Donnell R. Robie, JR
Electrician at Middle St, Rangely, CO

License number
Colorado 7757
Issued Date
Jul 20, 1984
Renew Date
Feb 28, 1995
Expiration Date
Feb 28, 1995
Type
Journeyman Electrician
Address
Address
298 Middle St, Rangely, CO 81648

Professional information

Donnell Robie Photo 1

Enhanced Oil Recovery Process Including The Simultaneous Injection Of A Miscible Gas And Water

US Patent:
5634520, Jun 3, 1997
Filed:
May 8, 1996
Appl. No.:
8/646888
Inventors:
Chris E. Stevens - Orchard Point, SG
Steven D. McPherson - Rangely CO
John R. Larson - Orchard Point, SG
Donnell R. Robie - Rangely CO
Ronald K. Wackowski - Vernal UT
Assignee:
Chevron U.S.A. Inc. - San Francisco CA
International Classification:
E21B 4322
US Classification:
166402
Abstract:
An enhanced oil recovery process comprises of the at least periodic introduction of (i) a non-condensible gas preferably selected from among carbon dioxide, nitrogen, methane or mixtures thereof, and (ii) an aqueous drive solution, preferably brine, into a reservoir formation. In this process, the half cycle of non-condensible gas injection, prior to aqueous drive fluid injection, measured in hydrocarbon pore volume is less than 0. 25%. In this preferred embodiment, the non-condensible gas, e. g. , carbon dioxide, and water, are simultaneously injected into the formation.


Donnell Robie Photo 2

Enhanced Oil Recovery Process Including The Simultaneous Injection Of A Miscible Gas And Water

US Patent:
5515919, May 14, 1996
Filed:
Jul 1, 1994
Appl. No.:
8/269581
Inventors:
Chris E. Stevens - Orchard Point, SG
Steven D. McPherson - Rangely CO
John R. Larson - Orchard Point, SG
Donnell R. Robie - Rangely CO
Ronald K. Wackowski - Vernal UT
Assignee:
Chevron U.S.A Inc. - San Francisco CA
International Classification:
E21B 4322
US Classification:
166273
Abstract:
An enhanced oil recovery process comprises of the at least periodic introduction of (i) a non-condensible gas preferably selected from among carbon dioxide, nitrogen, methane or mixtures thereof, and (ii) an aqueous drive solution, preferably brine, into a reservoir formation. In this process, the half cycle of non-condensible gas injection, prior to aqueous drive fluid injection, measured in hydrocarbon pore volume is less than 0. 25%. In this preferred embodiment, the non-condensible gas, e. g. , carbon dioxide, and water, are simultaneously injected into the formation.