Densifying carbon dioxide with a dispersion of carbon dioxide-philic water capsules

Patent metadata

Field	Value
Publication number	US-9546316-B2
Application number	US-201314074901-A
Country	US
Kind code	B2
Filing date	Nov 8, 2013
Priority date	Nov 12, 2012
Publication date	Jan 17, 2017
Grant date	Jan 17, 2017

Abstract

This invention generally relates to the field of oil recovery from reservoirs. More specifically, it relates to the recovery of oil from sandstone and carbonate reservoirs using a process for preparing a dispersion of capsules for use downhole including the steps of providing capsules containing a dense liquid, each capsule having a capsule wall defining an inner area, the capsule wall having an outer side. The capsules are functionalized by adding a carbon dioxide-philic compound to the outer side of the capsule wall. A dispersion is then prepared by adding the functionalized capsules to supercritical carbon dioxide such that a stable dispersion of capsules in supercritical carbon dioxide is achieved.

First claim

The invention claimed is:

1. A process for enhancing oil recovery comprising the steps of:
providing co-polymerized capsules containing a first liquid, the first liquid having a density greater than the density of supercritical carbon dioxide, each capsule having a capsule wall defining an inner area, the capsule wall having an outer side, the capsules prepared by a process comprising the steps of:
providing a second liquid, the second liquid operable to form a liquid phase when combined with the first liquid;
adding a first monomer to the first liquid to create a first monomer-liquid composition;
adding a second monomer to the second liquid to create a second monomer-liquid composition;
adding the first monomer-liquid composition to the second monomer-liquid composition;
agitating the first monomer-liquid composition and the second monomer-liquid composition to create a dispersion of first monomer-liquid composition in the second monomer-liquid composition; and
allowing the first and second monomers to diffuse and to co-polymerize at a liquid-liquid interface at a pre-determined time such that co-polymerized capsules are formed encapsulating the first liquid;

after preparing the co-polymerized capsules, functionalizing the capsules by adding a carbon dioxide-philic compound to the outer side of the capsule wall to create functionalized capsules;
preparing a capsule dispersion by adding the functionalized capsules to supercritical carbon dioxide such that a stable dispersion of capsules in supercritical carbon dioxide is achieved with the stable dispersion having a density greater than supercritical carbon dioxide; and
injecting the stable dispersion of capsules in supercritical carbon dioxide into a reservoir.

2. The process according to claim 1 , wherein said first liquid is non-supercritical at downhole operating pressure and temperature.

3. A process according to claim 1 , wherein the first liquid has a density of at least about 0.5 g/cc.

4. A process according to claim 1 , wherein the first monomer comprises triethylene tetramine.

5. A process according to claim 1 , wherein the second monomer comprises polymeric diphenylmethane diisocyanate.

6. A process according to claim 1 , wherein the carbon dioxide-philic compound comprises fluorinated carbon dioxide-soluble surfactant or oxygenated hydrocarbon carbon dioxide-philic molecules.

7. The process of claim 1 further comprising injecting water into the reservoir.

8. The process of claim 1 further comprising injecting a second amount of stable dispersion of capsules in supercritical carbon dioxide into the reservoir.

9. The process of claim 8 further comprising injecting a third amount of stable dispersion of capsules in supercritical carbon dioxide into the reservoir.

10. The process of claim 1 wherein the first liquid further comprises a heavy liquid filler.

11. The process according to claim 1 , wherein the co-polymerized capsules include nano-scale capsules between about 0.1 nanometer to about 1,000 nanometers.

12. The process according to claim 1 , wherein the co-polymerized capsules include nano-scale capsules between about 10 nanometers to about 1,000 nanometers.

13. The process according to claim 1 , wherein the co-polymerized capsules include nano-scale capsules between about 50 nanometers to about 250 nanometers.

14. The process according to claim 1 , wherein the co-polymerized capsules include micro-scale capsules between about 0.01 micrometer to about 1,000 micrometers.

15. The process according to claim 1 , wherein the co-polymerized capsules include micro-scale capsules between about 5 micrometers to about 500 micrometers.

16. The process according to claim 1 , wherein the co-polymerized capsules include micro-scale capsules between about 50 micrometers to about 250 micrometers.

Assignees

• Saudi Arabian Oil Co

Inventors

• Al-Otaibi Fawaz
• Chang Yun
• Kokal Sunil
• Schmidt Howard

Classifications

• B01J13/16

  Interfacial polymerisation · CPC title

• B01J13/20

  After-treatment of capsule walls, e.g. hardening · CPC title

• C09K8/588

  characterised by the use of specific polymers {(polymeric surfactants C09K8/584)} · CPC title

• E21B43/164 Primary

  Injecting CO2 or carbonated water (in combination with organic material C09K8/594) · CPC title

• B01J13/18

  In situ polymerisation with all reactants being present in the same phase · CPC title