Multi-well solution mining exploitation of an evaporite mineral stratum

Patent metadata

Field	Value
Publication number	US-2018156020-A1
Application number	US-201815880581-A
Country	US
Kind code	A1
Filing date	Jan 26, 2018
Priority date	Mar 14, 2014
Publication date	Jun 7, 2018
Grant date	—

Abstract

A method for in situ solution mining of a mineral from an underground evaporite stratum using a set of wells in fluid communication with at least one mineral cavity with some wells operated in solvent injection mode and other wells operated in brine production mode and optionally with some inactive wells, comprising switching the operation mode of one or more wells. The evaporite mineral preferably comprises trona. The at least one cavity may be formed by directionally drilled uncased boreholes or by lithological displacement of the evaporite stratum at a weak interface with an underlying insoluble stratum by application of a lifting hydraulic pressure to create an interfacial gap. The extracted brine can be processed to make valuable products such as soda ash and/or any derivatives thereof. This method can provide more uniform dissolution of mineral in the cavity, minimize flow channeling, minimize sodium bicarbonate blinding for solution mining of incongruent trona ore, and/or may avoid uneven deposit of insolubles.

First claim

What we claimed is:

1 . In an underground formation comprising an evaporite mineral stratum comprising trona, nahcolite, wegscheiderite, or combinations thereof, a method for solution mining an evaporite mineral from at least one cavity having a mineral free face, said method comprising:
a) providing a set of wells in fluid communication with the at least one cavity, said set comprising a first subset of wells being operated in injection mode and a second subset of separate wells operated in production mode; b) injecting a solvent into the at least one cavity through the first subset operated in injection mode for the solvent to contact the mineral free face as the solvent flows through the at least one cavity and to dissolve in situ at least a portion of the mineral from the free face into the solvent to form a brine; c) extracting at least a portion of said brine to the ground surface through the second subset of wells operated in production mode; d) switching the operation mode of at least one well from the set after a period of time based in response to measurement of at least one parameter selected from the group consisting of: brine temperature, brine pH, brine outflow rate from each well operated in production mode, insolubles content, brine concentration of mineral ore, content in solvent-soluble impurities, and any combinations thereof; and (e) repeating the steps (a) to (d).

2 . The method according to claim 1 , wherein at step (d) the at least one parameter is selected from the group consisting of: brine sodium bicarbonate content exceeding a maximum target level; a brine Total Alkalinity content below a minimum target level; a brine content in sodium chloride, in sodium sulfate, in organics, exceeding a maximum threshold level; a brine outflow rate below a minimum target level; and any combinations thereof.

3 . The method according to claim 1 , wherein the set of wells comprises a number ‘n’ of wells with n equal to or greater than 4, and wherein a number of wells which is less than ‘n’ are arranged in at least one pattern centered around at least one center well.

4 . The method according to claim 3 , wherein the at least one pattern is in the shape of at least one polygon with from 3 to up to 16 sides, a honeycomb shape, or at least one ovoid shape.

5 . The method according to claim 3 , wherein the wells in the set are paired, and wherein cross-over valves are provided and controlled so that the paired wells serve alternatively as injection and production wells.

6 . The method according to claim 1 , wherein the set of wells comprises from 4 to 100 wells.

7 . The method according to claim 1 , wherein steps (b) and (c) are facilitated by a pump, and wherein, when one of the wells switches operation mode in step (d), the solvent injection and brine production for this well are carried out by the same pump.

8 . The method according to claim 1 , wherein step (d) comprises switching the operation mode of at least one well from the first subset and also switching the operation mode of at least one well from the second subset after the suitable period of time.

9 . The method according to claim 1 , wherein the method further comprises:
carrying out step (f): switching at least one well from the first or second subset from an injection or production mode to an inactive mode; or carrying out step (f′): switching at least one well from the set from an inactive mode to an injection or production mode; or carrying out step (f) and (f′) simultaneously on at least two different wells from the set.

10 . The method according to claim 1 , wherein the at least one cavity is initially formed by a lithological displacement of the mineral stratum, said lithological displacement being performed when said mineral stratum is lying immediately above a water-insoluble stratum of a different composition with a weak parting interface being defined between the two strata and above which is defined an overburden up to the ground surface, said lithological displacement comprising injecting a fluid at the parting interface to lift the evaporite stratum at a lifting hydraulic pressure greater than the overburden pressure, thereby forming an interface gap which is a nascent mineral cavity at the interface and creating said mineral free-surface

11 . The method according to claim 1 , wherein the at least one cavity is initially formed by a lithological displacement of the mineral stratum, and wherein forming the at least one cavity by lithological displacement of the mineral stratum comprises applying a lifting hydraulic pressure characterized by a fracture gradient between 0.9 psi/ft (20.4 kPa/m) and 1.5 psi/ft (34 kPa/m).

12 . The method according to claim 1 , wherein the at least one cavity is initially formed from at least one uncased section of a borehole directionally drilled through the mineral stratum.

13 . The method according to claim 1 , wherein the injected solvent in step (b) comprises an unsaturated aqueous solution comprising sodium carbonate, sodium bicarbonate, sodium hydroxide, calcium hydroxide, or combinations thereof.

14 . The method according to claim 1 , wherein the set of wells comprises outermost wells surrounding innermost wells, and wherein in that switching the operation mode in step (d) for at least some of these outermost wells is more frequently than for the innermost wells.

15 . The method according to claim 1 , wherein the operation mode switching step (d) is performed on peripheral wells of the set to impart a rotating motion of solvent around a centered well of the set.

16 . The method according to claim 1 , wherein the at least one cavity is initially formed by one or more borehole horizontal sections drilled through the mineral stratum.

17 . The method according to claim 1 , wherein the injected solvent in step (b) comprises an aqueous alkaline solution.

18 . The method according to claim 1 , wherein the suitable period of time for switching operation mode in step (d) is from 1 hour to 1 week.

19 . A manufacturing process for making one or more sodium-based products from an evaporite mineral stratum comprising a water-soluble mineral ore selected from the group consisting of trona, nahcolite, wegscheiderite, and combinations thereof, the process comprising:
carrying out the method according to claim 1 to dissolve the water-soluble mineral ore from said cavity in said evaporite mineral stratum to obtain said brine comprising sodium carbonate and/or sodium bicarbonate, and passing at least a portion of said brine through one or more units selected from the group consisting of a crystallizer, a reactor, and an electrodialysis unit, to form at least one sodium-based product, the at least one sodium-based product being selected from the group consisting of soda ash, sodium bicarbonate, sodium hydroxide, sodium sulfite, sodium sesquicarbonate, any sodium carbonate hydrates, and any combination thereof.

Assignees

• Solvay

Inventors

• Hughes Ronald O
• Paperini Matteo
• Cuche Herve
• Vendetti Joseph A
• Refsdal Larry C
• Detournay Jean-Paul
• Hansen David M
• Brichacek Todd
• Patterson Justin T
• Kolesar John
• Schmidt Ryan
• Ortego Beatrice C

Classifications

• C22B26/10

  Obtaining alkali metals · CPC title

• C22B3/46

  by substitution, e.g. by cementation · CPC title

• E21B43/28 Primary

  Dissolving minerals other than hydrocarbons, e.g. by an alkaline or acid leaching agent (E21B43/241 takes precedence) · CPC title

• E21B43/305

  comprising at least one inclined or horizontal well · CPC title

• E21B43/283

  in association with a fracturing process · CPC title