US3057403A - In-situ combustion process for the recovery of oil - Google Patents

In-situ combustion process for the recovery of oil Download PDF

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US3057403A
US3057403A US767880A US76788058A US3057403A US 3057403 A US3057403 A US 3057403A US 767880 A US767880 A US 767880A US 76788058 A US76788058 A US 76788058A US 3057403 A US3057403 A US 3057403A
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well
oil
wells
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formation
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Malcolm R J Wyllie
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Gulf Research and Development Co
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    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/24Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
    • E21B43/243Combustion in situ

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  • This invention relates to the production of oil and more particularly to a secondary recovery process for producing oil from unconsolidated formations.
  • One of the secondary recovery processes used to increase the amount of oil produced from oil-bearing formations is the in-situ combustion process.
  • an oxygen-containing gas usually air
  • air is injected into the pay zone at an injection well, and oil in the formation is ignited at that well.
  • a combustion front moves through the pay zone from the injection well to an adjacent production well.
  • the heat and gases released by the burning of oil in the formation reduce the viscosity of the oil and the increased Ypressure resulting from the injection of gas into the formation drives the oil through the formation to the production well.
  • the conventional forward burning in-situ combustion process suffers disadvantages which in many instances prevent its use or the production of oil at rates sucient to justify the continued production of oil from the eld.
  • the radial flow pattern from a well makes necessary high velocities through the formation immediately adjacent to the injection well if satisfactory production rates are to be obtained.
  • the oil pushed ahead of the combustion front is cold and viscous.
  • the resistance to flow, particularly ⁇ at the high rates near the well is, consequently, very high.
  • the oxygen-containing gas sometimes cannot be injected at a rate sufficient to maintain the combustion.
  • Immediately ahead of the combustion front is la three-phase mixture of oil, water, and gas, which further increases resistance to flow through the formation.
  • the formation be hydraulically fractured before the in-situ combustion process is performed.
  • the permeability of the pay zone can be greatly increased and the resistance to ow during the initial stages of the in-situ combustion process can be greatly reduced.
  • many unconsolidated formations particularly those which are relatively young geologically, are extremely difficult to fracture, and are especially ditiicult to fracture iat a desired depth and in a controlled direction. Upon release of the pressure on the fracturing fluid, the unconsolidated formations frequently embed the propping agent and close the fracture.
  • This invention resides in a process for the secondary recovery of oil from unconsolidated oil-bearing formations in which a Zone of high permeability communicating with a Well is formed through the unconsolidated formation by reverse combustion. Then a fluid is injected into the formation through the zone of high permeability to drive oil from the pay zone to a production well.
  • a second zone of high permeability communicating with a production well and spaced from the first zone is formed by reverse combustion to provide a path through which oil moves from the formation to the production well.
  • FIGURE 1 is a diagrammatic illustration of an injection and production well for forming a stratum of high permeability from one well to an adjacent well by a re- Y verse combustion procedure.
  • an injection well indicated generally by reference numeral 10 extends down through a cap rock 12 and an oil-bearing formation designated as a pay zone 14 to a total depth 16.
  • Casing 18 is run into the well and is cemented in place by a cement sheath 20 in accordance with the usual practice. ln the apparatus shown in the drawings, casing 18 extends into a bed rock formation 22 underlying the pay zone 14.
  • Casing 18 and cement sheath Ztl are perforated, as indicated by reference numeral 24, at intervals from the top to the bottom of the pay zone 14.
  • the well 10 1 s closed at the well head by conventional equipment illustrated in the drawing as a cap Z6.
  • An air supply line 27 passes through the cap and extends down into the well for injection of air into the pay Zone 14.
  • FIGURE 2 a field having a number of rows of Wells is illustrated.
  • the rows are designated by letters A, B, and C.
  • the wells illustrated in FIGURE l are in row A.
  • wells and structures in rows B and C are identified by the reference numerals corresponding to the reference numerals of FIGURE 1, followed by the suiiix B and C, respectively.
  • a ⁇ second well, indicated generally by reference numeral 2S, adjacent to well llt) in row A extends through pay zone ⁇ 14 into the bed rock 22 in the manner described for well 10.
  • Casing 30 in well 28 also is cemented through the pay zone.
  • Perforations 32 extend through the casing and the surrounding cement sheath through the depth of pay zone 14.
  • Well 28 is closed at the surface by a suitable cap 34.
  • an electric heater 3.6 is suspended in the well at the level of the pay zone 14. Electric heater 36 is connected with a suitable source of current through lead lines 40 and 42. Although an electric heater 36 has been illustrated in well 28 for heating the pay zone 14 adjacent the well 28, other conventional heating means such as a burner for burning mixtures of a -fuel with air can be used,
  • an oxygen-containing gas preferably air
  • a permeable zone extending through the unconsolidated formation 14
  • an oxygen-containing gas preferably air
  • the greater permeability of the forniation to gas than oil allows the air to thread its way to vWell 28 and enter that well through perforations 32 ⁇ heater 36 can be withdrawn from well 28.
  • Burning of oil in the formation 14 by reverse combustion is accomplished by continuing injection of air into the formation 14 through well 10.
  • the combustion front moves counter to the ow of air from the vicinity of Vwell 28 toward injection well 10.
  • Oil driven from the pay zone by the hot combustion products travels in a dlrection opposite the combustion front and is produced at well 28.
  • reverse combustion proceeds from Ythe output well 28 to the well 10, continued injection of oxygen-containing gas into the formation 14 will cause forward combustion from well 10 to well 28 to burn hydrocarbons remaining in the pay zone between the two wells and further increase the permeability.
  • the process described above for Wells 10 and 28 is repeated for wells in row B to form a permeable Zone 46B between wells 10B and 28B.
  • the procedure can similarly be repeated for Wells in row C to ⁇ form a permeable zone indicated by reference numeral 46C between wells 10C and 28C.
  • the permeable zone extending from Wells l0 to 28 can be made to extend in both directions from Wells 10 and 28, for example to adjacent wells 48 and 49, to connect all of the wells in a single row, if desired.
  • an oxygen-containing gas is injected into the pay Zone 14 through one or more and preferably all of the wells in a single row in the field.
  • the wells 10, Z8, 48, and 49 in row Arand the Wells 10C, 28C, 48C, and 49C in row C are injection wells.
  • Oil in the pay Zone is then ignited and the continued injection of oxygen-containing gas, preferably air, through wells in rows A and C burns oil in therformation and supplies energy to move oil through the pay Zone 14 to the permeabie Zone 46B in row B. The oil then fiows readily through the permeable zone 46B into wells ⁇ ltBB and 23B lfrom which it is lifted to the surface.
  • the combustion to move the oil from the formation 14- towards permeable Zone 4B for delivery to the wells can be either forward or reverse combustion. Ordinarily because of the low permeability of the pay Zones in which this invention is most useful, reverse combustion to produce the oil from the pay zone yor to warm it prior to the initiation of a forward combustion phase is preferred.
  • Ignition in permeable Zone 46B can be accomplished by injecting a mixture of a combustible gas and air into permeable stratum 46B through wells in row B and igniting the mixture to heat the formation to a temperature at which ignition will occur upon contact with air or other oxygen-containing gas injected into the pay zone in row A or rows A and C.
  • permeable zones 46 and 46C to permeable zone 46B allows substantially complete removal of oil from the oil-bearing formation. Although resistance to flow through the oil-bearing formation between -the permeable zones will interfere with the fiow f oil in forward burning or gas repressuring secondary recovery procedures, the highly permeable zones extending to the wells greatly reduce the total resistance to flow. Oil can flow at high rates through the highly permeable zones directly into the Wells.
  • a mixure of air and lease gas is injected into the middle well and ignited at the other wells by means of an electric spark. After ignition, injection of the lease gas is stopped and the injection of air is continued at a rate of one and one-half million standard cubic feet per day. Reverse combustion is continued for 300 days and then converted to forward combustion in the vicinity of the first well by increasing the rate of air injection to three million standard cubic feet per day, and continued for 30 days. The procedure is repeated in three directly offset wells in an adjacent line.
  • a mixture of lease gas and air in a ratio of 15 volumes of air per volume of lease gas is injected into three wells in the first line at a total rate of ten million standard cubic feet per day.
  • the mixture breaks through into adjacent line of wells, the mixture is ignited.
  • Injection of the mixture of gases is continued forten days, after which the injection of the lease gas is stopped.
  • the injection of air is continued at .the rate of ten million standard cubic feet per day while the oil is produced from the wells in the second line.
  • the initial reverse combustion steps are highly effective in increasing the permeability of the unconsolidated formations and reducing the resistance to fiow of heavy oils present in the oil-bearing formation.
  • any clays present in that zone tend to be irreversibly dehydrated thereby preventing their swelling upon contact with Water.
  • the heat from the reverse combustion process raises the temperature of the oil in the formation and decreases its viscosity.
  • the reverse combustion procedure is particularly effective in fields containing Very heavy oils. It is possible in many such fields to cause flow of gas from one well to an adjacent well without displacing oil from the formation, whereas displacement of the cold oil from the formation is not feasible.
  • a second secondary recovery step using a linear iiow pattern is made possible.
  • the linear fiow pattern and relatively short dista-nce between the .permeable zone allow low fluxes (vol/sq. ft./hr.) for the injected air and reduced oxygen absorption in subsequent reverse combustion steps.
  • the process of this invention is particularly advantageous in producing oil from unconsolidated formations of low permeability in which the high resistance to flow makes the usual secondary recovery processes ineffective.
  • a process for the production of oil from a sub-surface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into the oil-bearing formation through a first well in a first row and withdrawing gas from a second well in the first row, igniting oil in -the formation at said second well, continuing the injection of oxygen-containing gas at the first well to cause reverse combustion to proceed from the second vwell to the first well to form a first permeable zone through a portion ⁇ of the oil-bearing formation communicating ⁇ with said first and second wells in the first row, thereafter injectingan oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of wells, igniting ⁇ oil in the formation at said second well in said second Vdrawing fluids from a well penetrating the second permeable zone to
  • a process for the production of oil from a subsurface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into the oil-bearing formation through a first well in a first row yand withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing the injection of Oxygen-containing gas at the first well to cause reverse combustion to proceed from the second well to ⁇ the first well to form a first permeable zone through a portion of the oil-bearing -formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of wells, igniting oil in the forniation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse
  • a process for the production of oil from a sub- -surface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing rgas into the oil- -bearing formation through the first well in a first row and withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing the injection of oxygen-containing gas at the first well to cause reverse combustion to proceed from the second well to the first well to form a first permeable zone through a portion of the oil-bearing formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of well-s, igniting oil in the formation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse combustion Ito
  • a process for the production of oil from a subsurface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into ⁇ the oilbearing formation through a first well in a first row and withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing Ithe injection of oxygen-containing Agas at the first well to cause reverse combustion to proceed from the second well to the first well to form a first permeable zone through a portion of the oil-bearing formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oilbearing formation through a first well in a second row of wells spaced from the first row of Wells and withdrawing gas from a second well in said second row of wells, igniting oil in the formation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse combustion to proceed from the second well in
  • a process for the production of oil from a subsurface oil-bearing formation penetrated :by -a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into the oil-bearing formation through a first well in a first row and withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing the injection of oxygen-containing gas at the first well to cause reverse combustion to proceed from the second well -to the first well to form a first permeable zone through a portion of the oil-bearing formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of wells, igniting oil in the formation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse combustion to proceed from the

Description

Oct. 9, 1962 M. R. J. WYLLIE 3,057,403
IN-sITU coMusToN PRocEss RoR THE RECOVERY oF on.
Filed Oct. 1'7, 1958 '/03 46a J3 49.5 I
-INV ENTOR. Macau Je.' J. WyLL/e 4 77' ORNE V Unite This invention relates to the production of oil and more particularly to a secondary recovery process for producing oil from unconsolidated formations.
One of the secondary recovery processes used to increase the amount of oil produced from oil-bearing formations is the in-situ combustion process. In the conventional in-situ combustion process, an oxygen-containing gas, usually air, is injected into the pay zone at an injection well, and oil in the formation is ignited at that well. A combustion front moves through the pay zone from the injection well to an adjacent production well. The heat and gases released by the burning of oil in the formation reduce the viscosity of the oil and the increased Ypressure resulting from the injection of gas into the formation drives the oil through the formation to the production well.
The conventional forward burning in-situ combustion process suffers disadvantages which in many instances prevent its use or the production of oil at rates sucient to justify the continued production of oil from the eld. The radial flow pattern from a well makes necessary high velocities through the formation immediately adjacent to the injection well if satisfactory production rates are to be obtained. At least during the early stages of the operation, the oil pushed ahead of the combustion front is cold and viscous. The resistance to flow, particularly `at the high rates near the well is, consequently, very high. If the permeability of the formation is low, the oxygen-containing gas sometimes cannot be injected at a rate sufficient to maintain the combustion. Immediately ahead of the combustion front is la three-phase mixture of oil, water, and gas, which further increases resistance to flow through the formation.
It has been suggested that the formation be hydraulically fractured before the in-situ combustion process is performed. In this manner the permeability of the pay zone can be greatly increased and the resistance to ow during the initial stages of the in-situ combustion process can be greatly reduced. However, many unconsolidated formations, particularly those which are relatively young geologically, are extremely difficult to fracture, and are especially ditiicult to fracture iat a desired depth and in a controlled direction. Upon release of the pressure on the fracturing fluid, the unconsolidated formations frequently embed the propping agent and close the fracture.
This invention resides in a process for the secondary recovery of oil from unconsolidated oil-bearing formations in which a Zone of high permeability communicating with a Well is formed through the unconsolidated formation by reverse combustion. Then a fluid is injected into the formation through the zone of high permeability to drive oil from the pay zone to a production well. In a preferred form of this invention, a second zone of high permeability communicating with a production well and spaced from the first zone is formed by reverse combustion to provide a path through which oil moves from the formation to the production well.
Referring to the drawings:
FIGURE 1 is a diagrammatic illustration of an injection and production well for forming a stratum of high permeability from one well to an adjacent well by a re- Y verse combustion procedure.
tates @atene i 3,057,433 Patented Oct. 9, 1962 wells after formation of permeable zones connecting adjacent wells in a row for a linear drive process for the secondary recovery of oil from the pay zone after the highly permeable zones have been formed through the pay zone.
Referring to FIGURE 1 of the drawings, an injection well indicated generally by reference numeral 10, extends down through a cap rock 12 and an oil-bearing formation designated as a pay zone 14 to a total depth 16. Casing 18 is run into the well and is cemented in place by a cement sheath 20 in accordance with the usual practice. ln the apparatus shown in the drawings, casing 18 extends into a bed rock formation 22 underlying the pay zone 14. Casing 18 and cement sheath Ztl are perforated, as indicated by reference numeral 24, at intervals from the top to the bottom of the pay zone 14. The well 10 1s closed at the well head by conventional equipment illustrated in the drawing as a cap Z6. An air supply line 27 passes through the cap and extends down into the well for injection of air into the pay Zone 14.
Referring to FIGURE 2, a field having a number of rows of Wells is illustrated. The rows are designated by letters A, B, and C. The wells illustrated in FIGURE l are in row A. For convenience, wells and structures in rows B and C are identified by the reference numerals corresponding to the reference numerals of FIGURE 1, followed by the suiiix B and C, respectively.
A `second well, indicated generally by reference numeral 2S, adjacent to well llt) in row A extends through pay zone `14 into the bed rock 22 in the manner described for well 10. Casing 30 in well 28 also is cemented through the pay zone. Perforations 32 extend through the casing and the surrounding cement sheath through the depth of pay zone 14. Well 28 is closed at the surface by a suitable cap 34.
For ignition o-f oil in the formation adjacent well 28, an electric heater 3.6 is suspended in the well at the level of the pay zone 14. Electric heater 36 is connected with a suitable source of current through lead lines 40 and 42. Although an electric heater 36 has been illustrated in well 28 for heating the pay zone 14 adjacent the well 28, other conventional heating means such as a burner for burning mixtures of a -fuel with air can be used,
To form the permeable zone extending through the unconsolidated formation 14, an oxygen-containing gas, preferably air, is pumped into the well through line 27 and injected through perforations 24 into the pay zone 14. Even though the permeability of the pay zone 14 is such that oil cannot be moved through the `formation at practical rates, the greater permeability of the forniation to gas than oil allows the air to thread its way to vWell 28 and enter that well through perforations 32 `heater 36 can be withdrawn from well 28.
Burning of oil in the formation 14 by reverse combustion is accomplished by continuing injection of air into the formation 14 through well 10. The combustion front moves counter to the ow of air from the vicinity of Vwell 28 toward injection well 10. Oil driven from the pay zone by the hot combustion products travels in a dlrection opposite the combustion front and is produced at well 28. After reverse combustion proceeds from Ythe output well 28 to the well 10, continued injection of oxygen-containing gas into the formation 14 will cause forward combustion from well 10 to well 28 to burn hydrocarbons remaining in the pay zone between the two wells and further increase the permeability.
The burning7 between wells 10` and 28, regardless of Whether the burning is by reverse combustion along or by reverse combustion followed by forward combustion, forms a highly permeable zone, indicated by reference numeral 46 in FIGURE 2, extending between the wells. The process described above for Wells 10 and 28 is repeated for wells in row B to form a permeable Zone 46B between wells 10B and 28B. The procedure can similarly be repeated for Wells in row C to `form a permeable zone indicated by reference numeral 46C between wells 10C and 28C. The permeable zone extending from Wells l0 to 28 can be made to extend in both directions from Wells 10 and 28, for example to adjacent wells 48 and 49, to connect all of the wells in a single row, if desired. After the formation of a permeable zone connecting adjacent Wells in a row, an oxygen-containing gas is injected into the pay Zone 14 through one or more and preferably all of the wells in a single row in the field. For purposes of illustration, the wells 10, Z8, 48, and 49 in row Arand the Wells 10C, 28C, 48C, and 49C in row C are injection wells. Oil in the pay Zone is then ignited and the continued injection of oxygen-containing gas, preferably air, through wells in rows A and C burns oil in therformation and supplies energy to move oil through the pay Zone 14 to the permeabie Zone 46B in row B. The oil then fiows readily through the permeable zone 46B into wells `ltBB and 23B lfrom which it is lifted to the surface.
The combustion to move the oil from the formation 14- towards permeable Zone 4B for delivery to the wells can be either forward or reverse combustion. Ordinarily because of the low permeability of the pay Zones in which this invention is most useful, reverse combustion to produce the oil from the pay zone yor to warm it prior to the initiation of a forward combustion phase is preferred. Ignition in permeable Zone 46B can be accomplished by injecting a mixture of a combustible gas and air into permeable stratum 46B through wells in row B and igniting the mixture to heat the formation to a temperature at which ignition will occur upon contact with air or other oxygen-containing gas injected into the pay zone in row A or rows A and C. A preferred method Of ignition is to inject a mixture of a combustible gas and air through the wells in row A and ignite that mixture as it enters the permeable zone 46B by means o=f an electric spark. After ignition, the injection of a combustible gas through the wells in row A is discontinued while the injection of the oxygen-containing gas is continued. In the arrangement shown in FIGURE 2, injection of oxygen-containing gas into the pay zone through wells in row C is continued simultaneously with the injection of oxygen-containing gas through the wells in row A.
The linear flow from permeable zones 46 and 46C to permeable zone 46B allows substantially complete removal of oil from the oil-bearing formation. Although resistance to flow through the oil-bearing formation between -the permeable zones will interfere with the fiow f oil in forward burning or gas repressuring secondary recovery procedures, the highly permeable zones extending to the wells greatly reduce the total resistance to flow. Oil can flow at high rates through the highly permeable zones directly into the Wells.
In an example of this process, in an oil field in which the Wells are arranged in a five spot pattern, three boreholes are drilled 660 feet apart in a line to a total depth of 1510, 1515, and 1522 feet through a pay zone 78 feet thick. Seven inch casing is set through the pay Zone and cemented in the conventional manner. The strings `of casing are perforated at the intervals 1445 to 1500 feet,
1450 to 1505 feet and 1455 to 1515 feet, respectively. A mixure of air and lease gas is injected into the middle well and ignited at the other wells by means of an electric spark. After ignition, injection of the lease gas is stopped and the injection of air is continued at a rate of one and one-half million standard cubic feet per day. Reverse combustion is continued for 300 days and then converted to forward combustion in the vicinity of the first well by increasing the rate of air injection to three million standard cubic feet per day, and continued for 30 days. The procedure is repeated in three directly offset wells in an adjacent line.
A mixture of lease gas and air in a ratio of 15 volumes of air per volume of lease gas is injected into three wells in the first line at a total rate of ten million standard cubic feet per day. When the gas mixture breaks through into adjacent line of wells, the mixture is ignited. Injection of the mixture of gases is continued forten days, after which the injection of the lease gas is stopped. The injection of air is continued at .the rate of ten million standard cubic feet per day while the oil is produced from the wells in the second line.
The initial reverse combustion steps are highly effective in increasing the permeability of the unconsolidated formations and reducing the resistance to fiow of heavy oils present in the oil-bearing formation. In addition to heating oil throughout the permeable zone of the formation, any clays present in that zone tend to be irreversibly dehydrated thereby preventing their swelling upon contact with Water. The heat from the reverse combustion process raises the temperature of the oil in the formation and decreases its viscosity. The reverse combustion procedure is particularly effective in fields containing Very heavy oils. It is possible in many such fields to cause flow of gas from one well to an adjacent well without displacing oil from the formation, whereas displacement of the cold oil from the formation is not feasible. By forming substantially parallel Zones of high permeability joining wells in adjacent lines, a second secondary recovery step using a linear iiow pattern is made possible. The linear fiow pattern and relatively short dista-nce between the .permeable zone allow low fluxes (vol/sq. ft./hr.) for the injected air and reduced oxygen absorption in subsequent reverse combustion steps. The process of this invention is particularly advantageous in producing oil from unconsolidated formations of low permeability in which the high resistance to flow makes the usual secondary recovery processes ineffective.
I claim:
l. A process for the production of oil from a sub-surface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into the oil-bearing formation through a first well in a first row and withdrawing gas from a second well in the first row, igniting oil in -the formation at said second well, continuing the injection of oxygen-containing gas at the first well to cause reverse combustion to proceed from the second vwell to the first well to form a first permeable zone through a portion `of the oil-bearing formation communicating `with said first and second wells in the first row, thereafter injectingan oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of wells, igniting `oil in the formation at said second well in said second Vdrawing fluids from a well penetrating the second permeable zone to displace loil through the oil-bearing formation in a direction substantially perpendicular to the rows of wells toward the second permeable zone.
2. A process for the production of oil from a subsurface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into the oil-bearing formation through a first well in a first row yand withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing the injection of Oxygen-containing gas at the first well to cause reverse combustion to proceed from the second well to` the first well to form a first permeable zone through a portion of the oil-bearing -formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of wells, igniting oil in the forniation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse combustion to proceed from the second well in said second row to the first well in said second row whereby a second permeable zone is formed spaced from and su-bstantially parallel to the first permeable zone, then injecting an oxygen-containing gas into the first permeable zone and withdrawing fluids through a well penetrating the second permeable zone to establish flow `through the oil-bearing formation between the first and ysecond permeable zone substantially perpendicular to the rows of wells, igniting oil in the formation Iadjacent the second permeable zone, continuing the injection of the oxygen-containing gas into the first permeable zone to cause reverse combustion to proceed from the second permeable zone to the first permeable zone, and lifting fluids to the surface through a well penetrating the second permeable zone.
3. A process for the production of oil from a sub- -surface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing rgas into the oil- -bearing formation through the first well in a first row and withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing the injection of oxygen-containing gas at the first well to cause reverse combustion to proceed from the second well to the first well to form a first permeable zone through a portion of the oil-bearing formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of well-s, igniting oil in the formation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse combustion Ito proceed from the second well in said second row to the first well in said second row whereby a second permeable zone is formed spaced from and substantially parallel to the first permeable zone, then injecting an oxygen-containing gas into the first permeable zone and withdrawing fiuids through a well penetrating the second permeable zone to establish fiow through the oil-bearing formation perpendicular to the rows of wells, igniting oil in the formation between the first permeable zone and the second permeable zone, continuing injection of the oxygen-containing gas into the first permeable zone to cause combustion of the oil between the two permeable zones and drive oil through the formation to -the second permeable zone and to a well penetrating the second permeable zone through which fiuids are withdrawn.
4. A process for the production of oil from a subsurface oil-bearing formation penetrated by a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into `the oilbearing formation through a first well in a first row and withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing Ithe injection of oxygen-containing Agas at the first well to cause reverse combustion to proceed from the second well to the first well to form a first permeable zone through a portion of the oil-bearing formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oilbearing formation through a first well in a second row of wells spaced from the first row of Wells and withdrawing gas from a second well in said second row of wells, igniting oil in the formation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse combustion to proceed from the second well in said second row to the first well in said second row where-by a second permeable zone is formed spaced from and substantially parallel to the first permeable zone, then injecting an oxygen-containing gas into the first permeable zone and withdrawing fluids through a well penetrating the second permeable zone to establish flow through the formation substantially perpendicular to the rows of wells, igniting oil in the formation adjacent the first permeable zone, and continuing the injection of the oxygen-containing gas into the first permeable zone to cause forward burning to proceed from the first permeable zone to the second permeable zone.
5. A process for the production of oil from a subsurface oil-bearing formation penetrated :by -a plurality of wells in a series of substantially parallel rows comprising injecting an oxygen-containing gas into the oil-bearing formation through a first well in a first row and withdrawing gas from a second well in the first row, igniting oil in the formation at said second well, continuing the injection of oxygen-containing gas at the first well to cause reverse combustion to proceed from the second well -to the first well to form a first permeable zone through a portion of the oil-bearing formation communicating with said first and second wells in the first row, thereafter injecting an oxygen-containing gas into the oil-bearing formation through a first well in a second row of wells spaced from the first row of wells and withdrawing gas from a second well in said second row of wells, igniting oil in the formation at said second well in said second row, continuing the injection of oxygen-containing gas into the first well in the second row of wells to cause reverse combustion to proceed from the second well in said second row to the first well in said second row whereby a second permeable zone is formed spaced from and substantially parallel to Ithe first permeable zone, then injecting a mixture of an oxygen-containing gas and a gaseous fuel into the first permeable zone and withdrawing fiuids through a well penetrating the second permeable zone to establish fiow through the formation substantially perpendicular to the rows of wells, igniting the mixture of oxygen-containing gas and fuel gas in the second permeable zone to ignite oil in the formation adjacent the second permeable zone, discontinuing -the injection of the fuel gas and continuing the injection of the oxygen-containing gas to cause reverse combustion from the second permeable zone to the first permeable zone and lifting fluids to the surface through a well in the second row of wells.
References Cited in the file of this patent UNITED STATES PATENTS 2,793,696 Morse May 28, 1957 2,888,987 Parker June 2, 1959 2,899,186 Crawford Aug. 11, 1959 2,906,340 Herzog Sept. 29, 1959
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Cited By (13)

* Cited by examiner, † Cited by third party
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US3132692A (en) * 1959-07-27 1964-05-12 Phillips Petroleum Co Use of formation heat from in situ combustion
US3152638A (en) * 1960-07-15 1964-10-13 Pan American Petroleum Corp Underground reverse combustion process
US3153448A (en) * 1959-09-17 1964-10-20 Continental Oil Co Combination in situ combustion-aqueous medium drive oil recovery method
US3154143A (en) * 1961-07-13 1964-10-27 Pan American Petroleum Corp Underground combustion process
US3167117A (en) * 1963-02-08 1965-01-26 Phillips Petroleum Co Producing oil from an oil-bearing stratum having high directional permeability
US3246693A (en) * 1963-06-21 1966-04-19 Socony Mobil Oil Co Inc Secondary recovery of viscous crude oil
US3253652A (en) * 1963-06-24 1966-05-31 Socony Mobil Oil Co Inc Recovery method for petroleum oil
US3259186A (en) * 1963-08-05 1966-07-05 Shell Oil Co Secondary recovery process
US3276518A (en) * 1961-08-08 1966-10-04 Deutsche Erdoel Ag Process for extracting liquid bitumens from an underground deposit
US3292699A (en) * 1964-08-10 1966-12-20 Mobil Oil Corp Process for in situ retorting of oil shale
US3386507A (en) * 1966-10-03 1968-06-04 Phillips Petroleum Co Oil well performance
US3386504A (en) * 1965-12-29 1968-06-04 Texaco Inc Recovery of hydrocarbons from underground formations by in situ combustion
US20110277992A1 (en) * 2010-05-14 2011-11-17 Paul Grimes Systems and methods for enhanced recovery of hydrocarbonaceous fluids

Citations (4)

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Publication number Priority date Publication date Assignee Title
US2793696A (en) * 1954-07-22 1957-05-28 Pan American Petroleum Corp Oil recovery by underground combustion
US2888987A (en) * 1958-04-07 1959-06-02 Phillips Petroleum Co Recovery of hydrocarbons by in situ combustion
US2899186A (en) * 1959-08-11 In situ combustion of stratum having an exposed face
US2906340A (en) * 1956-04-05 1959-09-29 Texaco Inc Method of treating a petroleum producing formation

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2899186A (en) * 1959-08-11 In situ combustion of stratum having an exposed face
US2793696A (en) * 1954-07-22 1957-05-28 Pan American Petroleum Corp Oil recovery by underground combustion
US2906340A (en) * 1956-04-05 1959-09-29 Texaco Inc Method of treating a petroleum producing formation
US2888987A (en) * 1958-04-07 1959-06-02 Phillips Petroleum Co Recovery of hydrocarbons by in situ combustion

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3132692A (en) * 1959-07-27 1964-05-12 Phillips Petroleum Co Use of formation heat from in situ combustion
US3153448A (en) * 1959-09-17 1964-10-20 Continental Oil Co Combination in situ combustion-aqueous medium drive oil recovery method
US3152638A (en) * 1960-07-15 1964-10-13 Pan American Petroleum Corp Underground reverse combustion process
US3154143A (en) * 1961-07-13 1964-10-27 Pan American Petroleum Corp Underground combustion process
US3276518A (en) * 1961-08-08 1966-10-04 Deutsche Erdoel Ag Process for extracting liquid bitumens from an underground deposit
US3167117A (en) * 1963-02-08 1965-01-26 Phillips Petroleum Co Producing oil from an oil-bearing stratum having high directional permeability
US3246693A (en) * 1963-06-21 1966-04-19 Socony Mobil Oil Co Inc Secondary recovery of viscous crude oil
US3253652A (en) * 1963-06-24 1966-05-31 Socony Mobil Oil Co Inc Recovery method for petroleum oil
US3259186A (en) * 1963-08-05 1966-07-05 Shell Oil Co Secondary recovery process
US3292699A (en) * 1964-08-10 1966-12-20 Mobil Oil Corp Process for in situ retorting of oil shale
US3386504A (en) * 1965-12-29 1968-06-04 Texaco Inc Recovery of hydrocarbons from underground formations by in situ combustion
US3386507A (en) * 1966-10-03 1968-06-04 Phillips Petroleum Co Oil well performance
US20110277992A1 (en) * 2010-05-14 2011-11-17 Paul Grimes Systems and methods for enhanced recovery of hydrocarbonaceous fluids

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