Hydrophobic Paramagnetic Nanoparticles as Intelligent Crude Oil Tracers
US-2015376493-A1 · Dec 31, 2015 · US
US9951263B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9951263-B2 |
| Application number | US-201013503033-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 15, 2010 |
| Priority date | Oct 20, 2009 |
| Publication date | Apr 24, 2018 |
| Grant date | Apr 24, 2018 |
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A process for the recovery of heavy oil from an underground reservoir, comprising: injecting an oil-in-water nanoemulsion into one or more injection wells; recovering said heavy oil from one or more production wells. Said process is particularly advantageous for enhancing the recovery of heavy oils from underground reservoirs within the range of technologies for tertiary recovery, usually known as “EOR” (Enhanced Oil Recovery”).
Opening claim text (preview).
The invention claimed is: 1. A process for the recovery of heavy oil from an underground reservoir, comprising: injecting an oil-in-water nanoemulsion into one or more injection wells; and recovering the heavy oil from one or more production wells, wherein the oil-in-water nanoemulsion contacts the heavy oil in the underground reservoir and reduces interfacial tension between the heavy oil in the underground reservoir and the water in the oil-in-water nanoemulsion and reduces the viscosity of the heavy oil in the underground reservoir, and the oil in the oil-in-water nanoemulsion is selected from the group consisting of aromatic hydrocarbons. 2. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the one or more injection wells and the one or more production wells are different. 3. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the one or more injection wells and the one or more production wells are the same. 4. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the heavy oil has a dynamic viscosity, measured at the reservoir temperature higher than or equal to 20 cP. 5. The process for the recovery of heavy oil from an underground reservoir according to claim 4 , wherein the heavy oil has a dynamic viscosity, measured at the reservoir temperature ranging from 22 cP to 150 cP. 6. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein in the oil-in-water nanoemulsion, the dispersed oil phase is distributed in the dispersing water phase in the form of droplets having a diameter ranging from 10 nm to 500 nm. 7. The process for the recovery of heavy oil from an underground reservoir according to claim 6 , wherein in the oil-in-water nanoemulsion, the dispersed oil phase is distributed in the dispersing water phase in the form of droplets having a diameter ranging from 15 nm to 200 nm. 8. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the oil-in-water nanoemulsion is prepared according to a process comprising: preparing a homogeneous water/oil mixture ( 1 ) having an interface tension lower than or equal to 1 mN/m, comprising water in an amount ranging from 65% by weight to 99.9% by weight, with respect to the total weight of the mixture ( 1 ), at least two surfactants having a different HLB, selected from non-ionic, anionic, polymeric surfactants, wherein the mixture ( 1 ) is homogeneous; diluting the mixture ( 1 ) in a dispersing phase comprising water and at least one surfactant selected from the group consisting of non-ionic, anionic, polymeric surfactants, the amount of the dispersing phase and of the surfactant being such as to obtain an oil-in-water nanoemulsion having a HLB higher than that of the mixture ( 1 ). 9. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the oil-in-water nanoemulsion has a HLB value higher than or equal to 9. 10. The process for the recovery of heavy oil from an underground reservoir according to claim 9 , wherein the oil-in-water nanoemulsion has a HLB value ranging from 10 to 16. 11. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein in the oil-in-water nanoemulsion, the dispersed oil phase is distributed in the dispersing water phase in the form of droplets having a specific area (area/volume) ranging from 6,000 m 2 /l to 300,000 m 2 /l. 12. The process for the recovery of heavy oil from an underground reservoir according to claim 11 , wherein in the oil-in-water nanoemulsion, the dispersed oil phase is distributed in the dispersing water phase in the form of droplets having a specific area (area/volume) ranging from 15,000 m 2 /l to 200,000 m 2 /l. 13. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the oil-in-water nanoemulsion comprises an amount of surfactants ranging from 0.1% by weight to 20% by weight with respect to the total weight of the oil-in-water nanoemulsion. 14. The process for the recovery of heavy oil from an underground reservoir according to claim 13 , wherein the oil-in-water nanoemulsion comprises an amount of surfactants ranging from 0.25% by weight to 12% by weight with respect to the total weight of the oil-in-water nanoemulsion. 15. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the oil-in-water nanoemulsion comprises an amount of oil ranging from 0.5% by weight to 10% by weight with respect to the total weight of the oil-in-water nanoemulsion. 16. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the oil-in-water nanoemulsion comprises an amount of oil ranging from 1% by weight to 8% by weight with respect to the total weight of the oil-in-water nanoemulsion. 17. The process for the recovery of heavy oil from an underground reservoir according to claim 13 , wherein the surfactants are non-ionic surfactants selected from the group consisting of alkyl polyglucosides; esters of fatty acids of sorbitan; polymeric surfactants such as grafted acrylic copolymers having a backbone of polymethylmethacrylate-methacrylic acid and side chains of polyethylene glycol, and mixtures thereof. 18. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the oil of the nanoemulsion is selected from the group consisting of xylene, mixtures of xylene isomers, toluene, benzene and mixtures thereof. 19. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the water of the nanoemulsion is selected from demineralized water, salt water, water with additives, or mixtures thereof. 20. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the water of the nanoemulsion is water present in the underground reservoir. 21. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein at least one base is added to the oil-in-water nanoemulsion in an amount ranging from 0.1% by weight to 10% by weight with respect to the total weight of the oil-in-water nanoemulsion. 22. The process for the recovery of heavy oil from an underground reservoir according to claim 21 , wherein at least one base is added to the oil-in-water nanoemulsion in an amount ranging from 0.2% by weight to 5% by weight with respect to the total weight of the oil-in-water nanoemulsion. 23. The process for the recovery of heavy oil from an underground reservoir according to claim 21 , wherein the base is selected from sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, or mixtures thereof. 24. The process for the recovery of heavy oil from an underground reservoir according to claim 1 , wherein the oil-in-water nanoemulsion is injected into one or more injection wells for a time ranging from 80 days to 200 days. 25. The process for the recovery of heavy oil from an underground reservoir according to claim 24 , wherein the oil-in-water nanoemulsion is injected into one or more injection wells for a time ranging from 90 days to 180 days. 26. The process for the recovery of heavy o
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