Method and foam composition for recovering hydrocarbons from a subterranean reservoir
US-2015175876-A1 · Jun 25, 2015 · US
US9518211B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9518211-B2 |
| Application number | US-201414760623-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 15, 2014 |
| Priority date | Jan 25, 2013 |
| Publication date | Dec 13, 2016 |
| Grant date | Dec 13, 2016 |
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The present invention relates to a process for recovering oil from a subterranean formation by injecting both solid particles and water into the formation. An oil-in-water emulsion that is stabilized by solid particles is formed in the pores of the formation. This emulsion is recovered from the subterranean formation.
Opening claim text (preview).
The invention claimed is: 1. A process for recovering oil from a subterranean oil-containing formation comprising at least the steps of: a) introducing solid particles and water into the subterranean oil-containing formation to obtain a solid particles-stabilized emulsion containing droplets, whereby water is the continuous phase and oil is the dispersed phase, and b) recovering said solid particles-stabilized emulsion from the subterranean oil-containing formation, wherein the solid particles comprise at least one layered double hydroxide of general formula (I) [M II (1-x) M III x (OH) 2 ] x+ [A n− ] x/n .y H 2 O (I), wherein M II denotes a divalent metal ion or 2Li, M III denotes a trivalent metal ion, A n− denotes an n-valent anion, n is 1 or 2, x is the mole fraction having a value ranging from 0.1 to 0.5 and y is a value ranging from 0 to 5.0; wherein the solid-particles stabilized emulsion has a viscosity at 20° C. in the range of 5 to 30 mPa·s at a temperature of 20° C. under shear rate of 10/s. 2. The process according to claim 1 , wherein the solid particles have an average particle size in the range of 30 nm to 10 μm. 3. The process according to claim 1 , wherein that the droplets have an average droplet size Dv 50 in the range of 1 to 40 μm. 4. The process according to claim 1 , wherein that the droplets have an average droplet size Dv 90 in the range of 10 to 30 μm. 5. The process according to claim 1 , wherein the subterranean oil-containing formation has pores and the solid particles-stabilized emulsion is obtained by transporting the solid particles and water through these pores. 6. The process according to claim 1 , wherein the solid particles are hydrophilic. 7. The process according to claim 1 , wherein the solid particles-stabilized emulsion comprises 10 to 90% by weight water, 10 to 90% by weight oil and 0.1 to 10% by weight of at least one layered double hydroxide of general formula (I), related to the overall weight of the emulsion. 8. The process according to claim 1 , wherein the oil is crude oil. 9. The process according to claim 1 , wherein the oil is crude oil having a viscosity in the range of 1 to 5000 mPa·s at a temperature of 20° C. 10. The process according to claim 1 , wherein the divalent metal ion is Ca, Mg, Fe, Ni, Zn, Co, Cu or Mn, the trivalent metal ion is Al, Fe, Cr or Mn, the n-valent anion is Cl − , Br − , NO 3 − , CO 3 2− , SO 4 2− or SeO 4 2− , x is the mole fraction having a value ranging from 0.1 to 0.5 and y is a value ranging from 0 to 5.0. 11. The process according to claim 1 , wherein the solid particles-stabilized emulsion has a conductivity in the range of 50 to 190 mS/cm. 12. The process according to claim 1 , wherein the aspect ratio of the solid particles is in the range of 1 to 30. 13. The process according to claim 1 , wherein upon introduction of the solid particles and water into the subterranean oil-containing formation, the solid particles and water transport into pores of the subterranean oil-containing formation to obtain the solid particles-stabilized emulsion, wherein: the solid particles-stabilized emulsion does not form a flow barrier for diverting flow of hydrocarbons in a subterranean formation; the solid particles-stabilized emulsion does not form effective horizontal barriers to vertical flow of gas or water to reduce coning of the gas or water to the oil producing zone of a well; and the solid particles-stabilized emulsion does not fill high permeability formation zones for profile modification applications to improve subsequent waterflood performance.
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