqueous solution of a cross-linking agent for polymer selected from the class consisting of mixtures of a compound of a multivalent metal and a reducing agent, a low molecular weight water-soluble aldehyde, and a water-soluble salt of a polyvalent cation which reacts in solution to form a colloidal hydroxide, c. about 90 to 10 percent by volume of an aqueous solution of an alkali metal silicate, and d. a gelling amount of an aqueous solution of a gelling agent for silicate selected from the group consisting of acid and acid-forming compounds, water-soluble ammonium salts, lower aldehydes, aluminum salts and alkali metal aluminates, and shutting in the well until a mixed polymer-silicate plug has formed.

Claim 18

In a method for the recovery of oil from a subterranean oil reservoir having strata of heterogeneous permeability and which is in communication with at least one producing well and at least one injection well, which method includes injection into the reservoir of a secondary or a tertiary recovery fluid via an injection well and recovery of oil via a production well, the improvement which comprises, at some point during the injection of the secondary or tertiary recovery fluid, introducing into the heterogeneous reservoir from about 5 to about 500 barrels per vertical foot of strata to be treated of a mixture of: a. about 10 to 90 percent by volume of an aqueous solution of a relatively high molecular weight polymer selected from the class consisting of acrylic acidacrylamide copolymers, polyacrylamides, partially hydrolyzed polyacrylamides, polyalkyleneoxides, carboxyalkylcelluloses, hydroxyethylcelluloses and heteropolysaccharides obtained by the fermentation of starch-derived sugar, b. a cross-linking amount of an aqueous solution of a cross-linking agent for polymer selected from the class consisting of mixtures of a compound of a multivalent metal and a reducing agent, a low molecular weight water-soluble aldehyde, and a water-soluble salt of a polyvalent cation which reacts in solution to form a colloidal hydroxide, c. about 90 to 10 percent by volume of an aqueous solution of an alkali metal silicate, and d. a gelling amount of an aqueous solution of a gelling agent for silicate selected from the group consisting of acid and acid-forming compounds, water-soluble ammonium salts, lower aldehydes, aluminum salts and alkali metal aluminates, and shutting in the well until a mixed polymer-silicate plug has formed.

Claim 19

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

Claim 20

The method defined in claim 16 wherein the cross-linking agent is a mixture of a compound of a multivalent metal and a reducing agent wherein the compound of a multivalent metal is employed at a concentration of from about 0.05 to 60 percent by weight of the polymer and the reducing agent is employed at a concentration of from about 0.1 to 150 percent by weight of the stoichiometric amount required to reduce the metal in a starting polyvalent state to a lower polyvalent state.

Claim 21

The method defined in claim 16 wherein the cross-linking agent is a low molecular weight water-soluble aldehyde employed at a concentration of from about 0.01 to 50 percent by weight of the polymer.

Claim 22

The method defined in claim 16 wherein the cross-linking agent is a water-soluble salt of a polyvalent cation which reacts in solution to form a colloidal hydroxide employed at a concentration of from about 0.005 to 5 percent by weight of the polymer.

Claim 23

The method defined in claim 16 wherein all of the said compositions are admixed at the surface before introduction into the reservoir.

Claim 24

The method defined in claim 16 wherein any two or more of the said compositions are admixed at the surface and simultaneously introduced into the reservoir along with the remaining compositions.

Claim 25

The method defined in claim 16 wherein each of the said compositions are introduced separately and simultaneously.

Claim 26

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

Claim 27

The method defined in claim 16 wherein the alkali metal silicate is employed at a concentration of from about 1 to 30 weight percent of the aqueous solution.

Claim 28

The method defined in claim 16 wherein the gelling agent is ammonium sulfate or ammonium bicarbonate.

Claim 29

The method defined in claim 16 wherein the gelling agent is employed at a concentration of one part by weight gelling agent per each part by weight alkali metal silicate employed.

Claim 30

The method defined in claim 16 wherein the alkali metal silicate solution and the gelling agent solution are admixed at the surface before introduction into the reservoir.

Claim 31

The method defined in claim 16 wherein the alkali metal silicate solution and the gelling agent solution are introduced into the reservoir as separate slugs.

Claim 32

The method defined in claim 16 wherein the relatively high molecular weight polymer is selected from the class consisting of an at least partially cationic polyacrylamide, an at least partially anionic polyacrylamide which has been partially hydrolyzed, and mixtures thereof.