Electrothermal process for recovering hydrocarbons

• US 4,412,585 A
• Filed: 05/03/1982
• Issued: 11/01/1983
• Est. Priority Date: 05/03/1982
• Status: Expired due to Fees

• Current Assignee: Cities Service Co. (PDV Holding, Inc.)
• Original Assignee: Cities Service Co. (PDV Holding, Inc.)
• Inventors: Bouck, Larry S.
• Primary Examiner(s): Novosad, Stephen J.
• Assistant Examiner(s): Suchfield, George A.
• Application Number:
  US06/374,582
• Time in Patent Office: 547 Days
• Field of Search: 166/248, 166/272, 166/288, 166/302, 166/57, 166/58, 166/59, 166/60, 166/65 R
• US Class Current: 166/248
• CPC Class Codes: E21B 36/04 using electrical heaters
• CPC Class Codes: E21B 43/2401 by means of electricity

Abstract

In a pair of electrode wells to be developed for injection and production wells for the electrothermal process for recovering heavy hydrocarbons, the electrodes are formed by inserting a heating device in each borehole and heating the surrounding formation to a temperature at which the hydrocarbon-containing material undergoes thermal cracking, resulting in a coke-like residue surrounding the heater. This conductive and permeable material serves as an electrode, for each well, by which the formation is heated. The heavy hydrocarbon material, such as bitumen found in tar sands, becomes mobile and can be recovered.

Claims

1. An electrothermal process for recovering hydrocarbon values from an underground hydrocarbon-bearing formation having at least two separated boreholes penetrating the hydrocarbon-bearing formation, comprising the steps of:

(a) placing a heating device in the first borehole,

(b) energizing the device to heat the surrounding formation to a temperature high enough to produce coking of at least a portion of the hydrocarbon-bearing formation, thus forming a coked zone, which, having conductive properties, acts as an electrode,

(c) maintaining the temperature of step (b) for a length of time to obtain a coked zone electrode having an effective radius at least twice that of the borehole,

(d) repeating steps (a-c) in a second borehole,

(e) applying a voltage between the coked zone electrodes of the first and second boreholes, to heat the formation between the boreholes to a temperature at which the hydrocarbon values are mobile, and

(f) recovering hydrocarbon values from one of said boreholes.

2. The process of claim 1, wherein:

(a) The temperature of the heating device varies from about 800°

F. (426°

C.) to about 1500°

F. (815°

C.),

(b) the time for maintaining the temperature of the heating device is from about one to about twelve months,

(c) an electrolyte solution is introduced to the coked zone to assist in the formation of an effective electrode of enlarged radius, said radius being larger than the radius of the borehole, and

(d) voltage is applied between the electrodes of the separated boreholes until the mid-point temperature of the formation is from about 130°

F. (54°

C.) to about 230°

F. (110°

C.).