Method for recovering viscous asphaltic or bituminous petroleum

• US 3,938,590 A
• Filed: 06/26/1974
• Issued: 02/17/1976
• Est. Priority Date: 06/26/1974
• Status: Expired due to Term

• Current Assignee: Texaco Exploration Canada Limited (Chevron Corp.)
• Original Assignee: Texaco Exploration Canada Limited (Chevron Corp.)
• Inventors: Redford, David A., Mitchell, David L.
• Primary Examiner(s): Novosad, Stephen J.
• Application Number:
  US05/483,173
• Time in Patent Office: 601 Days
• Field of Search: 166/270, 166/271, 166/272, 166/261, 166/259, 166/300, 166/303
• US Class Current: 166/270.1
• CPC Class Codes: C09K 8/592 Compositions used in combination with generated heat, e.g. by steam injection
• CPC Class Codes: E21B 43/24 using heat, e.g. steam injection
• CPC Class Codes: E21B 43/2405 in association with fracturing or crevice forming processes E21B43/247 takes precedence

Abstract

Disclosed is a process for recovering petroleum from subterranean, viscous asphaltic or bituminous petroleum-containing formations, including subterranean tar sand deposits. A zone of gas permeability is established in the formation first, such as by fracturing or gas sweeping a section of the formation. Oxidizing gas such as oxygen, air, oxygen enriched air, ozone, or chlorine, or a mixture of steam and an oxidizing gas is introduced into the zone of increased gas permeability to expand the zone and further to cause a reaction to occur between the oxidizing gas and the oxygen-susceptible groups or labile groups associated witn the bituminous or asphaltic petroleum molecules forming acidic or aldehyde groups. Next, a gaseous or liquid alkalinity agent such as ammonia is introduced into the formation to react with the oxidatively pre-treated groups in the bituminous or asphaltic petroleum to form surface active agents or surfactants in situ. Finally, steam or a mixture of steam and an alkalinity agent such as ammonia or steam and air or a mixture of steam, oxidative gas and an excess of ammonia is introduced into the treated zone to recover petroleum. This process may be applied as a push-pull process or it may be applied in a multi well, throughput process. In a preferred embodiment, gaseous ammonia serves as an alkaline agent to neutralize the surface active agents formed in the formation, and also functions as a non-condensable gas to prevent loss of gas permeability as the viscous petroleum is heated in the final stages of the process.

Claims

1. A method of recovering viscous, asphaltic or bituminous petroleum from a permeable, subterranean, viscous asphaltic or bituminous petroleum-containing formation including a tar sand deposit, penetrated by at least one well in fluid communication with the formation comprising:

a. forming a zone of increased permeability in at least a portion of the formation,

b. introducing chlorine gas into said zone of increased permeability to oxidize labile groups on the bituminous petroleum, to form surface active agents in the formation,

c. introducing an alkalinity agent into said zone of increased permeability to neutralize oxidized groups generated by action of the chlorine gas,

d. introducing into the formation a recovery fluid selected from the group consisting of steam, a mixture of steam and an oxygen containing gas including air, a mixture of steam and ammonia, or a mixture of steam, ammonia and an oxygen containing gas, and

e. recovering formation petroleum from the formation.

2. A method as recited in claim 1 wherein the step of forming the zone of increased permeability comprises fracturing the formation, introducing a propping agent, then introducing a solvent to dissolve bituminous petroleum from the tar sand material around the fracture to convert the propped fracture zone into an enlarged zone of high permeability.

3. A method as recited in claim 1 wherein the step of forming said zone of high permeability comprises fracturing and introducing a propping material into the fractured zone followed by introducing a hot aqueous fluid selected from the group consisting of steam and hot water into the propped fracture zone to remove bituminous petroleum from the tar sand material adjacent to the propped fracture zone to convert the propped fracture zone into an enlarged zone of high permeability.

4. A method as recited in claim 3 wherein the hot aqueous fluid also contains an alkalinity agent.

5. A method as recited in claim 1 wherein steam is mixed with the chlorine gas.

6. A method as recited in claim 1 wherein the alkalinity agent is selected from the group consisting of aqueous solutions of hydroxides of ammonia, sodium and potassium, mixtures thereof, and ammonia gas.

7. A method as recited in claim 6 wherein the alkalinity agent is an aqueous solution of sodium hydroxide.

8. A method as recited in claim 6 wherein the alkalinity agent is an aqueous solution of ammonium hydroxide.

9. A method as recited in claim 6 wherein the alkalinity agent is an aqueous solution of potassium hydroxide.

10. A method as recited in claim 6 wherein the alkalinity agent is gaseous ammonia.

11. A method as recited in claim 1 wherein steam is introduced into the zone of increased permeability between the step of introducing chlorine gas in the step of introducing alkalinity agent.