Recovery from a hydrocarbon reservoir

Patent metadata

Field	Value
Publication number	US-9534483-B2
Application number	US-201414316134-A
Country	US
Kind code	B2
Filing date	Jun 26, 2014
Priority date	Sep 9, 2013
Publication date	Jan 3, 2017
Grant date	Jan 3, 2017

Abstract

Methods and apparatus for recovering heavy oil from subterranean reservoirs. A steam-utilizing heavy oil recovery process may be used to recover the heavy oil while employing a steam-solvent mixture. The solvent may be a tailored hydrocarbon solvent obtained from a precursor mixture of hydrocarbon compounds from which light end hydrocarbon compounds have been removed.

First claim

What is claimed is:

1. A method of recovering heavy oil from a subterranean reservoir, the method comprising:
carrying out a steam-utilizing heavy oil recovery process to recover heavy oil from the subterranean reservoir while employing a steam/solvent mixture for said steam-utilizing heavy oil recovery process instead of steam alone,
wherein solvent used in said steam/solvent mixture is a tailored solvent obtained from a precursor mixture of hydrocarbon compounds by removing light end hydrocarbon compounds from said precursor mixture.

2. The method of claim 1 , wherein said solvent is substantially free of hydrocarbon compounds having one of (i) three carbon atoms and fewer, (ii) four carbon atoms and fewer, (iii) five carbon atoms and fewer and (iv) six carbon atoms and fewer.

3. The method of claim 1 , wherein said solvent contains amounts of hydrocarbon compounds having one of (i) seven to thirteen carbon atoms, (ii) seven to twelve carbon atoms and (iii) fourteen to thirty or more carbon atoms.

4. The method of claim 1 , wherein a combined mole fraction of one of (i) said at least some compounds having fourteen to thirty carbon or more atoms in said solvent is less than a combined mole fraction of all other hydrocarbon atoms present in said solvent, (ii) said at least some compounds having fourteen to thirty carbon or more atoms in said solvent is less than half a combined mole fraction of all other hydrocarbon atoms present in said solvent and (iii) said at least some compounds having fourteen to thirty carbon or more atoms in said solvent is less than a quarter of a combined mole fraction of all other hydrocarbon atoms present in said solvent and (iv) said at least some compounds having fourteen to thirty carbon or more atoms in said solvent is less than one tenth of a combined mole fraction of all other hydrocarbon atoms present in said solvent.

5. The method claim 1 , wherein said steam-utilizing heavy oil recovery process is operated at a reservoir operating pressures in a range of 0.1 to 15 MPa.

6. The method of claim 1 , wherein one of
(i) said steam-utilizing heavy oil recovery process is operated at a reservoir operating pressures in a range of 100-500 kPa, and wherein said tailored solvent is substantially free of hydrocarbon compounds having six carbon atoms and fewer,
(ii) said steam-utilizing heavy oil recovery process is operated at a reservoir operating pressures in a range of 500-1000 kPa, and wherein said tailored solvent is substantially free of hydrocarbon compounds having five carbon atoms and fewer,
(iii) said steam-utilizing heavy oil recovery process is operated at a reservoir operating pressures in a range of 1000-2000 kPa, and wherein said tailored solvent is substantially free of hydrocarbon compounds having four carbon atoms and fewer and
(iv) said steam-utilizing heavy oil recovery process is operated at a reservoir operating pressures higher than 2000 kPa, and wherein said tailored solvent is substantially free of hydrocarbon compounds having three carbon atoms and fewer.

7. The method of claim 1 , wherein said precursor mixture prior to removal of said light end hydrocarbon compounds is obtained by distillation of one of petroleum products and natural gas products.

8. The method of claim 1 , wherein said precursor mixture prior to removal of said light end hydrocarbon compounds comprises a hydrocarbon mixture recovered from said subterranean reservoir into which steam containing a tailored solvent was previously introduced.

9. The method of claim 1 , further comprising removing said light end hydrocarbon compounds from said precursor mixture to produce said tailored solvent.

10. The method of claim 9 , wherein removing said light end hydrocarbon compounds is carried out one of (i) in a vicinity of an injection well used for said steam utilizing heavy oil recovery process and (ii) remotely from an injection well used for said steam utilizing heavy oil recovery process.

11. The method of claim 9 , wherein removing said light end compounds comprises continuously removing said light end compounds while operating said steam utilizing heavy oil recovery process.

12. The method of claim 1 , wherein said steam-utilizing heavy oil recovery process is a process selected from the group consisting of solvent assisted-steam assisted gravity drainage, cyclic steam stimulation and steam flooding.

13. A method of recovering heavy oil from a subterranean reservoir by a solvent assisted, steam assisted gravity drainage process, comprising:
a) establishing fluid communication in a heavy oil-bearing formation between an injection well and a production well;
b) vaporizing water and a tailored hydrocarbon solvent to produce a vaporized mixture;
c) injecting said vaporized mixture into the subterranean reservoir via the injection well to permit the vaporized mixture to condense within the subterranean reservoir and to release latent heat of condensation to the subterranean reservoir; and
d) extracting heavy oil from the production well; wherein said tailored hydrocarbon solvent is a mixture of hydrocarbon compounds obtained from a precursor mixture of hydrocarbon compounds by removing light end hydrocarbon compounds from said precursor mixture.

Assignees

• Khaledi Rahman
• Boone Thomas J
• Exxonmobil Upstream Res Co

Inventors

• Khaledi Rahman
• Boone Thomas J

Classifications

• E21B43/24 Primary

  using heat, e.g. steam injection · CPC title

• E21B43/40

  Separation associated with re-injection of separated materials {(E21B43/385 takes precedence)} · CPC title

• E21B43/2408 Primary

  SAGD in combination with other methods · CPC title

• E21B43/166

  Injecting a gaseous medium; Injecting a gaseous medium and a liquid medium (CO2 injection E21B43/164; steam injection E21B43/24) · CPC title

• C09K8/592

  Compositions used in combination with generated heat, e.g. by steam injection · CPC title