초록 ▼

Injection fluids formed of reverse emulsions and related methods of forming and using reverse emulsions for cavity control in solution mining. The reverse emulsion can reduce the volume of oil required to create an oil pad at the roof of a solution mining cavern in order to prevent vertical leaching

Injection fluids formed of reverse emulsions and related methods of forming and using reverse emulsions for cavity control in solution mining. The reverse emulsion can reduce the volume of oil required to create an oil pad at the roof of a solution mining cavern in order to prevent vertical leaching and cavern collapse. The reverse emulsion can be formed from an emulsifier, a brine solution and oil. The emulsifier concentration can range from about 1% to about 5% by weight of the reverse emulsion. The emulsifier and the oil can be combined to form an oil/emulsifier mixture, wherein the oil/emulsifier mixture is combined with the brine solution to form the reverse emulsion. The oil/emulsifier mixture can be from about 1% to about 5% by weight of the reverse emulsion.

대표청구항 ▼

1. A method of solution mining, comprising: providing a reverse emulsion comprising an emulsifier, a brine solution, and a heavy hydrocarbon source; andinjecting the reverse emulsion into a solution mining cavern such that the reverse emulsion forms an oil pad that occupies a cavern roof. 2. The met

1. A method of solution mining, comprising: providing a reverse emulsion comprising an emulsifier, a brine solution, and a heavy hydrocarbon source; andinjecting the reverse emulsion into a solution mining cavern such that the reverse emulsion forms an oil pad that occupies a cavern roof. 2. The method of claim 1, wherein providing the reverse emulsion comprises: adding the emulsifier to the brine solution and the hydrocarbon source such that an emulsifier concentration in the reverse emulsion is from about 1% to about 5% by weight of the reverse emulsion. 3. The method of claim 1, wherein the emulsifier comprises polyisobutylene succinct anhydride (PIBSA). 4. The method of claim 1, wherein providing the reverse emulsion comprises: adding the brine solution such that a brine solution concentration in the reverse emulsion is from about 30% to about 80% by weight of the reverse emulsion. 5. The method of claim 1, wherein the brine solution comprises a solution of potassium chloride, sodium chloride, and/or calcium chloride, and water, wherein the potassium chloride, sodium chloride, and/or calcium chloride are present in an amount from about 25% to about 100% of saturation. 6. The method of claim 1, wherein the reverse emulsion is injected at a temperature from about 120° F. to about 200° F. 7. The method of claim 1, wherein providing the reverse emulsion, comprises: combining the emulsifier and the hydrocarbon source to form a hydrocarbon source/emulsifier mixture; andcombining the hydrocarbon source/emulsifier mixture with the brine solution to form the reverse emulsion. 8. The method of claim 7, wherein the hydrocarbon source/emulsifier mixture comprises from about 1% to about 5% by weight of the reverse emulsion. 9. The method of claim 1, wherein the hydrocarbon source comprises unprocessed or unused and/or reprocessed crude oil or fractions thereof including, but not limited to, heavy crude oil fractions such as heavy distillates, light crude oil, or combinations thereof. 10. The method of claim 1, wherein small particles or droplets of brine have a particle size of from about 0.5 to about 2 μm, and the reverse emulsion has a shelf stability of at least 5 years.