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US3091292A - Recovering hydrocarbons from subsurface formations - Google Patents

Recovering hydrocarbons from subsurface formations
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US3091292A
US3091292AUS792904AUS79290459AUS3091292AUS 3091292 AUS3091292 AUS 3091292AUS 792904 AUS792904 AUS 792904AUS 79290459 AUS79290459 AUS 79290459AUS 3091292 AUS3091292 AUS 3091292A
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formation
limestone
acid
hydrocarbons
hydrocarbon
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Paul F Kerr
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Texaco Inc
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Texaco Inc
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United States Patent Ofice 3,091,292 Patented May 28, 1963 3,091,292 RECOVERING HYDRGCARBUNS FRM SUB- SURFACE FRMATINS Paul F. Kerr, New York, NSY., assigner to Texaco Inc., a 4corporatirm of Delaware Filed Feb. 12, 1959, Ser. No. 792,904 16 Claims. (Cl. 16d-l1) This invention relates to the recovery of hydrocarbons from subsurface formations. In accordance with one embodiment this invention is directed to the recovery of hydrocarbons from the Athabasca tar sands. In accordance with another embodiment this invention is directed to the recovery of viscous petroleum or bituminous material from underground formations. In accordance with yet another embodiment this invention is particularly directed to the recovery of petroleum, bituminous or hydrocarbon material and the like from an underground formation adjacent an underlying limestone formation.
In the recovery of petroleum and/ or bituminous material from underground formations, such as the Athabasca tar sands, because of the rather high viscosity of the in place hydrocarbons and/or bituminous material and in formations where because of the absence of a substantial natural driving force the production of hydrocarbons therefrom is difficult, various methods have been proposed to improve the production and recovery of these hydrocarbons from these formations. Methods which have been proposed include in situ combustion of underground formations containing these hydrocarbons, the displacement of hydrocarbons from underground formations by contact with hot water, in situ solvent extraction processes and the like. None of the methods proposed heretofore have been completely satisfactory.
Accordingly it. is an object of this invention -to provide a method for the recovery of viscous petroleum and/or bituminous material and the like from underground formations.
Another object of this invention is to provide a method for the recovery' of petroleum and the like from underground formations, such as the Athabasca tar sands.
Still another object of this invention is to provide a method for the recovery of petroleum and similar material from an underground formation adjacent an underlying limestone formation.
How these and other objects of this invention are accomplished will become apparent in the light of the accompanying disclosure and drawing which schematically illustrates the practice of this invention as applied to a particular hydrocarbon-containing formation, such as the Athabasca tar sand. In at least one embodiment of the practice of this invention at least one of the foregoing objects will be achieved.
In accordance with this invention an improved method for the recovery of hydrocarbons or bituminous material and the like from underground formations is provided by creating or forming within said formation, especially in a different formation adjacent thereto but in communication with said hydrocarbon-containing formation, a relatively high temperature and relatively high pressure zone whereby formation fluids within said hydrocarboncontaining formations are heated and pressured. The resulting heated and pressured hydrocarbons are then displaced and recovered from the hydrocarbon-containing A formation at a location relatively remote from said high pressure, high temperature zone via a production well.
In accordance with a practice of this invention particularly applicable -to the production and recovery of petroleum or bituminous material and the like from the Athabasca tar sands, wherein the hydrocarbon-containing formation or tar sand is adjacent an underlying limestone (calcium-magnesium carbonate) formation, an injection Well is formed to penetrate the hydrocarbon-containing formation or tar sand and the adjacent, underlying limestone formation and a production well, at a location removed from said injection well, is formed to penetrate said hydrocarbon-containing and said underlying limestone formation. A relatively high temperature and high pressure Zone is then formed within said formations, desirably within said limestone formation, in the vicinity of said injection well. The resulting heated formation fluids, hydrocarbons and the like, within said hydrocarbon-containing formation are then displaced under the influence of said high temperature and pressure zone in the direction of said production well. These displaced formation fluids are then produced and recovered via said production well.
Various methods may be employed in the practice of this invention for the creation of a relatively high temperature, high pressure zone in the vicinity of the injection well to displace hydrocarbons from the hydrocarbon-containing formation toward a production well. In accordance with one embodiment the formation, such as the limestone formation, is fractured either by setting off an explosive charge (explosive fracturing) or by application of hydraulic pressure (hydraulic fracturing) to create a zone of relatively high permeability within the limestone formation in the vicinity of said injection well adjacent the hydrocarbon-producing formation. A displacing iluid, preferably a hot displacing fluid, is then introduced into the hydrocarbon-containing formation and into the fractured limestone formation to heat the formation fluids within said hydrocarboncontaining formation in the direction of the production well. Suitable displacing liuids include steam, hot air, hot ue gases, combustion gases, or mixtures or combinations thereof, either injected simultaneously or consecutively.
In accordance with one preferred embodiment of the practice of this invention the limestone formation in the vicinity of the injection well is fractured, eg. explosively fractured, and the resulting fractured formation then contacted wtih a suitable acid, preferably a mineral acid whose calcium salt is water soluble, such as sulfuric acid, hydrochloric acid and the like. The acid upon contact with the fractured limestone formation reacts with the limestone with the resulting formation of normally gaseous carbon dioxide. Since the heat of reaction between the acid and the limestone is substantial the resulting acidtreated formation increases in temperature. The heat of reaction, besides increasing the temperature of the acidtreated limestone formation, also heats the adjacent overlying hydrocarbon-containing formation or tar sand. The carbon dioxide generated during the acid treatment of the limestone formation in addition to pressuring the limestone formation and the adjacent hydrocarbon-containing formation and displacing hydrocarbons therefrom carries heat to the hydrocarbon-containing formation and the formation uids therein with the result that the formation fluids within the hydrocarbon-containing formation are heated and are more readily displaced toward the production well. As a result of the fracturing and acid treatment of the limestone formation in the vicinity of the injection well adjacent the hydrocarbon-containing formation there tends to be created or is created within the limestone formation a cavern or cavernous-like Zone or a zone of very high porosity and permeability. This zone is particularly useful for the subsequent injection of a treating or displacing fluid, such as hot water, steam, and the like, and/ or for the transfer of the carbon dioxide generated during the acid treatment step to heat and/or to displace the hydrocarbons within the hydrocarboncontaining formation adjacent the cavernous-like zone in the direction of the production well.
Desirably a cavern or cavernous-like zone or zone of high permeability is also established within the limestone formation in the vicinity of the production well penetrating the same. The thus-formed cavernous or highly permeable zone in the vicinity of the production well serves as a sump or collection point for the hydrocarbons within the hydrocarbon-containing formation displaced in Ithe direction from the injection well toward the production well.
Referring now to the accompanying drawing which schematically illustrates a practice of this invention as applied to the recovery of hydrocarbons or bituminous material from tar sands, such as Athabasca tar sand which overlie an adjacent limestone formation, an injection well 11 penetrates the overburden 12, the hydrocarbon-containing formation ortar sand 14 and thelimestone formation 15. Similarly, a production well 16 penetrates the overburden 12, .theltar sand 14 and thelimestone formation 15. Thelimestone formation 15 in the vicinity of injection well 11 is fractured, either explosively fractured by exploding a charge of explosive therein or hydraulically fractured by the application of hydraulic pressure.
The resulting fractured limestone formation is then treated with acid introduced into fracturedlimestone formation 15 via injection well 11 to form a cavernous zone or cavern 18. Suitable acid for treatment of thelimestone formation 16 to form cavern 18 therein include the mineral acids whose calcium salts are water soluble, such las sulfuric acid, hydrochloric acid and nitric acid or mixtures thereof. Upon introduction of the acid intolimestone formation 15 Via well bore 11 the acid reacts with the limestone (calcium carbonate) therein with the resultant generation of normally gaseous carbon dioxide. 'The heat of reaction betweent he acid and the limestone causes the temperature of thelimestone formation 15 in the vicinity of injection well 111 to increase. The heat of reaction, at least in part, is carried away from the acid-treated portion oflimestone formation 15 in the vicinity of injection well 11 by the gaseous carbon dioxide which, under a relatively elevated pressure, penetrates or invades thetar sand 14 adjacent cavern 18, the acidtreated portion oflimestone formation 15, and increases the temperature oftar sand 14 in the vicinity o-f injection well 11. The gaseous carbon dioxide which invades or penetratestar sand 14, and/or subsequently injected extraneous displacing fluid, serves to displace the formation hydrocarbons withintar sand 14 in the direction of production well `16j.
Desirably while cavern 18 is being formed withinlimestone formation 15 in the vicinity of injection well 11 another cavern or cavernous-like zone orhigh permeability Zone 19 is likewise being created within limestone 'formation 15 in the vicinity of production well 16. The
cavernous zone 19 withinlimestone formation 15 in the vicinity of production well 16 may 4be formed in substantially the same manner as cavern 118 was formed. The cavern orhigh permeability zone 19 serves as a sump or collecting point for the hydrocarbons displaced withintar sand 14 in the direction from injection well 11 to the production well 16.
As indicated in Ithe accompanying drawing fractures or high permeability zones orstreaks 20 are shown extending between cavern 18Vand cavern 19. These high permeability streaks or fractures, formed by properly spacing injection well 11 and production well 16 and by suitably carrying out the explosive or hydraulic fracturing oflimestone formation 15 for the formation ofcavernous Zones 18 and 19, enable ready iiuid communication between cavern 18 andcavern 19 and make possible rapid heating of thelimestone formation 15intermediate caverns 18 and 19 by the passage of a suitable heating iuid therethrough. The heating oflimestone formation 15intermediate caverns 18 and 19 serves toheat tar sand 14, at least that portion thereof overlying and immediatelyadjacent limestone formation 15, thereby expediting the recovery of the formation fluids therefrom.
To further expedite the recovery of the formation fluids, petroleum and the like, fromtar sand 14 there may be introduced via injection well 11 in-to cavern 18 an extraneous heating fluid such as hot water, hot combustion gases 4and the like. The thus-injected hot extraneous uid upon penetration intotar sand 14 would serve to displace the formation fluids therefrom in the direction ofcavern 19 and production well 16.
Itis mentioned that sincecaverns 18 and 19 are formed withinlimestone formation 15 in the vicinity of injection well 11 and production well 16, respectively, uid communication directly between these caverns and thetar sand 14 is effected. If desired, the formation ofcaverns 18 and 19 can be elected to such a radial extent that caving or collapse of a portion of thetar sand 14 in the vicinity of the wells into caverns 18 and/or 19 can be effected. By operating in the aforesaid manner, Le. cavern creation and, if desired, collapse of a portion oftar sand 14 into the cavern, a large amount of surface area is opened up withintar sand 14 for the injection thereinto of a displacing fluid to displace formation fluids fromtar sand 14 in the direction of production well 16.
One feature which makes this invention particularly applicable to the recovery of petroleum from the Athabasca tar sands resides in the recovery of sulfur from the petroleum recovered fromtar sand 14. This petroleum has a relatively high sulfur content. When this sulfur, after recovery by suitable known methods, is oxidized and converted to sulfuric acid the thus-formed sulfuric acid can be employed for the formation of additional caverns to promote the production of additional petroleum from the tar sand. If sulfuric acid is not desired, the presence of salt beds in the vicinity of the Athabasca tar sands suggests that the sulfuric acid can readily be chemically converted by reaction with sodium chloride to hydrochloric acid which can then be employed as the acid for the formation of caverns.
Although the drawing indicates the practice of this invention with respect to a single injection well and a single production well any number of injection wells and any number of production wells in any suitable pattern may be employed.
As will be apparent to those skilled in the art many changes, modifications and substitutions are possible in the practice of this invention without departing from the spirit or scope thereof.
I claim:
l. A method of producing hydrocarbons from a subsurface hydrocarbon-containing formation in contact with van underlying contiguous limestone formation, said hydrocarbon-containing formation and said limestone formation each being penetnated by at least one common injection well and at least one common production well, which comprises fracturing said limestone formation in the vicinity of said injection well Iand in the vicinity of said production well, introducing la Imineral acid whose calcium .salt is water soluble via said injection well .and said production well into the fractured limestone formation adjacent fthe wells `to react with the limestone therein -to form a zone of high permeability, introducing a hot displacing fluid v-ia said injection well into said hydrocarbon-containing formation :and said fractured, acid-treated iimestone lformation to displace in situ hydrocarbons from said hydrooarbon-containing formation toward said production well, and producing the resulting displaced hydrocarbons from said hydrocarbon-containing Iformation via said production well.
2. A method in accord-ance with claim l wherein said acid is hydrochloric acid.
3. A method in accordance with claim l wherein said acid is sulfuric acid.
4. A method in accordance with claim 1 wherein said displacing Kiuid is a hot gaseous iluid.
5. In the method of producing hydrocarbons as defined in claim 1, the additional formation of .a cavern-like Zone in the fractured limestone formation adjacent the wells.
6. A method of producing hydrocarbons from a su-bsurface hydrocarbon-containing formation in contact with an underlying contiguous limestone formation which comprises penetrating the formations with at least one injection Well and with at least one production Weil, tfracturing said `limestone. formation in the vicinity of said injection well and in the vicinity of said production well, introducing acid whose calcium salt is water soluble via said in jection well int-o the fractured limestone formation in the vicinity of said injection Well 4whereby said acid by reaction with the limestone forms a relatively high temperature zone in said fractured limes-tone 'formation due to chemical heat of reaction and forms a relatively high pressure Zone therein due to the release of carbon dioxide by reaction between said acid and said limestone, heating in situ hydrocarbons in the vicinity of said injection well and displacing said in situ hydrocarbons tow-ard said production Well by the thus-produced chemical heat of reaction and the released carbon dioxide, :and producing the resulting displaced hydrocanbons Via said production well.
7. A :method in accordance with claim 6 wherein acid whose calcium salt is water solubile is introduced also via said production Well into the fractured limestone formation in the vicinity thereof prior to the production of 4hydrocarbons from said hydrocanbon-containing formation via said production well.
8. A method in accordance with claim 6 wherein said acid is sulfuric acid.
9. A lmethod in accordance with claim 6 wherein said acid is hydrochloric acid.
10. A method in accordance with claim 6 wherein there is introduced via said injection well into the formations a displacing fluid .to aid in the displacement of the in situ hydrocarbons from said 'hydrocarbon-containing formation toward said production Well.
111. A method in accordance with claim 10 wherein said 'displacing fluid comprises relatively hot gaseous products of combustion.
12. A method in accordance with claim 10 wherein said displacing fluid is steam.
d3. A method in accordance with claim 10 'wherein said displacing iiuid is hot water.
14. A method in accordance with claim 10 wherein said Idisp-lacing vfluid is hot air.
15. A method in accordance with claim 7 wherein said acid is sulfuric acid.
y16. A method in accordance with claim 7 wherein said acid is hydrochloric acid.
References Cited in the le of this patent UNITED STATES PATENTS 2,584,605 Merriam etal. Feb. 5, 1952 2,734,578 Waiter Peb'. 14, 1956 12,734,579 Ellcins Fe' b. 14, 1956 2,780,449 Fisher et a-l Feb. 5, 1957 2,780,450 Ljungstrom Feb. 5, 1957

Claims (1)

1. A METHOD OF PRODUCING HYDROCARBONS FROM A SUBSURFACE HYDROCARBON-CONTAINING FORMATION IN CONTACT WITH
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US3272261A (en)*1963-12-131966-09-13Gulf Research Development CoProcess for recovery of oil
US3342258A (en)*1964-03-061967-09-19Shell Oil CoUnderground oil recovery from solid oil-bearing deposits
US3616852A (en)*1969-09-101971-11-02Texaco IncOil recovery process using dilute acid
US4473120A (en)*1983-04-291984-09-25Mobil Oil CorporationMethod of retorting oil shale using a geothermal reservoir
US4589487A (en)*1982-01-061986-05-20Mobil Oil CorporationViscous oil recovery
US5168930A (en)*1989-10-171992-12-08Ben W. WisemanDesiccant for well acidizing process
US5255740A (en)*1992-04-131993-10-26Rrkt CompanySecondary recovery process

Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2584605A (en)*1948-04-141952-02-05Edmund S MerriamThermal drive method for recovery of oil
US2734579A (en)*1956-02-14Production from bituminous sands
US2734578A (en)*1956-02-14Walter
US2780449A (en)*1952-12-261957-02-05Sinclair Oil & Gas CoThermal process for in-situ decomposition of oil shale
US2780450A (en)*1952-03-071957-02-05Svenska Skifferolje AbMethod of recovering oil and gases from non-consolidated bituminous geological formations by a heating treatment in situ

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2734579A (en)*1956-02-14Production from bituminous sands
US2734578A (en)*1956-02-14Walter
US2584605A (en)*1948-04-141952-02-05Edmund S MerriamThermal drive method for recovery of oil
US2780450A (en)*1952-03-071957-02-05Svenska Skifferolje AbMethod of recovering oil and gases from non-consolidated bituminous geological formations by a heating treatment in situ
US2780449A (en)*1952-12-261957-02-05Sinclair Oil & Gas CoThermal process for in-situ decomposition of oil shale

Cited By (7)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US3272261A (en)*1963-12-131966-09-13Gulf Research Development CoProcess for recovery of oil
US3342258A (en)*1964-03-061967-09-19Shell Oil CoUnderground oil recovery from solid oil-bearing deposits
US3616852A (en)*1969-09-101971-11-02Texaco IncOil recovery process using dilute acid
US4589487A (en)*1982-01-061986-05-20Mobil Oil CorporationViscous oil recovery
US4473120A (en)*1983-04-291984-09-25Mobil Oil CorporationMethod of retorting oil shale using a geothermal reservoir
US5168930A (en)*1989-10-171992-12-08Ben W. WisemanDesiccant for well acidizing process
US5255740A (en)*1992-04-131993-10-26Rrkt CompanySecondary recovery process

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