Process for recovery of mineral values from underground formations

Claim 2

In a method for the solution mining of a substance which in an oxidized state is soluble in an aqueous leaching solution, said method comprising the steps of (1) introducing an oxidant and an aqueous leaching solution into a subterranean deposit containing said substance, thereby to solubilize said substance in situ to form a pregnant liquor, (2) recovering said pregnant liquor from said deposit, and (3) separating said substance from said pregnant liquor, the improvement comprising: utilizing as said aqueous leaching solution a solution comprising a dilute aqueous carbonic acid solution and said oxidant.

Claim 3

The method of claim 1 wherein the concentration of said carbonic acid is sufficient to provide a bicarbonate ion concentration in said leaching solution between about 380 ppm and about 1000 ppm.

Claim 4

The method of claim 1 wherein the concentration of said carbonic acid is sufficient to provide a bicarbonate ion concentration in said leaching solution of between about 460 ppm and about 700 ppm.

Claim 5

The method of claim 1 further including the step of introducing gaseous carbon dioxide and a water soluble oxidizing agent into water thereby to form said leaching solution.

Claim 6

The method of claim 1 wherein said substance is selected from the group consisting of uranium, thorium, vanadium, copper, nickel, molybdenum, rhenium and selenium.

Claim 7

The method of claim 1 wherein said substance is uranium.

Claim 10

The method of claim 7 wherein the concentration of said carbonic acid in said leaching solution is sufficient to provide a bicarbonate ion concentration in said leaching solution between about 460 ppm and about 700 ppm.

Claim 11

The method of claim 7 wherein the concentration of said carbonic acid in said leaching solution is sufficient to provide a bicarbonate ion concentration in said pregnant liquor between about 600 ppm and about 690 ppm.

Claim 12

The method of claim 7 wherein said oxidizing agent is selected from the group consisting of potassium permanganate, hydrogen peroxide, potassium ferricyanide, sodium hypochlorite, potassium peroxydisulfate, oxygen and oxygen-containing gases.

Claim 13

The method of claim 7 wherein said oxidant is hydrogen peroxide.

Claim 14

The method of claim 7 wherein the concentration of said oxidizing agent in said leaching solution is between about 50 ppm and about 200 ppm on a free oxygen basis.

Claim 15

The method of claim 7 wherein said carbonic acid solution is formed by introducing gaseous carbon dioxide into water thereby to form an aqueous solution of at least a portion of said carbon dioxide.

Claim 16

A process for the recovery of uranium values from a subterranean deposit comprising the steps of: (a) penetrating said deposit with at least one injection well and at least one production well in spaced relation with said injection well; (b) introducing an aqueous leaching solution comprising carbonic acid and an oxidizing agent selected from the group consisting of hydrogen peroxide, oxygen and oxygen-containing gases from said injection well into said deposit to leach in situ uranium values therefrom thereby forming a pregnant liquor, the concentration of said carbonic acid in said leaching solution being sufficient to provide a bicarbonate ion concentration in said leaching solution between about 380 ppm and about 1000 ppm and the concentration of said oxidizing agent in said leaching solution being between about 50 ppm and about 200 ppm on a free oxygen basis; (c) recovering said pregnant liquor at said production well; (d) forming a barren liquor by separating said uranium values from said pregnant liquor; (e) introducing gaseous carbon dioxide and said oxidizing agent into said barren liquor thereby to form said aqueous leaching solution; and (f) recycling at least a portion of the solution formed in step (e) for reintroduction into said deposit in step (b).

Claim 17

A process for the recovery of uranium values from a subterranean deposit comprising the steps of: (a) penetrating said deposit with at least one injection well and at least one production well in spaced relation with said injection well; (b) introducing an aqueous leaching solution comprising carbonic acid and an oxidizing agent selected from the group consisting of hydrogen peroxide, oxygen and oxygen-containing gases from said injection well into said deposit to leach in situ uranium values therefrom thereby forming a pregnant liquor, the concentration of said carbonic acid in said leaching solution being sufficient to provide a bicarbonate ion concentration in said leaching solution between about 380 ppm and about 1000 ppm and the concentration of said oxidizing agent in said leaching solution being between about 50 ppm and about 200 ppm on a free oxygen basis; (c) recovering said pregnant liquor at said production well; (d) forming a barren liquor by separating said uranium values from said pregnant liquor; (e) introducing gaseous carbon dioxide and said oxidizing agent into said barren liquor thereby to form said aqueous leaching solution; and (f) recycling at least a portion of the solution formed in step (e) for reintroduction into said deposit in step (b).

Claim 18

The process of claim 14 wherein said carbon dioxide and said oxidizing agent are introduced into said barren liquor prior to reinjecting the solution thus formed into said injection well as said leaching solution.

Claim 19

The process of claim 14 wherein said leaching solution has a pH of between about 6 and about 7.

Claim 20

The process of claim 14 wherein said leaching solution has a carbonic acid concentration sufficient to provide a bicarbonate ion concentration in said leaching solution of between about 460 ppm and about 700 ppm.

Claim 21

The process of claim 14 wherein said carbon dioxide is introduced directly into said injection well and is therein solubilized in an aqueous solution comprising said barren liquor and said oxidizing agent to thereby form said leaching solution in said injection well.

Claim 22

The method of claim 1 wherein said oxidant is selected from the group consisting of potassium permanganate, hydrogen peroxide, potassium ferricyanide, sodium hypochlorite, potassium peroxydisulfate, oxygen and oxygen-containing gases.

Claim 23

The method of claim 1 wherein the concentration of said oxidant in said leaching solution is between about 50 ppm and about 200 ppm on a free oxygen basis.

Claim 24

In the solution mining of substances from a subterranean formation using an alkaline carbonate leaching solution wherein the leaching solution is introduced into an injection well for percolation through the formation and the solution containing dissolved substance is recovered from a production well spaced from said injection well, a method for increasing the injectivity of said injection well comprising injecting an aqueous solution of an oxidizing agent into the injection well and simultaneously introducing gaseous carbon dioxide into the injection well.

Claim 25

In the solution mining of substances from a subterranean formation using an alkaline carbonate leaching solution wherein the leaching solution is introduced into an injection well for percolation through the formation and the solution containing dissolved substance is recovered from a production well spaced from said injection well, a method for increasing the injectivity of said injection well comprising injecting an aqueous solution of an oxidizing agent into the injection well and simultaneously introducing gaseous carbon dioxide into the injection well.

Claim 26

The method of claim 21 wherein the oxidizing agent is hydrogen peroxide.

Claim 27

The method of claim 22 wherein the concentration of said hydrogen peroxide in said aqueous solution is between about 50 ppm and about 200 ppm on a free oxygen basis.

Claim 28

The method of claim 21 wherein at least a portion of said gaseous carbon dioxide is solubilized into said aqueous solution to form a dilute carbonic acid solution in said injection well, said portion being sufficient to provide a bicarbonate ion concentration in said aqueous solution between about 380 ppm and about 1000 ppm.

Claim 29

The process of claim 14 wherein said oxidizing agent is hydrogen peroxide.