Oil recovery process

• US 4,333,529 A
• Filed: 08/29/1980
• Issued: 06/08/1982
• Est. Priority Date: 08/31/1979
• Status: Expired due to Term

• Current Assignee: Robert P. Mccorquodale
• Original Assignee: Wetcom Engineering Limited
• Inventors: McCorquodale, Robert P.
• Primary Examiner(s): Novosad, Stephen J.
• Assistant Examiner(s): Suchfield, George A.
• Application Number:
  US06/182,572
• Time in Patent Office: 648 Days
• Field of Search: 166/265, 166/266, 166/267, 166/272, 166/303, 210/758, 210/761
• US Class Current: 166/267
• CPC Class Codes: E21B 43/164 Injecting CO2 or carbonated water in combination with organic material C09K8/594
• CPC Class Codes: E21B 43/24 using heat, e.g. steam injection
• CPC Class Codes: E21B 43/40 Separation associated with re-injection of separated materials E21B43/385 takes precedence

Abstract

Oil recovery from formations is effected using a gas stream containing steam, carbon dioxide and nitrogen which is injected into the formation to form a water-oil mixture which is removed from the formation. The gas stream is formed by wet oxidation of a carbonaceous material which includes residual oil in the aqueous material remaining from oil separation.

Claims

1. A continuous process for the recovery of oil from an oil deposit, which comprises:

(a) continuously feeding an aqueous dispersion of carbonaceous material having a concentration of about 10 to about 20 wt.% COD to an enclosed reaction zone,

(b) continuously contacting said aqueous dispersion of carbonaceous material with an oxidizing gas in said enclosed reaction zone at a temperature of about 200°

to about 350°

, at a pressure of about 500 to about 3000 psi and for a time of about 5 to about 120 minutes to effect substantial wet oxidation combustion of said carbonaceous material to form a product gas stream having a pressure of about 500 to about 3000 psi and containing about 50 to about 95% by volume of steam, about 5 to about 50% by volume of carbon dioxide and 0 to about 35% by weight of nitrogen,

(c) continuously injecting said product gas stream into said oil deposit under sufficient pressure to cause said oil to be ejected from said deposit in aqueous admixture,

(d) continuously recovering oil from said ejected aqueous admixture to leave an aqueous medium containing residual quantities of said oil in a concentration of about 1000 to about 10,000 ppm COD,

(e) continuously adding to said aqueous medium sufficient quantity of a fossil fuel to provide an aqueous dispersion of carbonaceous material having a concentration of about 10 to about 20 wt.% COD, and

3. The process of claim 1 wherein said oil deposit is a conventional subterranean oil deposit in which the oil readily flows upon the application of pressure supplied at least in part by said product gas stream thereto.

4. The process of claim 1 wherein said oil deposit is a subterranean heavy crude oil and said product gas stream possesses sufficient enthalpy to decrease the viscosity of said heavy crude oil in said deposit sufficient to enable the same to flow under pressure supplied at least in part by said product gas stream.

5. The process of claim 1 wherein said oil deposit is a bituminous oil sand and said product gas stream possesses sufficient enthalpy to decrease the viscosity of said bituminous oil in said oil sand sufficient to enable the same to flow under pressure supplied at least in part by said product gas stream.

6. The process of claim 1 wherein said temperature is about 275°

to about 325°

C., said pressure is about 1500 to about 2500 psi and said time is about 20 to about 60 minutes.

7. The process of claim 1 wherein said fossil fuel-based carbonaceous material is selected from the group consisting of oil recovered from the formation, a by-product from upgrading of such oil, coke, coal, peat and lignite.

8. The process of claim 1 wherein said oxidizing gas is air, whereby said product gas stream contains steam, carbon dioxide and nitrogen.

2. (f) continuously forwarding said latter aqueous dispersion to said enclosed reaction zone as said continuously fed aqueous dispersion in step (a), whereby said residual quantities of said oil are consumed in forming said gas stream.