Using nanoparticles for water flow control in subterranean formations
View Patent ↗Non-aqueous carrier fluids containing nano-sized particles in high concentration are effective for zone isolation and flow control in water shutoff applications for subterranean formations. The nanoparticles interact with water and solidify it to inhibit its flow, but do not have the same effect on hydrocarbons and thus selectively assist the production of hydrocarbons while suppressing water. Suitable nanoparticles include alkaline earth metal oxides, alkaline earth metal hydroxides, alkali metal oxides, alkali metal hydroxides, transition metal oxides, transition metal hydroxides, post-transition metal oxides, post-transition metal hydroxides, piezoelectric crystals, and/or pyroelectric crystals.
1. A method for inhibiting or preventing a flow of water in a subterranean formation comprising:
injecting into the subterranean formation where water is present, a treating slurry comprising:
a non-aqueous carrier fluid and particles,
where the non-aqueous fluid is selected from the group consisting of oils, glycols and mixtures thereof, and
where the particles are added in an amount effective to inhibit the flow of water when the treating slurry contacts water and consist of nanoparticles having a mean particle size between about 4 to 500 nm and are selected from the group consisting of piezoelectric crystals and pyroelectric crystals in turn selected from the group consisting of berlinite (AlPO 4 ), lithium tantalate (LiTaO 3 ), gallium orthophosphate (GaPO 4 ), BaTiO 3 , SrTiO 3 , PbZrTiO 3 , KNbO 3 , LiNbO 3 , LiTaO 3 , BiFeO 3 , sodium tungstate, Ba 2 NaNb 5 O 5 , Pb 2 KNb 5 O 15 , potassium sodium tartrate, tourmaline, topaz and mixtures thereof; and
contacting the water with the treating slurry to solidify the nanoparticles within the subterranean formation where the solidified nanoparticles inhibit or prevent the flow of water in the formation.
2. The method of claim 1 where the non-aqueous carrier fluid is selected from the group consisting of glycol ethers, polyols, propylene carbonate, carboxylate esters, terpene, vegetable oils, mineral oils, mineral spirits, diesel, biodiesel, condensate, aromatic hydrocarbons, ethylene glycol, propylene glycol, glycerol and mixtures thereof.
3. The method of claim 1 where the amount of nanoparticles in the treating slurry ranges from about 2 to about 50 weight percent based on the total treating slurry.
4. The method of claim 1 where the non-aqueous carrier fluid does not inhibit a flow of hydrocarbons it encounters.
5. The method of claim 1 further comprising subsequently injecting an acid into the subterranean formation to dissolve at least a portion of the nanoparticles and substantially restore water flow.
6. The method of claim 1 where the subterranean formation is beneath a seabed that is at least 500 meters deep and the water present in the subterranean formation is a shallow water flow.
7. The method of claim 1 further comprising subsequently injecting heat into the subterranean formation, where the solidified nanoparticles at least partially control where the heat is injected.
8. The method of claim 1 further comprising inhibiting water flow to improve sweep efficiency during secondary and/or tertiary recovery of hydrocarbons from the subterranean formation, where the injecting is performed in an injection well to inhibit or prevent a water flow from the injection well to at least one production well.
9. A method for inhibiting or preventing a flow of water in a subterranean formation comprising:
injecting into the subterranean formation where water is present, a treating slurry comprising:
a non-aqueous carrier fluid and particles,
where the non-aqueous fluid is selected from the group consisting of oils, glycols and mixtures thereof, and
where the particles are added in an amount of about 2 to about 50 weight percent based on the total treating slurry and consist of nanoparticles having a mean particle size between about 4 to 500 nm and are selected from the group consisting of piezoelectric crystals and pyroelectric crystals in turn selected from the group consisting of berlinite (AlPO 4 ), lithium tantalate (LiTaO 3 ), gallium orthophosphate (GaPO 4 ), BaTiO 3 , SrTiO 3 , PbZrTiO 3 , KNbO 3 , LiNbO 3 , LiTaO 3 , BiFeO 3 , sodium tungstate, Ba 2 NaNb 5 O 5 , Pb 2 KNb 5 O 15 , potassium sodium tartrate, tourmaline, topaz and mixtures thereof; and
contacting the water with the treating slurry to solidify the nanoparticles within the subterranean formation where the solidified nanoparticles inhibit or prevent the flow of water in the formation and where the nanoparticles in the non-aqueous carrier fluid do not inhibit the flow of hydrocarbons they encounter.
10. The method of claim 9 where the non-aqueous carrier fluid is selected from the group consisting of glycol ethers, polyols, propylene carbonate, carboxylate esters, terpene, vegetable oils, mineral oils, mineral spirits, diesel, biodiesel, condensate, aromatic hydrocarbons, ethylene glycol, propylene glycol, glycerol and mixtures thereof.
11. The method of claim 9 further comprising subsequently injecting an acid into the subterranean formation to dissolve at least a portion of the nanoparticles and substantially restore water flow.
12. The method of claim 9 where the subterranean formation is beneath a seabed that is at least 500 meters deep and the water present in the subterranean formation is a shallow water flow.
13. The method of claim 9 further comprising subsequently injecting heat into the subterranean formation, where the solidified nanoparticles at least partially control where the heat is injected.
14. The method of claim 9 further comprising inhibiting water flow to improve sweep efficiency during secondary and/or tertiary recovery of hydrocarbons from the subterranean formation, where the injecting is performed in an injection well to inhibit or prevent a water flow from the injection well to at least one production well.
15. A method for inhibiting or preventing a flow of water in a subterranean formation comprising:
injecting into the subterranean formation where the water is present, a treating slurry comprising:
a non-aqueous carrier fluid and particles,
where the non-aqueous fluid is selected from the group consisting of glycol ethers, polyols, propylene carbonate, carboxylate esters, terpene, vegetable oils, mineral oils, mineral spirits, diesel, biodiesel, condensate, aromatic hydrocarbons, ethylene glycol, propylene glycol, glycerol and mixtures thereof and
where the particles are added in an amount of about 10 to about 40 weight percent based on the total treating slurry and consist of nanoparticles having a mean particle size between about 4 to 500 nm and are selected from the group consisting of piezoelectric crystals and pyroelectric crystals in turn selected from the group consisting of berlinite (AlPO 4 ), lithium tantalate (LiTaO 3 ), gallium orthophosphate (GaPO 4 ), BaTiO 3 , SrTiO 3 , PbZrTiO 3 , KNbO 3 , LiNbO 3 , LiTaO 3 , BiFeO 3 , sodium tungstate, Ba 2 NaNb 5 O 5 , Pb 2 KNb 5 O 15 , potassium sodium tartrate, tourmaline, topaz and mixtures thereof; and
contacting the water with the treating slurry to solidify the nanoparticles within the subterranean formation where the solidified nanoparticles inhibit or prevent the flow of water in the formation and where the nanoparticles in the non-aqueous carrier fluid do not inhibit the flow of hydrocarbons they encounter.
16. The method of claim 15 further comprising subsequently injecting an acid into the subterranean formation to dissolve at least a portion of the nanoparticles and substantially restore the water flow.
17. The method of claim 15 where the subterranean formation is beneath a seabed that is at least 500 meters deep and the water present in the subterranean formation is a shallow water flow.
18. The method of claim 15 further comprising subsequently injecting heat into the subterranean formation, where the solidified nanoparticles at least partially control where the heat is injected.
19. The method of claim 15 further comprising inhibiting the water flow to improve sweep efficiency during secondary and/or tertiary recovery of hydrocarbons from the subterranean formation, where the injecting is performed in an injection well to inhibit or prevent a water flow from the injection well to at least one production well.