Process for carbon capture and sequestration in a subsurface formation by injection of liquefied biomass
US-2024167365-A1 · May 23, 2024 · US
US10047275B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10047275-B2 |
| Application number | US-201514958660-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 3, 2015 |
| Priority date | Dec 4, 2014 |
| Publication date | Aug 14, 2018 |
| Grant date | Aug 14, 2018 |
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In one aspect, a method of recovering hydrocarbons from a subterranean zone includes flowing carbon dioxide in a first state into the subterranean zone including hydrocarbons, wherein a density of the carbon dioxide in the first state is greater than a density of carbon dioxide in a gaseous state, and recovering at least a portion of the hydrocarbons in the subterranean zone in response to flowing carbon dioxide in the first state into the subterranean zone.
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What is claimed is: 1. A secondary or tertiary hydrocarbon recovery method comprising: flowing a complex emulsion into the subterranean zone, the complex emulsion comprising an internal fluid-in-gas emulsion configured to increase a density and a viscosity of a gas in the internal fluid-in-gas emulsion emulsifying a fluid in the internal fluid-in-gas emulsion, the complex emulsion comprising an external fluid emulsifying the internal fluid-in-gas emulsion, the external fluid configured to carry corrosion inhibitors into the subterranean zone, wherein the complex emulsion further comprises a first plurality of hydrophobic silica particles encapsulating an outer surface of droplets of the fluid in the internal fluid-in-gas emulsion, wherein a concentration of the first plurality of hydrophobic silica particles is between about 0.1% and 0.5% by weight; and recovering at least a portion of hydrocarbons in the subterranean zone using the complex emulsion flowed into the subterranean zone. 2. The method of claim 1 , wherein the fluid in the internal fluid-in-gas emulsion comprises water. 3. The method of claim 2 , wherein the gas in the internal fluid-in-gas emulsion comprises carbon dioxide (CO 2 ). 4. The method of claim 1 , wherein the complex emulsion comprises a second plurality of particles encapsulating an outer surface of droplets of the external fluid. 5. The method of claim 4 , wherein the second plurality of particles comprise hydrophilic particles. 6. The method of claim 4 , wherein the second plurality of particles comprise hydrophilic silica. 7. The method of claim 4 , wherein a concentration of the second plurality of particles is between about 0.1% and 0.5% by weight. 8. The method of claim 1 , wherein the complex emulsion further comprises corrosion inhibitors added to the external fluid. 9. The method of claim 1 , wherein the complex emulsion is flowed into the subterranean zone in a secondary, tertiary or enhanced hydrocarbon recovery operation after a primary hydrocarbon recovery operation. 10. A secondary or tertiary hydrocarbon recovery method comprising: manufacturing a complex emulsion comprising an internal fluid-in-gas emulsion configured to increase a density and a viscosity of a gas in the internal fluid-in-gas emulsion emulsifying a fluid in the internal fluid-in-gas emulsion, the complex emulsion comprising an external fluid emulsifying the internal fluid-in-gas emulsion, the external fluid configured to carry corrosion inhibitors into the subterranean zone, wherein the complex emulsion further comprises a first plurality of hydrophobic silica particles encapsulating an outer surface of droplets of the fluid in the internal fluid-in-gas emulsion, wherein a concentration of the first plurality of hydrophobic silica particles is between about 0.1% and 0.5% by weight; flowing the complex emulsion into the subterranean zone; and recovering at least a portion of hydrocarbons in the subterranean zone using the complex emulsion flowed into the subterranean zone. 11. The method of claim 10 , wherein manufacturing the complex emulsion comprises mixing the gas in the internal fluid-in-gas emulsion, the fluid in the internal fluid-in-gas emulsion and the external fluid in a tank under controlled temperature and pressure. 12. The method of claim 11 , wherein the complex emulsion further comprises a second plurality of particles encapsulating an outer surface of droplets of the external fluid, wherein manufacturing the complex emulsion comprises mixing the first plurality of particles and the second plurality of particles with the gas in the internal fluid-in-gas emulsion, the fluid in the internal fluid-in-gas emulsion and the external fluid in the tank. 13. The method of claim 12 , wherein the first plurality of particles and the second plurality of particles are added to the tank after mixing the gas in the internal fluid-in-gas emulsion, the fluid in the internal fluid-in-gas emulsion and the external fluid. 14. The method of claim 11 , wherein manufacturing the complex emulsion comprises first manufacturing the internal fluid-in-gas emulsion and then manufacturing the complex emulsion as an emulsion of the internal fluid-in-gas emulsion in the external fluid. 15. A complex emulsion for secondary or tertiary hydrocarbon recovery from a subterranean zone, the complex emulsion comprising: an internal fluid-in-gas emulsion configured to increase a density and a viscosity of a gas in the internal fluid-in-gas emulsion emulsifying a fluid in the internal fluid-in-gas emulsion; and an external fluid emulsifying the internal fluid-in-gas emulsion, the external fluid configured to carry corrosion inhibitors into the subterranean zone. 16. The complex emulsion of claim 15 , further comprising: a first plurality of hydrophobic nanoparticles encapsulating an outer surface of droplets of the fluid in the internal fluid-in-gas emulsion; and a second plurality of hydrophilic particles encapsulating an outer surface of droplets of the external fluid.
Injecting CO2 or carbonated water (in combination with organic material C09K8/594) · CPC title
Nanoparticle-containing well treatment fluids · CPC title
Compositions used in combination with injected gas {, e.g. CO2 orcarbonated gas}(C09K8/592 takes precedence) · CPC title
Injecting a gaseous medium; Injecting a gaseous medium and a liquid medium (CO2 injection E21B43/164; steam injection E21B43/24) · CPC title
Anticorrosion additives · CPC title
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