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Publication numberUS3196944 A
Publication typeGrant
Publication dateJul 27, 1965
Filing dateDec 11, 1961
Priority dateDec 11, 1961
Publication numberUS 3196944 A, US 3196944A, US-A-3196944, US3196944 A, US3196944A
InventorsBernard George G, Holbrook Orrin C
Original AssigneePure Oil Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Miscible-displacement process
US 3196944 A
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Description  (OCR text may contain errors)

3,196,944 MISCIBLE-DISPLACEMENT PROCESS George G. Bernard and Orrin C. Holbrook, Crystal Lake, [1]., assignors to The Pure Oil Company, Chicago, 11].,

a corporation of Ohio No Drawing. Filed Dec. 11, 1961, Ser. No. 158,575 7 Claims. (Cl. 166-9) This invention relates to the recovery of petroleum from subterranean reservoirs. It is more specifically concerned with improving the efficiency o f gas-drive, secondaryr e; covery operations.

Secondary recovery of petroleum by the injection of a gas through an input well and withdrawal of reservoir fluids from a producing Well has long been known and practiced. It was later discovered, in laboratory core experiments, that the recovery of petroleum by gas-drive could be greatly increased by first injecting a liquid hydrocarbon of low viscosity through the injection well, and

following this slug of liquid hydrocarbon with a gas which is miscible with or highly soluble in the liquid hydrocarbon. Thus, it was found, for example, that when a petroleum-containing core was treated by the injection of a small amount of low-molecular-weight hydrocarbon, such as liquid propane, and then driven by a gas which is miscible with the propane, such as natural gas or methane, a highly efiicient process was obtained.

Oil recoveries achieved in applying such miscibledisplacement gas-drive processes to actual reservoirs were disappointing, in that the total oil recovery fell far short of that anticipated from predictions based on core experiments. It was found that while the process in fact succeeds in recovering practically all of the petroleum in the reservoir which is contacted by the injected liquid hydrocarbon, large quantities of petroleum are still by-passed and left in the reservoir when the process is carried out. This unfortunate result is due to the unfavorable mobility relationships of the reservoir fluids and injected fluids, which results in unsatisfactory areal sweep efficiencies and a corresponding decrease in the over-all efficiency of the process.

It is an object of this invention to provide an improved miscible-displacement, gas-drive, secondary-recovery proc cess by which greater quantities of oil can be produced. Another object of this invention is to provide a miscibledisplacement, gas-drive process in which greatly enhanced areal sweep efficiencies are obtained.

It has ben found that the areal sweep efliciency of miscible-displacement, gas-drive, secondary-recovery processes can be greatly improved, and the over-all efficiency of the processes thereby enhanced, by incorporating in the low-viscosity liquid hydrocarbon injected a small amount of a high-foaming surfactant. The surfactant must be oilsoluble, and of the high-foaming type as hereinafter defined. It has been found that the injected driving gas coacts with the surfactant-containing liquid hydrocarbon to produce a stable foam which appears as a bank at the trailing edge of the bank of injected liquid hydrocarbon.

In carrying out the process of this invention, about 0.03 to 0.20 reservoir pore volume of a low-viscosity liquid hydrocarbon is first injected through the input well and into the reservoir. The liquid hydrocarbon is preferably a liquefied, normally gaseous, low-molecular-weight material, such as L.P.G., propane, or butane. However, other low-molecular-weight, normally liquid hydrocarbon fractions may be used. In general, hydrocarbon fractions consisting predominantly of C and lower hydrocarbons are satisfactory. The gas injected to provide a gas drive must be inert, and miscible with, or highly soluble in, the injected hydrocarbon. Gases such as methane, ethane, and natural gas are preferred. The oil-soluble, high-foaming surfactant should be incorporated in the United States Patent 0 SEARm-i WWW 3,196,944 Patented July 27, 1965 ice first-injected liquid hydrocarbon in the amount of about 0.1 to 5% by weight. The exact amount will vary de pending upon the nature of the surfactant injected, but should be suflicient to produce a substantial quantity of stable foam upon contact of the surfactant-containing liquid hydrocarbon with natural gas. The exact amount of surfactant to be used can be determined by experiment, as hereinafter described.

The term high-foaming surfactant, as used in this specification and the appended claims, denotes a surfactant which, when incorporated in a liquid hydrocarbon in an amount not in excess of 5% by weight, meets the follow ing test. The surfactant is dissolved in a hydrocarbon, such as hexane, and 500 ml. of the solution is placed in a graduated cylinder to form a column having a height of 50 centimeters. Natural gas at low pressure is passed into the bottom of the column through a fritted-glass disc at substantially atmospheric pressure, so that the gas bubbles through the column of liquid and passes out of the top of the cylinder. The gas rate is maintained at about 500 ml. of gas per minute, per square inch of column cross-sectional area. The flow of gas is continued for a period of 15 minutes, after which time the flow of gas is discontinued. A column of foam will then be found to exist at the top of the column of liquid hydrocarbon. A high-foaming surfactant, as defined in this specification, must be capable of producing a column of foam not less than centimeters in height under the conditions aforedescribed.

With some high-foaming surfactants, the afore-described 3;;

hydrocarbon. Thus, where it is found that 2% by weight of a given surfactant is capable of meeting the requirements of the afore-defined experiment, it is preferred, for reasons of economy, that this amount be used. The use of excess quantities of surfactant should be avoided for reasons of economy, and to prevent the production of an excessively thick and viscous foam bank, which results in the necessity for employing excessive gas-injection pressures. While the use of various commercial high-foaming surfactants is contemplated, an example of a satisfactory foaming agent is a 1-to-1 mixture of di-coco dimethyl ammonium chloride and decyl trimethyl ammonium chloride. This mixture can be used in the amount of about 2% by weight, with excellent results. High-foaming surfactants can be selected from published tables describing the properties of commercially available surfactants.

As a speci figgxample of the method of this invention, a petroleum-containing reservoir is subjected to secondary recovery by injecting through an input well a s lpgpf liquid propane in which is incorporated 2% by weight of a 1-to-1 mixture of di-coco dimethyl ammonium chloride and decyl trimethyl ammonium chloride. Natural ga s is then injected at sufiicient pressure to maintain the propane as a liquid, to drive the propane bank toward four producing wells which surround the injection well. Petroleum is produced from the producing wells until the gas-to-oil ratio reaches an unattractively high value. At this point, the injection of gas is terminated and production continued under conditions of pressure depletion.

While allifi the injected liquid hydrocarbon may contain a high-foaming surfactant, and such is preferred where small amounts of liquid hydrocarbon are injected, when larger banks of liquid hydrocarbon are used, it is preferred that the surfactant be incorporated (mlyim the last-injected portion of the liquid hydrocarbon. Thus, where the quantity of liquid hydrocarbon l entire quantity of liquid hydrocarbon, or at least in most j' of it. Where a largerbank of propane is employed, such as 0.15 reservoir pore volume, it is preferred that the surfactanb-he incorporated only in the last-injected por-, tion of the liquid hydrocarbon. The amount of liquid hydrocarbon in which the surfactant is placed should be not less than about 0.03 reservoir pore volume, and ordinarily will be about 0.05 reservoir pore volume. Where the reservoir is known to contain substantial quantities of free gas dispersed in a substantially homogeneous distribution throughout the reservoir, it is especially preferred that the first-injected liquid hydrocarbon contain no surfactant in order to avoid the production of a bank of foam at the leading edge of the liquid hydrocarbon bank, thereby encouraging the liquid hydrocarbon to bypass a portion of the reservoir. On the other hand, where the reservoir is known to contain free gas which is localized in a gas cap above the petroleum-containing portions of the reservoir, it is advantageous to distribute the surfactant throughout the entire liquid hydrocarbon bank, so that the production of a foam bank at the interface with the gas cap will occur, thus retarding the entry of the liquid hydrocarbon bank into the gas cap, and avoiding consequent bypassing of the petroleum-containing portions of the formation.

' The objects of this invention cannot be achieved by incorporating the surfactant in the injected gas, rather than in the liquid hydrocarbon, for the reason that any foam produced will lag behind the liquid hydrocarbongas interface, and the presence of the foam at this interface is essential.

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:

1. The method for recovering petroleum from underground reservoirs penetrated by an injection well and a 2. The method in accordance with claim 1 in which the amount of liquid hydrocarbon injected is in excess of 0.05 reservoir pore volume, and the portion of said liquid hydrocarbon in which the high-foaming surfactant is incorporated is not in excess of 0.05 reservoir pore volume.

3. The method in accordance with claim 1 in which the high-foaming surfactant is in hydrocarbon solution in the amount of about 0.1 to 5.0% by weight.

4. The method in accordance with claim 1 in which the liquid hydrocarbon is liquefied propane, and the hydrocarbon gas is injected under sufficient pressure to maintain said propane as a liquid in the reservoir.

- 5. The method in accordance with claim 4 in which the concentration of high-foaming surfactant in said propane is about 0.1 to 5.0% by weight.

6. The method in accordance with claim 5 in which the quantity of propane injected is in excess of 0.05 reservoir pore volume, and the last-injected portion of said bank in which high-foaming surfactant is incorporated amounts to about 0.05 reservoir per volume.

7. The method in accordance with claim 6 in which said high-foaming surfactant is a 1-to-1 mixture of dicoco dimethyl ammonium chloride and decyl trimethyl producing well comprising injecting through said injection well and into said formation 0.03 to 0.20 reservoir pore volume of a low-molecular-weight liquid hydrocarbon, at least the last-injected 0.03 reservoir pQIe. volume.

of which contains in solution ghigh-fogming, oil-soluble V surfactant in an amount suflicient to produce a foam on contact in the reservoir with a hydrocarbon gas, win; jecting hydrocarbon gas, substantially free of a surfactant, to form a foam bank at least between said injected liquid hydrocarbon and said hydrocarbon gas and to drive said injected liquid hydrocarbon toward said producing well, and recovering petroleum therefrom.

ammonium chloride, and the mixture is incorporated in the propane in the amount of about 2% by weight.

References Cited by the Examiner UNITED STATES PATENTS Armour and Company publication, received in Patent Officer, 1954.

Dunning:

Using Foaming Agents To Remove Liquids From Gas Wells, Monograph 11, Bureau of Mines. Published 1961, 166-45 (38 pages).

5 CHARLES E. OCON-NELL, Primary Examiner.

NOR AN YU OFF, Examin

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2866507 *Dec 24, 1956Dec 30, 1958Pure Oil CoGas drive oil recovery process
US3082822 *Nov 19, 1959Mar 26, 1963Pure Oil CoSecondary recovery waterflood process
GB696524A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3306354 *Jun 5, 1964Feb 28, 1967Union Oil CoMethod for storing fluids in a subterranean formation
US3323588 *Sep 28, 1964Jun 6, 1967Union Oil CoMethod of secondary recovery employing successive foam drives of different ionic characteristics
US3329206 *Dec 29, 1964Jul 4, 1967Poollen Hendrik K VanProcess for storing natural gas
US3335792 *Dec 18, 1964Aug 15, 1967Union Oil CoMethod for increasing oil recovery
US3342256 *Apr 17, 1964Sep 19, 1967Union Oil CoMethod for recovering oil from subterranean formations
US3342261 *Apr 30, 1965Sep 19, 1967Union Oil CoMethod for recovering oil from subterranean formations
US3366175 *Oct 1, 1965Jan 30, 1968Continental Oil CoSecondary recovery process in a gas cap reservoir
US3376924 *Oct 1, 1965Apr 9, 1968Continental Oil CoFoam drive for secondary recovery
US3599715 *Feb 18, 1970Aug 17, 1971Marathon Oil CoUse of surfactant foam for recovery of petroleum
US3648772 *Aug 19, 1970Mar 14, 1972Marathon Oil CoMiscible-type recovery process using foam as a mobility buffer
US3759325 *Jun 24, 1971Sep 18, 1973Marathon Oil CoFoam for secondary and tertiary recovery
US4301868 *Oct 15, 1979Nov 24, 1981Petrolite CorporationMethod using hydrocarbon foams as well stimulants
US4624314 *Jun 3, 1985Nov 25, 1986Amerigo Technology LimitedModified waterflood technique for enhanced hydrocarbon recovery from argillaceous subterranean reservoirs
US4828029 *Dec 14, 1987May 9, 1989Irani Cyrus AEnhanced oil recovery, cosolvents, carobn dioxide, nitrogen, light hydrocarbons
US6024167 *May 15, 1998Feb 15, 2000Cyrus A. IraniTransporting waterflood mobility control agents to high permeability zones
Classifications
U.S. Classification166/270.2
International ClassificationC09K8/594, C09K8/58
Cooperative ClassificationC09K8/594
European ClassificationC09K8/594